905D95002G
REGION 5
Risk Assessment for the Waste Technologies Industries (WTI)
Hazardous Waste Incinerator Facility (East Liverpool, Ohio)
DRAFT — DO NOT CITE OR QUOTE
Volume VII:
ACCIDENT ANALYSIS:
SELECTION AND ASSESSMENT OF POTENTIAL RELEASE SCENARIOS
Prepared with the assistance of:
A.T. Kearney, Inc. (Prime Contractor: Chicago, IL);
with Subcontract support from: ENVIRON Corp. (Arlington, VA), Midwest Research Institute (Kansas City, MO)
and EARTH TECH, Inc. (Concord, MA) under EPA Contract No. 68-W4-0006
NOTICE: THIS DOCUMENT IS A PRELIMINARY DRAFT.
It has not been formally released by the U.S. Environmental Protection Agency as
a final document, and should not be construed to represent Agency policy.
It is being circulated for comment on its technical content.
-------
VOLUME VH
ACCIDENT ANALYSIS: SELECTION AND ASSESSMENT OF
POTENTIAL RELEASE SCENARIOS
CONTENTS
I. INTRODUCTION 1-1
A. General Methodology 1-1
B. U.S. EPA/FEMA/DOT Approach to Hazard Analysis 1-2
1. Hazards Identification 1-4
2. Vulnerability Analysis 1-5
3. Risk Analysis 1-6
C. Previous Accident Analyses for the WTI Facility 1-9
D. History of Emergency Incidents Reported at Commercial
Incineration Facilities in the United States 1-10
II. IDENTIFICATION OF ACCIDENT SCENARIOS II-1
A. Methodology II-l
B. Initial Identification of Accident Scenarios II-l
C. Selection of Accident Scenarios for Quantitative
Consequence Evaluation II-6
1. On-Site Spill II-6
2. On-Site Fire 11-10
3. On-Site Mixing of Incompatible Wastes 11-12
4. Off-Site Tanker Truck Spill 11-14
5. Off-Site Tanker Truck Spill with Fire 11-16
D. Summary of Results and Key Assumptions 11-16
III, CHEMICALS OF POTENTIAL CONCERN III-l
A. Methodology III-l
B. Preliminary Identification of Chemicals of Potential Concern III-l
C. Selection of Specific Chemicals for Each Accident Event III-5
1. On-Site Spill ffl-5
2. On-Site Fire ffi-7
3. On-Site Mixing of Incompatible Wastes III-8
4. Off-Site Tanker Truck Spill III-9
5. Off-Site Tanker Truck Spill with Fire III-9
D. Summary of Results and Key Assumptions III-9
IV. CHARACTERIZATION OF ACCIDENTAL RELEASES IV-1
A. Methodology IV-1
B. Chemical-Specific Emissions Rate Calculations IV-1
1. On-Site Spill IV-1
2. On-Site Fire IV-3
Volume VII External Review Draft
-i- Do Not Cite or Quote
-------
CONTENTS
(continued)
3. On-Site Mixing of Incompatible Wastes . IV-5
4. Off-Site Tanker Truck Spill IV-5
5. Off-Site Tanker Truck Spill with Fire IV-6
C. Summary of Results and Key Assumptions IV-6
V. ATMOSPHERIC DISPERSION MODELING V-l
A. Model Selection V-l
B. Meteorological Conditions V-l
1. Typical Conditions V-2
2. Conservative Conditions V-2
3. Calm/Inversion Conditions . V-3
C. Summary, of Results and Key Assumptions V-4
VI. SEVERITY OF CONSEQUENCES AND PROBABIUTY
OF OCCURRENCE VI-1
A. Severity of Consequences VI-2
1. On-Site Spill VI-2
2. On-Site Fire VI-4
3. On-Site Mixing of Incompatible Wastes VI-5
4. Off-Site Spill VI-6
5. Off-Site Fire VI-7
B. Probability of Occurrence VI-9
1. On-Site Events VI-9
2. Off-Site Events VI-12
C. Summary of Results and Key Assumptions VI-14
VII. UNCERTAINTIES VIM
A. Toxicity Evaluation VII-1
B. Exposure Assessment VII-1
1. Scenario Uncertainty VII-2
2. Parameter Uncertainty VII-3
3. Model Uncertainty Vtt-4
C. Sensitivity Analyses VII-5
1. Effect of Mitigation Measures VII-5
2. Effect of Averaging Time VII-8
3. Effect of Using LOCs to Estimate Downwind
Distance VII-10
Volume VII External Review Draft
-ii- Do Not Cite or Quote
-------
CONTENTS
(continued)
VIII. SUMMARY AND CONCLUSIONS
IX. REFERENCES
Page
VHI-1
IX-1
TABLES
Table 1-1: Accident Scenarios Evaluated in the WTI Credible Event
Analysis 1-12
Table 1-2: Results of the Report on Emergency Incidents at Hazardous Waste
Incinerators and Commercial Treatment, Storage, and Disposal
Facilities (TSDFs) 1-13
Table II-1: Partial List of Passive Mitigation Features at the WTI Facility 11-17
Table II-2: Preliminary List of Potential Accident Scenarios at WTI 11-18
Table II-3: WTI Pure Protection Systems 11-23
Table II-4: Distribution of Cargo Losses from Full Size Tankers
During Highway Transit in the U.S. from 1971 to October
1986 11-24
Table II-5: Scenarios Selected for Quantitative Evaluation 11-25
Table II-6: Key Assumptions Made in the Identification of
Accident Scenarios 11-26
Table III-l: Summary of Chemicals of Potential Concern for
Short-Term Exposures 111-10
Table III-2: Constituents Received hi Largest Quantities hi Pumpable Waste
at the WTI Facility 111-17
Table III-3: Hydrogen Chloride and Phosgene Formation from Decomposition of
Chlorinated Hydrocarbons hi Contact with Flame III-18
Table III-4: Wastes and Chemicals Evaluated III-19
Table III-5: Key Assumptions Made hi Selecting Chemicals of
Potential Concern 111-20
Table IV-1: Chemical-Specific Emission Rates IV-7
Table IV-2: Key Assumptions Made in Estimating Chemical
Emission Rates IV-8
Table V-l: Stability Wind Speed Combinations Used to Determine
"Conservative" Meteorological Conditions V-5
Table V-2: Summary of Downwind Air Concentrations for the On-Site
Spill Scenario V-6
Table V-3: Summary of Downwind Ah* Concentrations for the On-Site
Mixing of Incompatible Wastes Scenario V-7
Table V-4: Summary of Downwind Air Concentrations for the Off-Site
Spill Scenarios V-8
Volume VH
-Ill-
External Review Draft
Do Not Cite or Quote
-------
CONTENTS
(continued)
Table V-5:
Table V-6:
Table
Table
Table
Table
Table
Table
Table
Table
Table
Table
Table
Table
Table
V-7:
VI-1:
VI-2:
VI-3:
VI-4:
VI-5:
VI-6:
VI-7:
VI-8:
VI-9:
VI-10:
VI-11:
VI-12:
Table VI-13:
Table VI-14:
Table VII-1:
Table VII-2:
Table VII-3:
Table VIM:
Table VH-5:
Table VII-6:
Table VII-7:
Table VII-8:
Table VII-9:
Table VH-10:
Table Vffl-1:
Table VIII-2:
Table VIII-3:
Summary of Downwind Air Concentrations for the On-Site Fire
Scenario
Summary of Downwind Air Concentrations for the Off-Site Fire
Scenarios
Key Assumptions Made in Dispersion Modeling
Criteria Used in Ranking the Severity of Consequence
Criteria Used in Ranking Probability of Occurrence
Severity of Consequence for On-Site Scenarios
Severity of Consequence for Off-Site Scenarios
Consequence Assessment, On-Site Spill
Consequence Assessment, On-Site Fire
Consequence Assessment, On-Site Mixing of Incompatible Wastes
Consequence Assessment, Off-Site Spill
Consequence Assessment, Off-Site Fire
Probability of Occurrence for On-Site Scenarios
Probability of Occurrence for Off-Site Scenarios
Severity of Consequence and Probability of Occurrence
Results for On-Site Scenarios
Severity of Consequence and Probability of Occurrence
Results for Off-Site Scenarios
Key Assumptions Made in Ranking of Accident Events
Consequence Assessment, On-Site Spill with Mitigation
Consequence Assessment, On-Site Fire with Mitigation
Consequence Assessment, On-Site Mixing of Incompatible Wastes
with Mitigation
Results of Averaging Time Sensitivity Analysis
IDLH and LOG Values Used for Chemicals Evaluated hi the
Accident Analysis
Summary of Downwind Distance to LOC, On-Site Spill
Summary of Downwind Distance to LOC On-Site Fire
Summary of Downwind Distance to LOC, On-Site Mixing
of Incompatible Wastes
Summary of Downwind Distance to LOC Off-Site Spill
Summary of Downwind Distance to LOC Off-Site Fire
Probability/Severity Matrix - Typical Meteorological Conditions
Probability/Severity Matrix - Conservative Meteorological Conditions
Probability/Severity Matrix - Calm/Inversion Meteorological
Conditions
V-9
V-10
V-ll
VI-16
VI-17
VI-18
VI-19
VI-20
VI-21
VI-22
VI-23
VI-24
VI-25
VI-26
VI-27
VI-28
VI-29
VII-12
VH-13
VII-14
VII-15
VII-16
VII-17
VII-18
VII-19
VII-20
VII-21
VIII-3
vm-4
VIII-5
Volume VH
-IV-
External Review Draft
Do Not Cite or Quote
-------
CONTENTS
(continued)
Page
FIGURES
Figure H-l: WIT Site Plan H-27
Figure n-2: Local Access Route n-28
Figure H-3: Off-Site Spill Area H-29
Figure IV-1: Location for the Off-Site Spill IV-9
Figure VDI-1: Illustrative Accident Frequency/Severity Screening Matrix VHI-6
APPENDICES
Appendix VII-1: Incidents Reported at the WIT Facility and Comparable Facilities
Appendix Vn-2: Ranking of Chemicals of Potential Concern
Appendix Vn-3: Accidental Release Modeling
Appendix VH-4: Atmospheric Dispersion Modeling
Appendix VII-5: Off-Site Accident and Spill Frequency Analysis
Volume VII External Review Draft
-V- Do Not Cite or Quote
-------
I. INTRODUCTION
A. General Methodology
The WTI Risk Assessment includes an analysis of potential human health effects caused
by accidents that may occur during operation of the WTI facility. The approach for
conducting this analysis has been developed based on guidance published by the United States
Environmental Protection Agency (e.g., U.S. EPA 1987; 1995a) and other agencies, such as
the U.S. Federal Emergency Management Agency (FEMA 1993). The primary objective of
the Accident Analysis is to assess the potential for human health effects associated with
general types or classes of accidents that could occur at the WTI facility.
The WTI Accident Analysis also addresses comments from the independent peer review
of the WTI Phase II Project Plan (U.S. EPA 1993a). During the peer review, concerns were
raised regarding health impacts associated with chemical releases that could occur as a result
of on-site and off-site accidents, particularly given the proximity of the WTI facility to
schools and residences (U.S. EPA 1994a).
The data base for evaluating the human health risks posed by low frequency accidents at
hazardous waste management facilities is limited. Due to this limited data base, there is
significant uncertainty in conducting a quantitative analysis of risks posed by accidents at the
WTI facility. The Accident Analysis has, therefore, been developed based on scientific
judgment as well as available quantitative and qualitative information, an approach consistent
with the U.S. EPA's Accidental Release Prevention Requirements: Risk Management
Programs Under Clean Air Act Section 112(r)(7)', Proposed Rule (U.S. EPA 1995a) and
Technical Guidance for Hazards Analysis: Emergency Planning for Extremely Hazardous
Substances (U.S. EPA 1987).
The Accident Analysis for the WTI facility evaluates the potential for acute health effects
that may result from short-term (i.e., less than 24 hour) exposures of individuals located
within the immediate vicinity of the WTI facility. Of primary interest in the Accident
Analysis are the potential health affects associated with events which could have significant
short-term off-site consequences, but generally do not have a high probability of occurring.
In addition to these conservative scenarios, more typical events with a greater likelihood of
occurrence but a lower probability of causing adverse off-site health effects are also
examined. For both conservative and typical accident scenarios, a range of meteorological
Volume VII External Review Draft
1-1 Do Not Cite or Quote
-------
conditions (including atmospheric inversions) are evaluated, and the effect of emergency
response measures is assessed.
Consistent with the peer review comments, both on-site and off-site accidents are
included hi the analysis. For the on-site accident scenarios, the off-site distance over which
human health effects might be anticipated is estimated. The distance over which health
effects may occur in the event of an off-site transportation accident along the local access
roads to the facility is also identified. In determining the distance over which effects may
occur, inhalation is expected to be the primary route of short-term exposure for the off-site
community. While direct dermal exposure may also be of concern, exposures through
inhalation are predicted to occur over a larger area, and be more likely to result hi adverse
health effects. Furthermore, this analysis focuses on the short-term, direct exposure to
accidental releases, rather than longer-term, indirect exposures that might occur from
contamination caused by an accident.
Given that the focus of this assessment is the adequacy of existing design and operation
features in protecting the off-site community, risks to on-site workers are not evaluated.
Furthermore, as discussed hi U.S. EPA guidance (U.S. EPA 1992a), ecological assessments
typically focus on risks to ecological communities, rather than risks to individual receptors.
Most plausible accident scenarios would affect relatively small areas (i.e., within 5 miles of
the facility), and thus are unlikely to affect entire ecological communities. Thus, potential
ecological risks associated with facility accidents are not evaluated.
Many different types of events, or combination of events, could lead to the general
classes of accidents evaluated hi this study. Thus, a rigorous evaluation of the causes of
specific accident scenarios, based on fault-tree analyses or other detailed techniques, has not
been performed. Instead, probabilities of occurrence of the various classes of accident events
considered are estimated using the semi-quantitative methods presented hi technical guidance
for hazards analysis by U.S. EPA (1987) and FEMA (1993). This approach is consistent
with U.S. EPA's Proposed Rule for Accidental Release Prevention Requirements (U.S. EPA
1995a).
B. U.S. EPA/FEMA/DOT Approach to Hazards Analysis
The Emergency Planning and Community Right-to-Know Act (EPCRA) of 1986, also
known as Title III of the Superfund Amendments and Reauthorization Act (SARA), requires
local emergency planning committees (LEPCs) to develop emergency response plans for
facilities hi the event of an emergency. Site-specific hazards analysis is one tool LEPCs can
use to better understand the potential risks posed by airborne releases of extremely hazardous
substances (EHSs) from a facility. An EHS is defined by U.S. EPA as a chemical with high
acute lethality, having the potential for causing death hi unprotected populations after
Volume VII External Review Draft
1-2 Do Not Cite or Quote
-------
relatively short exposure periods at low doses (U.S. EPA 1987). More than 360 chemicals
listed under Title III of SARA have been identified by U.S. EPA as EHSs, primarily on the
basis of acute toxicity (U.S. EPA 1987). This list of EHSs was considered in selecting
chemicals of potential concern hi the WTI Accident Analysis. Additional chemicals of
potential concern hi the WTI Accident Analysis were identified through a review of
information on wastes projected to be received during the first year of WTI operations.
To assist hi the development of comprehensive emergency plans, U.S. EPA,'FEMA and
the United States Department of Transportation (U.S. DOT) jointly issued the Technical
Guidance for Hazards Analysis (U.S. EPA 1987) outlining a three-step "hazards analysis"
process for identifying potential hazards facing a community with respect to accidental
releases of EHSs. This general approach was also adopted hi the FEMA Handbook of
Chemical Hazard Analysis Procedures (FEMA 1993). The process described hi U.S. EPA
(1987) consists of the following three components:
• Hazards Identification, involving the collection and review of specific information on
situations that have the potential for causing injury to life or damage to property and
the environment due to a hazardous materials spill or release (e.g., chemical
identities; location of storage and use; quantities stored or used; nature of the
hazard).
• Vulnerability Analysis, involving the identification of areas hi the community that
may be affected or exposed (vulnerable zones); individuals hi the community who
may be subject to injury or death from certain specific hazardous materials
(including sensitive human subpopulations); and facilities, property or environment
that may be susceptible to damage should a hazardous materials release occur
(critical facilities and environment).
• Risk Analysis, involving an assessment of the likelihood (probability) that an
accidental release of a hazardous material might occur, and the severity of
consequences that might result from the release. Combining the accident probability
analysis with measures of predicted consequences provides an estimation of the
overall risk, which can be used for prioritization and planning purposes.
The intent of the Technical Guidance for Hazards Analysis (U.S. EPA 1987) is to assist with
the development of a community-scale emergency plan. Other guidance has been used as
necessary to supplement the Technical Guidance for Hazards Analysis as described
throughout this report. In developing a methodology for the Accident Analysis for the WTI
Volume VII External Review Draft
1-3 Do Not Cite or Quote
-------
facility, the hazards analysis process has been adopted as a general framework, as described
below.
1. Hazards Identification
Hazards identification, the first step in hazards analysis, is the process of collecting
and reviewing information on:
• the types and quantities of hazardous materials at the facility;
• the locations and conditions of specific areas within the facility where hazardous
materials are handled, stored, used, treated or disposed; and
• routes used for transporting hazardous materials to, from and within the facility.
From this information, it is possible to develop potential accident scenarios (both on-site
and off-site) that might result in spills or releases that could lead to off-site exposures in
the surrounding community. Examples of on-site accident scenarios that might be
relevant for a hazardous waste facility include storage tank ruptures, process line
failures, fires hi storage tank areas, failures of transfer lines and hoses during off-loading
of tanker trucks, spills from off-loading tanker trucks, explosions during operation of a
combustion system, and failure of the air pollution control equipment. Off-site accident
scenarios that could be considered include chemical releases caused by collisions
involving tanker trucks or railcars hauling hazardous materials.
In the WTI Accident Analysis, the hazards identification process consists of the
following major elements:
• Identification of conservative and typical accident scenarios, based on a general
review of the facility layout, a site visit and an evaluation of reports on
accidents that have occurred at WTI and at comparable U.S. facilities. The
accident scenarios identified for the WTI facility are representative of categories
of accidents listed in FEMA (1993), and which could occur during the types of
activities performed at the facility.
• Review of chemicals of possible concern with regard to the identified accident
scenarios. Chemicals of possible concern are identified primarily through a
review of waste profiles received during WTI's first year of operation, acutely
hazardous wastes ("P" wastes) as defined hi 40 CFR §261.33(e), and hazardous
Volume VII External Review Draft
1-4 Do Not Cite or Quote
-------
substances listed under Section 112(r) of the Clean Ah- Act and Section 302 of
( EPCRA. Although "P" wastes are not currently received at the WTI facility,
these wastes are not prohibited by the permit.
• Compilation of acute toxicity criteria and physical/chemical data for the
chemicals of possible concern. For this analysis, predicted off-site
concentrations associated with selected accident scenarios relevant to the WTI
facility are compared to acute toxicity criteria known as "Immediately
Dangerous to Life or Health" (IDLH) values. IDLH values are developed by
the National Institute for Occupational Safety and Health (NIOSH), and
represent the maximum concentration of a chemical hi ah" from which an
individual could escape within 30 minutes without experiencing any escape-
impairing or irreversible health effects (FEMA 1993). The IDLH values
published by NIOSH were originally developed to be protective for healthy
adult male workers, and have not been adjusted to account for the heterogeneous
population (e.g., children, elderly, ) who might be exposed to chemicals hi an
event with off-site consequences. In some cases individuals in the general
population might require a longer escape tune and/or be more sensitive to the
( chemical exposure compared to healthy adult male workers (U.S. EPA 1987).
^ Therefore, as a sensitivity analysis, predicted off-site concentrations were also
compared to "Levels of Concern" (LOCs), which are generally more
conservative than the IDLH values. LOCs are defined by U.S. EPA (1987) to
be the "concentrations of extremely hazardous substances hi air above which
there may be serious irreversible health effects or death as a result of a single
exposure for a relatively short period of tune." LOG values are usually, but not
always, equal to the IDLH divided by a factor of ten.
Each of the above steps is described hi greater detail in subsequent chapters of this
volume of the WTI Risk Assessment.
2. Vulnerability Analysis
According to the Technical Guidance for Hazards Analysis document (U.S. EPA
1987), the vulnerability analysis involves the identification of areas of the community
surrounding a facility that may be affected in the event of a hazardous release, and the
identification of specific subpopulations within this area that may be of particular
( concern. The vulnerability analysis also includes an evaluation of the consequences of
v ^ an accident.
Volume VII External Review Draft
1-5 Do Not Cite or Quote
-------
In the WTI Accident Analysis, the methodology for the consequence analysis
consists of the following steps:
• selecting, on the basis of comparison to published acute exposure levels, specific
waste materials and chemical constituents to characterize the potential
consequences of each accident scenario. Those substances with the greatest
hazard, based.on acute toxicity, quantity, and release potential are selected for
further evaluation, as these substances would generate the greatest impact if they
were carried downwind in sufficient concentrations;
• estimating the chemical constituent release rates for each accident scenario;
• calculating the atmospheric dispersion of released materials or propagation of
energy release (e.g., heat effects) to receptors; and
• comparing the resultant modeled exposure levels to published acute exposure
levels as a measure of the area over which adverse health effects might occur.
Specific subpopulations within the community that may be at particular risk are
identified. A number of residences and an elementary school (East Elementary School)
are located approximately 1,000 feet north of the facility. This area is comprised of
single-family homes, the elementary school and a business college. The area due west
of the facility (approximately one-quarter mile) is also residential/commercial. Based on
the peer review Work Group comments (U.S. EPA 1994a), and observations made
during a site visit, subpopulations of special concern include children in the nearby
school, as well as residents living near the site or along the local access route.
3. Risk Analysis
Risk analysis, the final step in hazards analysis, provides an assessment of the
likelihood that an accidental release of a hazardous material will occur, a semi-
quantitative assessment of the associated consequences and the potential effect of
emergency response measures. Considered together, the outcomes of the accident
probability analysis and the consequence analysis can provide an overall measure of the
risk. This overall measure of risk can be expressed qualitatively, semiquantitatively or
quantitatively, depending on the objectives of the analysis and the nature of the available
data.
Volume VII External Review Draft
1-6 Do Not Cite or Quote
-------
As discussed previously, because of the limited availability of quantitative data, the
probability analysis consists primarily of a semi-quantitative evaluation of the likelihood
of an event occurring. The Technical Guidance for Hazards Analysis document (U.S.
EPA 1987) identifies the following guidelines as examples for evaluating accident
probability:
Low Probability of occurrence considered unlikely during the expected
lifetime of the facility, assuming normal operation and maintenance.
Medium Probability of occurrence considered possible during the expected
lifetime of the facility.
High Probability of occurrence considered sufficiently high to assume event
will occur at least once during the expected lifetime of the facility.
In addition to these qualitative guidelines, FEMA (1993) has also developed five
categories hi cases where more quantitative information is available on accident
frequency:
Common Expected to occur one or more times each year on average.
Likely Expected to occur at least once every 10 years on average according to
available statistics.
Reasonably
Likely Predicted to occur between once every 10 years and once every 100
years on average.
Unlikely Predicted to occur between once every 100 years and once every 1,000
years on average hi a specific locale.
Very
Unlikely Predicted to occur less than once in 1,000 years.
Based on the guidelines presented hi FEMA (1993), common and likely accidents
may be equated to "high"; reasonably likely and unlikely accidents to "medium"; and
very unlikely accidents to "low" probability categories, as defined by U.S. EPA (1987).
Volume VII External Review Draft
1-7 Do Not Cite or Quote
-------
The following qualitative guidelines are provided by U.S. EPA (1987) as an
example to evaluate the severity of consequences:
Low Chemical is expected to move into the surrounding environment in
negligible concentrations. Injuries expected only for exposure over
extended periods or when individual personal health conditions create
complications.
Medium Chemical is expected to move into the surrounding environment in
concentrations sufficient to cause serious injuries and/or deaths unless
prompt and effective corrective action is taken. Death and/or injuries
expected only for exposure over extended periods or when individual
personal health conditions create complications.
High Chemical is expected to move into the surrounding environment in
concentrations sufficient to cause serious injuries and/or deaths upon
exposure. Large numbers of people expected to be affected.
FEMA (1993) presents a four tier system for classifying the consequences of
accident scenarios:
Minor
Moderate
Major
Low potential for serious human injuries; no potential for human
fatalities; and no need for a formal evacuation, although the public
may be cleared from the immediate area of the spill or discharge.
Up to 100 potential human injuries requiring medical treatment or
observation; up to 10 potential human fatalities; or evacuation of
up to 2,000 people.
Up to several hundred potential human injuries requiring medical
treatment or observation; up to 100 potential human fatalities; or
evacuation of up to 20,000 people.
Catastrophic More than 300 potential human injuries requiring formal medical
treatment; more than 100 potential human fatalities; or evacuation
of more than 20,000 people.
Volume VII
1-8
External Review Draft
Do Not Cite or Quote
-------
Although not explicitly indicated by FEMA (1993), it is reasonable to equate minor
accidents to "low"; moderate accidents to "medium"; and major and catastrophic
accidents to "high" severity of consequence categories, as defined by U.S. EPA (1987).
The accident scenarios identified for the WTI facility are evaluated to determine
whether any have likelihood-consequence rankings of high-high, high-medium, medium-
high, or medium-medium. Based on the Technical Guidance document (U.S. EPA
1987), such events should be evaluated to determine whether additional mitigation or
emergency response measures are feasible. FEMA (1993) suggests that scenarios with
likelihood-consequence ranking of low-high and/or high-low also be included in
evaluating emergency planning.
C. Previous Accident Analyses for the WTI Facility
An analysis of the potential off-site consequences of accidents at the WTI facility was
previously performed by WTI to address the implications for immediate response actions.
The results of this analysis were summarized in a report entitled Waste Technologies
Industries Credible Event Analysis for Emergency Planning, prepared by SE Technologies,
Inc. (1992). The objectives stated hi the report are to identify credible accident scenarios,
assess then" impact hi terms of release of hazardous agents into the environment, and identify
a maximum credible event that could be used as a reasonable basis for on-site and off-site
emergency planning. The WTI Credible Event Analysis does not include the preparation of a
comprehensive list of all potential accident scenarios, or the calculation of the relative
probabilities of various accidents occurring.
The final WTI Credible Event Analysis incorporated review comments provided by Ohio
State Emergency Management Agency, Ohio Department of Public Health, Ohio
Environmental Protection Agency, Columbiana County (Ohio) Local Emergency Planning
Committee, and the Emergency Management Agencies of Columbiana County (Ohio),
Hancock County (West Virginia), and Beaver County (Pennsylvania). The scenarios used in
the final report were selected during a meeting held on January 17, 1992 in Columbus, Ohio
between WTI, SE Technologies, Inc., Ohio Environmental Protection Agency, Ohio
Department of Public Health, and Ohio Emergency Planning Agency.
The Credible Event Analysis evaluates eight accident scenarios. Of the eight scenarios,
one (a release of 20,000 Ib of ammonia), is no longer relevant to the WTI facility due to a
change in proposed facility design and operation. Of the seven remaining scenarios, five are
predicted to involve off-site hazards, as summarized hi Table 1-1. The event determined by
WTI to have the greatest potential off-site consequences involves mixing of incompatible
wastes, which is predicted to result hi possible exceedances of the LOG for chlorine up to
7,000 m downwind. Based on these results, the report concludes that it is prudent to plan
Volume VII External Review Draft
1-9 Do Not Cite or Quote
-------
for public protection actions within approximately a 5-mile (8,000 m) radius of the WTI site.
While this is not the area over which worst-case accident scenarios would be confined, it is
identified as the area most likely to be affected hi an extreme credible accident event (SE
Technologies 1992).
D. History of Emergency Incidents Reported at Commercial Incineration Facilities in
the United States
The U.S. EPA (1995b) has compiled a review of reported emergency incidents at
hazardous waste incinerators and commercial treatment, storage and disposal facilities
(TSDFs) regulated under the Resource Conservation and Recovery Act (RCRA).
Information on incidents that were reported at 11 commercial hazardous incinerators, 10
noncommercial incinerators and 23 other commercial TSDFs between 1977 .and May 1995
are presented hi U.S. EPA (1995b), and summarized hi Tables 1 and 2 of Appendix VII-1.
The information included hi U.S. EPA (1995b) was compiled by contacting combustion
experts and permit writers hi each of the 10 U.S. EPA Regional offices, as well as
individuals within state regulatory agencies. Since U.S. EPA does not maintain a central
data base of information on emergency incidents, some information is based on the
recollections of U.S. EPA and State staff. Additional limitations of the study include the
lack of information on the reporting period for the individual facilities, and mat the
information is received hi response to a voluntary survey.
In the U.S. EPA (1995b) report, an emergency incident is defined as "a hazardous waste
spill, unauthorized release, fire, or explosion." Not all incidents identified hi the report
resulted hi releases of hazardous waste to the environment. Furthermore, many of the
incidents reported hi U.S. EPA (1995b) occurred before facilities received RCRA permits,
and full RCRA safeguards were, therefore, not necessarily hi effect. The results of the U.S.
EPA (1995b) report are summarized on Table 1-2.
A total of 50 emergency incidents, as defined by U.S. EPA, were reported at the
hazardous waste incinerators identified hi the study. For commercial hazardous waste
incinerators only, 24 emergency incidents at 11 facilities were reported, with 10 of these
incidents involving a release of hazardous waste. It should be noted that no emergency
incidents have been reported at 15 commercial incineration facilities (including WTI), so
these facilities were not discussed hi U.S. EPA (1995b). The combustion facilities with no
reported emergency incidents are included hi Table 1 hi Appendix VII-1 to facilitate
evaluation of emergency incidents relative to the number of facilities operating hi the United
States.
The total operating time for the 26 commercial incinerators during the tune period
considered by the study is approximately 250-300 years. This operating tune total is likely
Volume VII External Review Draft
I-10 Do Not Cite or Quote
-------
to be an underestimate, since no information is available for operations before 1981, and no
operating dates were available for two facilities. Based on 10 reported emergency incidents
involving hazardous waste over a total of 250-300 years of operation, approximately one
emergency incident involving a hazardous waste release has been reported for every 25-30
years of operation for the commercial incinerators. None of the 10 reported incidents
involving releases of hazardous waste resulted hi a fatality or serious injury hi off-site
communities, although on-site worker injuries and fatalities have occurred (U.S. EPA
1995b). Based on the lack of fatalities or serious off-site injuries associated with reported
accidents at commercial hazardous waste combustion units, the probability of an event having
moderate, major or catastrophic consequences (i.e., a release of hazardous waste resulting hi
serious off-site injuries or fatalities) would be classified as unlikely, or very unlikely over the
facility lifetime, using the definitions presented hi FEMA (1993). The probability of
occurrence of an event having minor consequences (i.e., a release of hazardous waste
resulting hi minor or no off-site effects) would be classified as reasonably likely over the
facility lifetime, according to FEMA (1993).
Volume VII External Review Draft
1-11 Do Not Cite or Quote
-------
TABLE 1-1
Accident Scenarios Evaluated in the WTI Credible Event Analysis1
Scenario
1. On-site spill of 55 gallons of liquid
waste containing 10% methyl acrylate
(volatile release).
2. On-site spill of 50 gallons of liquid
waste containing 40% acrolein (volatile
release).
3. On-site spill of 5,000 gallons of liquid
waste containing 85 % toluene (volatile
release).
4. On-site spill of 5,000 gallons of liquid
waste containing 85% toluene (fire).
5. On-site spill of 50 gallons of liquid
waste containing 20% acetone (volatile
release).
6. On-site mixing of incompatible waste,
resulting in 10,000 Ib release of
chlorine gas over 60 minutes.
7. On-site spill of 5,000 gallons of liquid
waste containing methyl ethyl ketone
(MEK) (volatile release).
8. On-site release of 20,000 Ib. of
ammonia over 60 minutes.2
C onsequence
1. Exceedance of LOG up to 16 meters
(m) downwind; no off-site hazard
anticipated.
2. Exceedance of LOG up to 900 m
downwind.
3. Exceedance of LOG up to 70 m
downwind.
4. Damage from explosion of vapor cloud
could extend up to 375 m; detonation
of fireball could result in an injury
zone radius of 190 m and a fatality
zone radius of 90 m.
5. Exceedance of LOG up to 10 m
downwind; no off-site hazard
anticipated.
6. Exceedance of LOG up to 7,000 m
downwind, under early morning
inversion conditions.
7. Exceedance of LOG up to 335 m
downwind.
8. Exceedance of LOG up to 6,300 m
downwind.
Notes:
Source: SE Technologies (1992)
This scenario is no longer relevant to the WTI facility due to a change in facility
design and operation.
Volume VII
1-12
External Review Draft
Do Not Cite or Quote
-------
TABLE 1-2
Results of the Report on Emergency Incidents at Hazardous Waste Incinerators
and Commercial Treatment, Storage, and Disposal Facilities (TSDFs)
Number of Facilities Reporting Incidents'
total Number of Incidents Reported
Number of Incidents Involving a Release of
Hazardous Waste to the Environment2
Hazardous Waste
Combustion
Facilities
21
50
21
Commercial
Hazardous Waste
Combustion Facilities
11
24
10
Other
Commercial
TSDFs
23
48
27
Notes:
1 Count adjusted from U.S. EPA (1995b) because (a) there was a typographical error under Region V, in
which there are 5 (not 6) combustion faculties and (b) classification of Rollins Environmental Services in
Logan Township, New Jersey, as an incinerator and not a TSDF, per Appendix 1 of U.S. EPA (1995b).
2 Counts in this row are derived from the summary table in U.S. EPA (1995b), which does not specify the
criteria used to classify "a release of hazardous waste to the environment." Based on information provided
in U.S. EPA (1995b) probable incidents at combustion facilities were identified; of these, 10 occurred at
commercial facilities.
Volume VII
1-13
External Review Draft
Do Not Cite or Quote
-------
II. IDENTIFICATION OF ACCIDENT SCENARIOS
A. Methodology
A first step in performing the Accident Analysis for the WTI facility is to identify
accident scenarios that may have the potential to cause adverse human health effects in the
surrounding community. Such scenarios are identified through a general review of the
design and operation of the WTI facility, and accident events that have occurred at WTI or
comparable U.S. facilities. Given the large number of hypothetical scenarios of potential
concern, a subset of accident events is selected for quantitative analysis. These events are
chosen to represent general types or classes of accidents that might occur, as identified iii
FEMA (1993), such as a spill or fire.
This chapter provides an overview of the process used to identify possible accident
scenarios, and to select the specific scenarios to evaluate in the Accident Analysis.
B. Initial Identification of Accident Scenarios
The initial identification of accident scenarios involves the following steps:
• A general background review of the facility design and layout, along with
information on operating procedures and controls. Available accident data reported
at WTI and at facilities comparable to WTI are also reviewed.
• Development of a preliminary list of accident events based on the background
review.
• A site visit to the WTI facility by the U.S. EPA Accident Analysis team to confirm
information gathered during the background review and observe actual facility
operations.
• Analysis of information gathered by the U.S. EPA Accident Analysis work group
resulted hi refinement of the preliminary list of accident scenarios and identification
of events of primary concern.
Volume VII External Review Draft
II-1 Do Not Cite or Quote
-------
The general background review of information relevant to accidents at the WTI facility
focuses on identifying areas where hazardous materials are transported, received, handled,
stored or treated. This involves a review of the permit and permit application for the WTI
facility, as well as a review of the facility plot plan. An overview of key accident prevention
emergency response features of the design and operation of the WTI facility, as presented in
WTI (1982) and WTI (1992), is provided below.
Fires and releases at the WTI facility are detected, monitored and controlled through a
computerized system that is run by the operator in the control room. Through a control
panel, the operator is able to monitor all process areas, thus assuring that they are
functioning normally. The operator is able to shut down facility processes and equipment,
including the electrical, heating, ventilation, air conditioning and exhaust systems, should a
problem arise. The facility was designed for orderly shutdownin the event of an equipment
failure or power outage. An emergency power generator is designed to provide electricity
for electrical motors, emergency lighting, pumps, instruments, and controls essential to safe
plant operation.
According to WTI, the WTI facility was designed so that potential on-site spills would
be contained by a combination of sumps, drainage trenches, dikes, walls, curbs, speed
bumps, ramps, berms, and other contour features. Table II-1 presents a partial list of
passive mitigation features hi place at the WTI facility. In the event of a spill, inert or
absorbent materials will reportedly be placed in the path of the release to confine the release
to as small an area as possible. Materials and equipment that come in contact with waste
have been selected to withstand chemical and physical attack. Material thicknesses equal to
or exceeding the minimum required industry standards or codes have been specified to
provide protection against both corrosion and erosion. Concrete surfaces have been covered
or treated, where appropriate, to resist chemical attack. Incompatible wastes are segregated
into separate containment areas.
Where possible, piping is visible and easily accessible. Visual inspections are conducted
by WTI personnel at least once per day for the tanks and blending vessels, ventilation and
exhaust systems; instruments and controls; surfaces and sumps in the unloading, loading, and
sampling areas; processing and treatment areas; and paved and concrete surfaces.
Inspections of pumps and fans; electrical motors; and the emergency electric power generator
are conducted at least once per week. Additionally, more extensive inspection procedures
are conducted on a regular basis.
All buildings where hazardous waste is handled are protected by automatic fire
suppression systems designed to extinguish fires and keep fires from spreading. For certain
buildings or areas, this includes a foam system which is generally regarded as effective in
extinguishing and preventing the re-ignition of a wide variety of chemical fires. These
Volume VII External Review Draft
H-2 Do Not Cite or Quote
-------
systems are reportedly designed, constructed, equipped, and installed according to all
applicable codes and regulations, including those promulgated by the National Fire Protection
Association (NFPA), Factory Mutual, the Ohio Fire Code, and the Ohio Basic Building
Code. In addition, fire suppression systems have been inspected and certified by the East
Liverpool Fire Department. Alarms on the fire monitor are triggered automatically.
whenever one of the automatic sprinkler systems is activated or manually when one of the
fire alarm boxes located throughout the plant is activated.
Temperature, pressure, and fluid level data are available in the control room for each
enclosed tank, including the wastewater tanks and process water holding tanks. When pre-set
limits are reached, visual and audible alarms hi the control room will signal the operator that
a problem exists. In the case of a vessel or a tank being filled with a pump, the fluid level
control device will automatically deactivate the pump and close the intake valve whenever a
high level is indicated. Combustible gas detectors are present in sumps in the organic waste
tank farm to detect flammable vapors and thereby alert the operator to the potential for a
fire.
In addition to an assessment of the facility design and operation, the background review
includes an evaluation of the following:
• reported equipment and procedural failures at the WTI facility between June
1993 and February 1995, as summarized in Table 3 of Appendix VII-1
(Victorine 1995d).
• scenarios described hi two accident analyses previously performed for the WTI
facility — Credible Event Analysis for Emergency Planning (SE Technologies
1992) and WTI's Emergency Plan Exercise (Von Roll 1993).
• reported incidents at hazardous waste incinerators and treatment, storage and
disposal facilities (TSDFs) hi the United States, as compiled by U.S. EPA
(1995b). These incidents, which are summarized hi Table 3 of Appendix VII-1,
tend to be relatively high frequency, low consequence events — primarily minor
explosions hi incineration and air pollution control equipment. None of the
incidents reported hi U.S. EPA (1995b) resulted hi serious injuries or fatalities
off-site, although serious injuries and fatalities have occurred among on-site
workers. The results of the U.S. EPA (1995b) study were confirmed through a
review of incidents reported at TSDFs hi the U.S. EPA Accident Release
Inventory Program (ARIP) data base, which summarizes information on releases
which occurred from 1987 to early 1993 (Chung 1995).
Volume VII External Review Draft
II-3 Do Not Cite or Quote
-------
Based on the background review, a preliminary list of conservative on-site and off-site
candidate scenarios is developed for consideration in the WTI analysis (Table II-2). Many of
the scenarios are very similar, differing only hi the location of the accident and the quantities
of the chemicals involved. The potential accident scenarios for the WTI facility identified in
Table II-2 can be grouped into the following general categories:
• Spill or leak of liquid waste, followed by:
— evaporation and atmospheric dispersion of hazardous constituents; or
— fire with entrainment and dispersion of hazardous constituents, generation and
dispersion of hazardous products of combustion or incomplete combustion, or
boiling, vaporization and dispersion of hazardous constituents hi close proximity
to the fire.
• Mixing of incompatible wastes, followed by:
— venting and dispersion of gaseous reaction products; or
— bursting of tank or pipe and release of liquid waste.
• Explosion of tank or pipe (hydraulic or thermal over-pressure) with release of liquid
wastes.
• Failure of the air pollution control equipment.
• Release and dispersion of hazardous substances from incinerator due to a leak,
explosion or component failure.
• Transportation accidents, followed by a spill or leak.
Scenarios that involve fires or rapid gas generation may also involve explosions, depending
on the nature of the accident and waste.
Following the background review, these scenarios were further refined based on site
specific information resulting from a site visit by members of the U.S. EPA accident analysis
work group. Participating work group members included representatives of U.S. EPA
Region 5, the Office of Solid Waste and Emergency Response (OSWER) and the Chemical
Emergency Preparedness and Prevention Office (CEPPO). The primary objective of the site
visit was to examine potential accident scenarios hi the context of the WTI facility location,
layout and operational practices.
Volume VII External Review Draft
II-4 Do Not Cite or Quote
-------
Based on existing guidance, the review of accidents reported at WTI and comparable
facilities, a review of the design and operation of the WTI facility, the site visit, and
subsequent discussions within the U.S. EPA Accident Analysis team, the following general
scenarios are considered to be of primary concern:
• On-site spill
• On-site fire
• On-site mixing of incompatible wastes
• Off-site tanker truck spill
• Off-site tanker truck spill with fire
The criteria used hi selecting these general scenarios are: 1) potential for significant off-
site consequences, and 2) potential for occurring during the expected operating life of the
facility (30 years), based on available data. The on-site scenarios selected for the Accident
Analysis (spill, fire, and mking of incompatible waste) are consistent with those evaluated in
the WTI Credible Event Analysis (SE Technologies 1992). However, an ammonia release
evaluated by SE Technologies (1992) is no longer relevant due to changes hi the proposed
design and operation of the WTI facility. Furthermore, the Accident Analysis examined
several off-site scenarios not included hi the Credible Event Analysis.
Possible off-site impacts due to upset conditions and accidents occurring inside the
incinerator are judged to be of lesser concern than other types of facility accidents, based on
a review of the consequences of accidents which have been reported at hazardous waste
facilities (U.S. EPA 1995b) and other industrial facilities. The consequences of these types
of events relative to accidents involving waste storage, handling or transport are typically
lower, primarily because the quantity of waste being processed by the incinerator at any one
time is much less than the quantities that are stored, handled or transported. As a result,
accidents involving the storage, handling and transport of wastes would be expected to have
more severe off-site consequences than accidents directly involving the incinerator.
In assessing off-site accidents, this analysis considers waste transport through the local
community. Although it is theoretically possible hi the future for wastes to be received by
the WTI facility via truck or rail, local waste transport currently occurs by truck. Transport
via barge does not occur within the vicinity of the facility, and there are no plans for barge
transport hi the future. Rail transport represents a future option for the WTI facility, but
plans remain at the concept stage. Thus, the Accident Analysis evaluates the potential effects
of truck accidents only.
Specific accident events from Table II-2 within each of the five general scenario
categories are evaluated. Because many of the events within each general scenario category
Volume VII External Review Draft
II-5 Do Not Cite or Quote
-------
are similar in nature, a single conservative site-specific event within each category is selected
for quantitative evaluation. A more "typical" event, i.e., one with a higher likelihood of
occurrence than the conservative event, was also selected within each category. The five
conservative events and five typical events selected for quantitative evaluation and the criteria
for their selection are discussed below.
C. Selection of Accident Scenarios for Quantitative Consequence Evaluation
1. On-Site Spill
Spills could be caused by numerous situations, including leaks from drums that are
not hi good condition or are damaged; leaks from improperly packaged containers;
releases from tanks due to overfilling, faulty transfer lines or structural defects; releases
of the contents of tanker and trailer trucks from leaks or ruptures resulting from an on-
site accident; and releases caused by catastrophic events, such as a tornado. On-site
spills have been reported by U.S. EPA (1995b) at several commercial hazardous waste
TSDFs. Examples of some larger spills that have occurred include the following:
• In 1982, at the Laidlaw incineration facility in Roebuck, South Carolina, 3,000-
gallons of solvent spilled from a corroded pipe. A 6,000-gallon spill of maleic
anhydride from a storage tank was reported to have occurred at the same facility
in 1988.
• In 1985, at the CP Chemicals TSDF in Sumter, South Carolina, storage tank
valves reportedly were left open intentionally by two facility workers (both of
whom were later arrested), releasing 2,200 gallons of ammonia and 2,000
gallons of HC1.
• In 1989, a transfer line failure resulted hi a 9,600-gallon spill of wastewater
with solvents at the Oil and Solvent Process Company TSDF hi Azusa,
California. A transfer line failure also reportedly resulted hi a 30,000-gallon
spill of wastewater containing wood treating waste at the International Paper
TSDF hi Joplin, Missouri hi 1992.
At the WTI facility, a total of five spills of waste, all less than 20 gallons have been
reported since operations began in June 1993 (see Table 3 of Appendix VII-1).
Volume VII External Review Draft
H-6 Do Not Cite or Quote
-------
Spills that occur on-site may result in the formation of a liquid pool, the areal extent
and depth of which depends on the release rate and duration, as well as the presence of
any containment barriers (e.g., dikes, speed bumps, building walls, etc.) hi the spill
vicinity. If no containment barriers are present to limit the areal extent of the pool, it
can be assumed that the spill will spread to an area with a thickness of approximately
1 cm (U.S. EPA 1987; Moorhouse and Carpenter 1986). Following the release,
evaporation of the pool could result hi off-site exposure to the spilled chemicals. The
evaporation rate of chemicals from a liquid pool is determined primarily by the rate of
mass transfer as air flows over the surface of the pool. The mass transfer rate is, in
turn, determined largely by the wind speed, the vapor pressure of the spilled material
and the surface area of the pool.
Spills could occur at the WTI facility during waste handling, transfer and storage.
The WTI facility can store approximately 800,000 gallons of liquid waste hi two main
permitted storage areas: 1) the Organic Waste Tank Farm, and 2) the Container
Processing Building (WTI 1992). The Container Holding Area is allowed to store only
solid wastes.
Consistent with the objective of this analysis to evaluate credible events that are
expected to result hi the most potentially significant off-site consequences, three
conservative accident types are considered for quantitative analysis:
• A major spill within the indoor drum storage area of the Container Processing
Building. The total capacity of the area is approximately 500,000 gallons of
liquid waste hi drums. This corresponds to approximately 9,000 55-gallon
drums, which are stored hi twelve separate rows and placed in racks with three
vertical levels. The Container Processing Building is divided into two sections,
each having a secondary containment capacity that exceeds 10%, i.e., one-tenth,
of the maximum volume of waste that can be accumulated hi that area.
• A major spill in the indoor Organic Waste Tank Farm storage area. There is a
total capacity of approximately 300,000 gallons of waste hi the 16 large tanks in
this building, as well as a 20,000-gallon fuel tank. The Organic Waste Tank
Farm is divided into four sections, each having a secondary containment
capacity that exceeds the volume of the largest tank hi that area.
• A major spill outdoors due to an accident involving one full tanker truck, with a
capacity of 5,000 gallons of liquid waste. Locations where such an accident
could occur include the Truck Holding and Sampling Area, the Truck Unloading
Volume VII External Review Draft
II-7 Do Not Cite or Quote
-------
Station, and the paved area between the Truck Unloading Station and the Truck
Holding and Sampling Area (see Figure II-1).
Of these three conservative events, the outdoor spill involving a tanker truck in the
Truck Unloading Station is selected for quantitative evaluation in the Accident Analysis.
This event is selected for the following reasons:
• All three events could involve a spill of large quantities of liquid waste. The
composition of the waste could also be the same hi each event. While the two
indoor scenarios could conceivably result in larger volumes of spilled material,
the areas of the spills (and thus the hazardous waste constituent emission rates)
would be largely constrained by berms. For example, the Organic Waste Tank
Farm is divided into four containment areas of approximately 180 m2 each. An
outdoor spill from a tanker truck potentially could spread and cover a maximum
area of approximately 418 m2 due to the containment barriers. Thus, the area
of an outdoor spill, depending on its location, could be significantly larger than
the area of an indoor spill.
• For indoor spills that do not exceed the secondary containment capacities,
atmospheric emissions will occur primarily via volatilization. Such
volatilization would be reduced relative to outdoor spills due to lower air flow
rates over the surface of the pool. Furthermore, a significant portion of the
releases from an indoor spill would be expected to be contained within the
building. Because of this, outdoor spills are expected to have a greater potential
for substantial off-site impacts.
• A very large spill hi the Container Processing Building or the Organic Waste
Tank Farm could possibly spill over the containment barriers, leading to a
larger pool area. However, it is unlikely that such pools would be larger than
the pool size (418 m2) estimated for the outdoor tanker truck spill. Although
the containment volume for each building is smaller than the maximum storage
capacity, the containment volumes should be sufficient for containing spills most
likely to occur.
It should be emphasized that the event selected to evaluate the potential off-site
impacts of an on-site spill is judged to represent a "worst case" scenario. Thus, other
on-site spills, such as a leak from a transfer line, would be expected to have lower off-
Volume VII External Review Draft
H-8 Do Not Cite or Quote
-------
site consequences. To evaluate the potential off-site health effects associated with a
more "typical" accident scenario, an on-site spill of 100 gallons of liquid waste is also
evaluated. The spill volume of 100 gallons is selected based on the review of reported
incidents at the WTI facility (the largest spill reported at WTI from June 1993 to
February 1995 was approximately 20 gallons), and data from the U.S. DOT (1995).
According to U.S. DOT (1995), the average spill of liquid hazardous materials
accidentally released during highway transportation was 120 gallons for the 10 year
period ending in 1994, and 80 gallons for the 5 year period ending hi 1994, indicating
that 100 gallons is a reasonable estimate of the size of a typical spill. For the purposes
of this assessment, the typical 100-gallon spill is also assumed to occur near the Truck
Unloading Station.
In this Accident Analysis, both conservative and typical scenarios are evaluated
assuming no active mitigation. In finalizing its proposed rule regarding accidental
release prevention requirements (USEPA 1995a), U.S. EPA is considering incorporating
effects of passive mitigation systems, but not active mitigation systems, into the worst-
case release scenario, if such systems are capable of withstanding destructive events
(e.g., fires, explosions, floods, hurricanes and earthquakes). Passive systems would
include dikes, catch basins, and drams for liquids, and enclosures for both liquids and
gases. Scenarios involving passive mitigation systems that have connections to the
environment (such as a rainwater drain valve) would have to assume failure of that
connection. In the WTI Accident Analysis, passive systems capable of withstanding
destructive events are included hi evaluating the no active mitigation scenarios.
In Chapter VII (Uncertainties), a separate evaluation of the potential effect of active
mitigation is also assessed. Two mitigation scenarios are evaluated:
• All releases are effectively mitigated within 10 minutes. This mitigation time
is conservative for smaller spills and in situations where automatic systems are
in place (e.g., foams for fire suppression). However, as discussed in Chapter
VII, mitigation of larger spills or accidents may require more than 10 minutes.
• All releases are effectively mitigated in one hour. This mitigation time may be
appropriate for high volume spills and in situations where automatic mitigation
systems are not hi place. Based on a detailed review of emergency response
procedures, one hour was determined to be the approximate mitigation tune for
two major accident scenarios evaluated in WTI's Emergency Exercise Plan (Von
Roll 1993).
Volume VII , External Review Draft
II-9 Do Not Cite or Quote
-------
Chapter VII also presents an assessment of the impact of a failure of passive
mitigation devices (e.g,. dikes and berms) in the case of a large on-site spill.
2. On-Site Fire
Several events, including an on-site spill, could cause a fire if an ignition source is ,
present. Such a fire could result hi the increased volatilization of waste constituents, as
well as the formation of combustion products of concern, particularly when wastes
containing nitrogen, sulfur or halogens (e.g., chlorine or bromine) are burned. While
complete combustion typically results hi the formation of relatively simple compounds
such as carbon dioxide (CO2), water (H2O), nitrogen oxides (NOJ, sulfur dioxide (S02)
and hydrogen chloride (HC1), other more complex substances may also be produced as a
result of incomplete combustion. The types of substances formed will depend on a
number of factors, including the chemical makeup of the waste, the combustion
temperature, and the extent of mixing with air. In addition to the release of these
products of combustion and incomplete combustion, heat effects from the fire could
cause the contents of nearby storage tanks to boil.
For a fire scenario, the most significant parameters for determining off-site
consequences are the types and quantities of the chemicals ignited, and the location of
the fire. Based on a review of U.S. EPA (1995b), most fires and explosions at
hazardous waste incineration facilities have been associated with operations of the
combustion system. The more frequently reported events include steam explosions
resulting from molten slag dropping into the ash quench, and fires and explosions hi the
air pollution control equipment. These incidents have not been reported to have had
off-site human health effects (U.S. EPA 1995b). Additionally, the consequences of
incidents of this type are expected to be limited by the small amount of waste present at
any one tune hi these locations.
A fire with greater potential for causing adverse effects hi the off-site community
was recently reported at the ThermalKem hazardous waste incinerator in South Carolina
(U.S. EPA 1995b). In January 1995, almost 1,900 30-gallon fiber drums possibly
containing hazardous and nonhazardous waste caught fire and burned, causing extensive
damage and one minor injury to an on-site employee. The fire started hi two fiber
drums containing nonhazardous molybdenum wastes that had been rendered reactive due
to mixing with wood flour during shredding. All fire-fighting water was contained, no
explosions occurred, and no off-site releases occurred above reportable quantities.
A significantly smaller fire was reported at the WTI facility hi February 1995 (see
Table 3 of Appendix VII-1). According to facility records, bulk solid waste in a
clamshell used to feed bulk solids into the incinerator caught fire. The sprinkler system
Volume VII External Review Draft
11-10 Do Not Cite or Quote
-------
was activated, extinguishing the fire within approximately one minute. Damage
reportedly was limited to the crane bucket wires, cables and insulation in the immediate
area.
WTI reported a second, similar, waste-related fire on July 3, 1995. This time, the
fire occurred in one of the two bulk solid waste pits. The automatic water deluge system
extinguished this fire quickly, and only minor damage (mostly to the loading door for the
pit) was reported: Although the exact cause of this minor fire is unclear, it has been
hypothesized that a burning piece of waste somehow escaped the double doors of the
incinerator feed chute and either floated through the ah* back to the waste pit or was
carried back to the waste pit via the clamshell bucket. WTI has made changes to
operating procedures, equipment, and control logic hi response to this event (Victorine
1995c).
Automatic fire protection systems are hi place at various locations across the WTI
facility, to allow quick response to fires such as those which occurred hi February and
July of 1995. A summary of the WTI fire protection systems, as reported by Von Roll
(1994), is presented in Table II-3. Details regarding the fire protection systems are
provided hi Von Roll (1994).
For the WTI Accident Analysis, the conservative on-site fire event selected for
quantitative evaluation involves a storage tank rupture hi the Organic Waste Tank Farm
followed by ignition. It is assumed that a 20,000-gallon tank ruptures, emptying its
contents into the diked area, which has an area of approximately 180 m2. With the pool
size defined by this diked area, the pool depth is estimated to be 0.42 m, using the
methodology outlined hi Appendix VII-3. It is assumed that the waste is ignited by an
undefined source, such as a spark, generating products of combustion. The primary
reason for selecting this indoor fire scenario is the volume of the wastes involved. The
storage tanks hi the Organic Waste Tank Farm have the largest on-site storage capacity
for a single container. The quantities involved hi a spill from one of these tanks,
followed by ignition, would be expected to result hi a more prolonged fire than a spill
from any other on-site containers.
In the "typical" on-site scenario, a fire involving 200 gallons of waste is assumed to
ignite outdoors on a paved area near the center of the facility, generating products of
combustion. This is approximately the equivalent of four 55-gallon drums, and roughly
twice the size of a typical transportation spill for the ten-year period ending hi 1994,
according to U.S. DOT (1995).
As hi the on-site spill scenario, the consequences of an on-site fire are evaluated
assuming no active mitigation to limit duration of emissions. An evaluation of the
Volume VII External Review Draft
II-11 Do Not Cite or Quote
-------
impact of active mitigation measures on the consequences of the accident scenarios
described is presented in Chapter VII.
3. On-Site Mixing of Incompatible Wastes
Wastes containing certain chemicals may react when mixed, resulting in a variety of
adverse consequences, including the generation of flammable or toxic gases, fires or
explosions, or heat effects. Wastes which react to produce such adverse effects are
sometimes referred to as "incompatible" wastes. The specific outcome of-mixing
incompatible wastes depends upon the concentrations and volumes of the reactants, the
rate of reaction, the type of vessel in which the reaction occurs, and the presence or
absence of mitigation devices. Among these possible consequences, the generation of a
gaseous toxic reaction product (e.g., HC1 or C12) can affect the largest off-site area
because the chemicals can be carried considerable distances downwind. For example,
the release and off-site migration of toxic and corrosive fumes such as HC1, phosgene
and other gaseous halogenated compounds can occur if halogenated hydrocarbons are
mixed with mineral acids (oxidizing or nonoxidizing), amines (aliphatic or aromatic), or
strong oxidizing agents (Sax and Lewis 1989; ASTM 1986; Bretherick 1985).
Under the Resource Conservation and Recovery Act (RCRA), incompatible wastes
must be segregated, reducing the potential for accidents (40 CFR 264.172). Despite
such precautions, a few incidents that may have been caused by mixing of incompatible
wastes at commercial hazardous waste treatment facilities have been reported (U.S. EPA
1995b). At the TWI hazardous waste incinerator hi Sauget, Illinois, hi 1990, mixing of
incompatible wastes is believed to have caused the contents of a blending tank to boil
over, releasing a plume of chlorinated gas. No off-site effects were reported in the
• TSDF incident study (U.S. EPA 1995b). At the Washington Chemical Facility in the
State of Washington, mixing of incompatible wastes in a drum reportedly caused an
explosion, propelling the drum through the air and resulting in the release of waste
material. Minor property damage occurred but no on-site or off-site injuries were
reported.
Mixing of incompatible wastes is a known hazard and, due to this concern,
procedures have been established at the WTI facility to reduce the potential for such an
event to occur. For example, incompatible wastes must be segregated as required under
RCRA (40 CFR 264.172). This Accident Analysis, however, assumes that an accident
or unforeseen circumstance occurs, or there is a failure to follow the established accident
prevention procedures, and incompatible wastes are thus allowed to mix. Locations
where inadvertent mixing of incompatible wastes is most likely to occur at the WTI
facility are the Truck Unloading Stations, Organic Waste Tank Farm and Container.
Volume VII External Review Draft
H-12 Do Not Cite or Quote
-------
Processing Facility (extruder, pump-out tanks). Other possible scenarios include a
release of vapors during truck sampling (if a shipper mixed incompatible wastes, thereby
generating vapors within the truck during transport) and an on-site two truck accident
involving the release of incompatible materials from the two trucks and subsequent
mixing of the materials.
In storage areas where separate tanks of wastes are stored under a common roof
(i.e., Organic Waste Tank Farm and Container Processing Facility), incompatible wastes
are stored hi separate areas, and permanent containment barriers are hi place to reduce
the potential for mixing of incompatible wastes hi the event of a spill. Situations where
mixing of incompatible materials might occur hi these storage areas would thus likely
involve the misidentification or improper storage of incompatible wastes.For example, if
two tanks having a common containment barrier were to leak, mixing of incompatible
wastes could occur, but only if the operator failed to follow the standard practice of
storing incompatible wastes in separate areas. Similarly, a misidentified waste could be
accidently pumped into a storage vessel already containing an incompatible material.
For the WTI analysis, two possibilities for on-site mixing of incompatible wastes are
considered for quantitative evaluation:
• An on-site collision between two tanker trucks, each containing 5,000 gallons of
different wastes that are incompatible, resulting hi toxic gases being released to
the atmosphere.
• The inadvertent addition of 5,000 gallons of waste from a tanker into a 20,000
gallon Organic Waste Tank Farm storage tank containing 5,000 gallons of an
incompatible material, resulting hi an incompatible mixture and the release of
toxic gases.
Between these two events, the scenario involving inadvertent mixing hi the storage tank
is selected for quantitative evaluation because it is highly unlikely that complete mixing
of incompatible wastes from two tanker trucks would occur on-site due to the low
volume of on-site traffic and the low speed restriction at the facility. Pumping of a
potentially incompatible waste from a tanker truck to the wrong storage vessel is
representative of accidents which could occur because of sampling/analysis uncertainty or
error, operator error, or other circumstances believed to have a higher probability of
occurrence than the collision of two tanker trucks.
In addition to the conservative scenario described above, a more "typical" scenario
involving the mixing of incompatible wastes is evaluated. In the typical scenario, a total
Volume VII External Review Draft
H-13 Do Not Cite or Quote
-------
of 200 gallons of incompatible wastes are mixed together outdoors near the center of the
WTI facility, resulting in the generation of toxic gases. The 200-gallon volume
corresponds to the approximate volume of four 55-gallon drums.
In the Accident Analysis both conservative and typical scenarios are evaluated
assuming no active mitigation, although active mitigation measures are available at the
WTI facility. A separate evaluation of the potential effect of active mitigation is
assessed and presented hi Chapter VII.
4. Off-Site Tanker Truck Spill
Off-site spill scenarios involve the release of the contents, or a portion of the
contents, of a tanker truck. Collisions, which could result hi the release of a majority of
the contents of the tanker hi a single location, would generally be expected to have the
greatest potential for adverse consequences hi the community.
The U.S. DOT maintains a database entitled Hazardous Materials Information
System (HMIS) regarding accidents during the transport of both hazardous wastes and
hazardous materials (e.g., gasoline, process chemicals). A review of data between 1984
and 1993 indicates that during that 10-year period, there were 1,959 transportation
incidents involving hazardous waste on highways hi the U.S., resulting hi 143 reported
injuries and one reported fatality (U.S. DOT 1995). By comparison, during the same
ten year period, there were 63,577 highway transportation incidents involving hazardous
materials, resulting hi 2,781 reported injuries and 115 reported fatalities (U.S. DOT
1995).
In the WTI Accident Analysis, the subpopulation that is most likely to be adversely
affected by an off-site accident would be individuals who live or work along the local
access route. In the East Liverpool area, trucks transporting waste to the facility are
expected to travel along Pennsylvania Avenue (Route 39), a two-lane city street that
serves as the main thoroughfare for East Liverpool. Residences and commercial
establishments are located along this portion of the route, immediately adjacent to the
roadway. Approximately one-half mile from the facility, trucks turn to the south along
Virginia Avenue, a two-lane residential street with houses located within 20 feet of the
street. A street light and gas station are located at the intersection of Virginia and
Pennsylvania Avenues. Trucks travel approximately three blocks along Virginia
Avenue, cross a set of railroad tracks, and proceed to the facility gate. A map of the
local access route is shown on a topographic map hi Figure II-2. This topographic map
was rendered prior to construction of the WTI facility, and thus depicts tanks at the
current site of the WTI facility.
Volume VII External Review Draft
H-14 Do Not Cite or Quote
-------
For the purposes of the WTI Accident Analysis, a spill on a local access road near
the facility is assumed for the conservative off-site spill scenario. For this scenario
category, a 5,000-gallon tanker is assumed to rupture, releasing its entire contents.
According to U.S. DOT data covering the period from 1971 through 1986, as shown in
Table II-4, approximately 95% of all spills involving full-size tankers were less than
5,000 gallons (U.S. DOT 1986). Furthermore, FEMA (1993) estimates that about 20%
of all spills would involve loss of the entire tanker contents. The pool is assumed to
spread in all directions at an equal rate, with liquids reaching the edge of the road
running off onto soil or into a ditch. Assuming the road on which the spill occurs is flat
and has no curbs capable of acting as a containment barrier, the liquid pool is assumed
to reach a maximum length and area defined by the width of the road and a 1 cm pool
depth. In reality, the road is likely to be sloped from the center line to the sides,
reducing the spill area; thus the assumption of a non-sloped road surface is believed to
be conservative and tends to overestimate potential off-site consequences. The location
assumed for the spill is shown hi Figure II-3.
In addition to a spill onto the roadway, a spill into surface water is also theoretically
possible. For example, a collision on the Route 30 Bridge might possibly lead to a spill
into the Ohio River. In the event of a spill into surface water, chemicals in the waste
may either: 1) float; 2) sink; or 3) mix with the water. The greatest potential for acute
human exposures would involve inhalation of volatilizing chemicals that are floating on,
or mixed in, the water. Other potential pathways (such as fishing or drinking water
ingestion) might represent potential longer-term exposure routes, if remediation were not
undertaken, but would be less likely than inhalation to pose an acute risk. Short-term
exposures associated with a spill into surface water will not be quantified hi the Accident
Analysis because the potential resulting acute impacts are judged to be less significant
than the impacts from a spill onto the road, for the following reasons:
• A spill into surface water is less likely to occur than a spill onto the roadway.
• Chemical mixing with the water, or sinking below the surface of the water,
would reduce emission rates relative to a spill onto the road.
• Potential human receptors are likely to be closer to a spill on the roadway than
to one into surface water, and thus receive higher levels of exposure as a result
of a roadway spill.
Volume VII External Review Draft
11-15 Do Not Cite or Quote
-------
Potential adverse ecological effects associated with a spill into surface water are not
evaluated in this analysis. Although the ecological consequences of a spill into surface
water could possibly be significant, the probability of occurrence of such an event is
judged to be very low based on the accident frequency data from U.S. DOT (1995) and
the relatively short distance travelled over surface water.
In the "typical" off-site accident scenario, a spill of 100 gallons is assumed. As
previously discussed, a 100 gallon spill can be considered typical based on data reported
by U.S. DOT (1995). The location of the spill is assumed to be the same in the typical
scenario as in the conservative scenario.
5. Off-Site Tanker Truck Spill with Fire
If an ignition source is present at the time of the off-site tanker truck spill described
above, a fire could occur. U.S. DOT (1995) does not identify the number of hazardous
waste or hazardous material transportation incidents involving fire. Therefore, it is not
known what percentage of the 1,959 incidents between 1984 and 1993 involved fire.
In the WTI Accident Analysis, 5,000 and 100-gallon spills are considered for the
conservative and typical off-site spill with fire scenarios, respectively. The rationale for
selecting these volumes is the same as the rationale for the volumes used in the off-site
spill scenarios. Emissions were assumed to consist of the same types of products of
combustion and incomplete combustion as those evaluated in the on-site fire scenario.
As in the off-site spill scenario, no mitigation or emergency response is assumed
which could limit emissions.
D. Summary of Results and Key Assumptions
As shown on Table II-5, the scenarios selected for quantitative evaluation in the Accident
Analysis are an on-site spill, an on-site fire, on-site mixing of incompatible wastes, an off-
site spill and an off-site fire.
Major assumptions made in the identification of accident scenarios are summarized in
Table II-6.
Volume VII External Review Draft
II-16 Do Not Cite or Quote
-------
TABLE H-l
Partial List of Passive Mitigation Features at the WTI Facility1
Source
Organic waste reception tanks
Organic waste holding tanks
Organic waste sludge tanks
Organic waste blending tanks
Tank truck unloading stations
Truck unloading docks - Drum Processing
Building.
Container holding rooms or areas
Container processing areas
Drum Extruder Area
Drum pumpout tank
Drum staging area
Short-term containerized staging areas
Scrubber water holding tanks
Exterior truck wash
Storm water tanks
Caustic tank
Scrubber
Fuel oil tank
Diesel generator day-tank
Fire pump No. 1 day-tank
Fire pump No. 2 day-tank
Type of Containment or
Diversionary Structures
Contoured surfaces and reinforced concrete dikes and sumps
Contoured surfaces and reinforced concrete dikes and sumps
Contoured surfaces and reinforced concrete dikes and sumps
Contoured surfaces and reinforced concrete dikes and sumps
Contoured surfaces, speed bumps, curbs, building walls,
reinforced concrete and sumps
Contoured surfaces, speed bumps, curbs, building walls and
reinforced concrete drainage trenches and sump
Contoured surfaces and reinforced concrete dikes and sumps
Contoured surfaces and reinforced concrete dikes and sumps
Contoured surfaces and reinforced concrete dikes and sumps
Reinforced concrete dikes and sumps
Contoured surfaces and reinforced concrete curbs and sumps
Contoured surfaces and reinforced concrete curbs and sump
Contoured surfaces and reinforced concrete dikes and sump
Contoured surfaces and reinforced concrete curbs and sump
Contoured surfaces and reinforced concrete dikes and sumps
Contoured surfaces and reinforced concrete dikes and sump
Contoured surfaces and reinforced concrete dikes and sump
Contoured surfaces and reinforced concrete dikes and sumps
Contoured surfaces and reinforced concrete sump
Reinforced concrete dike
Reinforced concrete dike
Note:
1 Source: WTI 1992.
Volume VII
11-17
External Review Draft
Do Not Cite or Quote
-------
TABLE II-2
Preliminary List of Potential Accident Scenarios at WTI
Location
Accident Scenario
Assumptions/Considerations
Off-site Transportation
Tanker/Drum Truck
— Spill onto roadway (evaporation)
— Spill onto roadway (fire)
— Spill into Ohio River
Transportation routes within a 5-mile
radius of WTI facility will be evaluated
River barge not considered as a transport
option
Tank truck volume assumed to be 5,000
gallons
Trailer truck capacity assumed to be 80
55-gallon drums
Transported wastes are similar to WTI
waste profile for first year of operation
Truck Holding and Sampling Area
• Tanker truck rupture (evaporation)
• Tanker truck rupture (fire)
• Incompatible wastes in tanker (vapor
release upon opening)
60'x96' (60 ft by 96 ft) area
Tank truck volume assumed to be 5,000
gallons
6" (6 inch) curbs and speed bumps
(connected) and paved surface sloped
toward a reinforced concrete sump.
Containment capacity is 31,000 gallons.
Volume VII
External Review
Do Not Cite (
-------
TABLE II-2
Preliminary List of Potential Accident Scenarios at WTI
Location
Accident Scenario
Assumptions/Considerations
Truck Unloading Stations (drum
and bulk)
• Drum Scenarios
— Spill from pallet of drums during
transfer (evaporation)
— Truck of drums catches fire
— Spill of truck load of drums
— Release from leaking drums
within trailer
• Bulk Pumpable Scenarios
— Spill from tanker truck
(evaporation)
— Spill from tanker truck (fire)
— Failure of transfer lines/hoses
— Overflow due to improper
unloading
— Mixing of incompatible wastes
— Collision of trucks
— Release of combined contents of
truck and tank due to siphoning
• Solids Scenarios
60'x 75'area
A combination of 7V4" high speed bumps,
8" high curbs, and building walls
surround each of three unloading stations.
Paved surface in each unloading station
sloped toward concrete sump.
Containment capacity in each unloading
station is 10,000 gallons.
Volume VII
11-19
External Review Draft
Do Not Cite or Quote
-------
TABLE II-2
Preliminary List of Potential Accident Scenarios at WTI
Location
Accident Scenario
Assumptions/Considerations
Organic Waste Tank Farm
Tank spill (multiple/single)
Fire (multiple/single)
Fire with boil-off
Ventilation fan failure
Mixing of incompatible wastes
52'x 162'area
Storage capacity is 300,000 gallons
Tank farm divided into two groups of
tanks by a reinforced concrete aisle,
which acts as a common containment
curb. Entire combined containment area
surrounded by an exterior dike wall;
surface in each containment area sloped
toward two concrete sumps. Capacity of
each containment area is 21,500 gallons.
Drum/Container Storage Area
(Container Processing
Facility)
• Multiple drum spill
• Fire (maximum number of drums)
• Ventilation fan failure
100'X210'area
Storage capacity of entire Container
Processing Facility is 500,000 gallons
Storage area divided into two areas by a
reinforced concrete aisle, which acts as a
common containment curb. The entire
combined containment area is surrounded
on three sides by an exterior wall and on
the fourth side by a curbed fire wall with
three doors having 1V4" high speed
bumps. The surface in each containment
area is sloped toward a concrete sump.
Capacity of each containment area is
20,000 gallons.
Vol-me VII
External Review Draft
Do Not Cite te
-------
TABLE II-2
Preliminary List of Potential Accident Scenarios at WTI
Location
Accident Scenario
Assumptions/Considerations
Drum Processing/Extruder
(Container Processing
Facility)
• Drum Processing
— Drum spill
— Vapor release
— Transfer line failure
— Ventilation fan failure
• Extruder
— Drum spill
— Mixing of incompatible wastes
— Explosion in hydropulper
• Pump-Out Tanks
— Mixing of incompatible wastes
100'X237'area
Storage capacity of entire Container
Processing Facility is 500,000 gallons
Drum processing area surrounded by 6"
high concrete curb with IVi" high speed
bumps at the three interior doors to the
storage area and at the unloading
platform. All other exterior doors for the
area have either a 6" high concrete sill or
speed bump. The floor is sloped towards
three concrete sumps. Containment
capacity is 50,000 gallons.
Drum extruder area surrounded by a 6"
high concrete curb. The floor is sloped
toward a concrete sump. Containment
capacity is 9,000 gallons.
Outdoor tanks area contains three pump-
out tanks and one sludge reception tank.
The capacity of the pumpout tanks is
2,500 gallons; the capacity of the sludge
reception tank is 7,000 gallons. Area
surrounded by a 16" high concrete
containment wall. Surface is sloped
toward a concrete- sump. Containment
capacity is 11,000 gallons.
Total containment capacity is 70,000
gallons.
Volume VII
II-21
External Review Draft
Do Not Cite or Quote
-------
TABLE II-2
Preliminary List of Potential Accident Scenarios at WTI
Location
Incinerator Feed Building
Incinerator Train (e.g., kiln,
secondary combustion
chamber [SCC], air pollution
control equipment)
Steam Plant Building
Wastewater Treatment Building
and Collection Tank Area
Analytical Lab
Accident Scenario
• Fire in containerized waste area
• Fire in feed chute
• Explosion in kiln
• Steam explosion in quench water
• Release due to power failure
• Failure of air pollution control
equipment
— Acid gas release
— Non-combusted waste release
— Particulates release
• Boiler explosion
• Failure of ID fan
• Explosion
• Release of wastewater
• Vapor release
• Fire
• Release from lab collection tank
Assumptions/Considerations
• 61 'x 55' area
• Stores approximately 500 cubic yards of
bulk solids.
• 6" curb and/or speed bumps run along the
outer edge of the incinerator area that is
not bordered by the Feed Building, the
Steam Plant Building, the Scrubber
Building, and the Caustic Tank
Containment walls. Paved surfaces inside
the curbs are sloped toward either the
incinerator train storm water sump, the
spray dryer sump, or the slag quench tank
sump. Containment capacity is 176,000
gallons.
• 50' x 80' area
• No hazardous materials released.
• 35' x48' building with 46.5' X202'
collection tank area (5 tanks)
• Tanks are surrounded by a 6' 8" high
concrete containment wall. An
intermediate concrete wall 3" lower than
the surrounding walls separates the tanks
into two groups. Total containment
capacity is 290,000 gallons.
• Located within 100' x 120' Administration
Building
Vpl'"ne VII
External Review Draft
Do Not Cite >te
-------
TABLE H-3
WTI Fire Protection Systems
Facility Area
Administration
Laboratory
Maintenance Building
Steam Plant
Utility Bridge
Incinerator Feed Building
Container Holding Area
Truck Holding Area
Fire Water Pump House
Organic Waste Tank Farm
Foam Pump House
Truck Wash
Container Processing Building
Truck Unloading
Rack Storage Building
Fire Protection System
Wet System
Wet System and Halon 1301 System
Wet System
Wet System
Water Deluge
Water Deluge
Dry System
Water Deluge
Wet System
Foam Deluge
Foam Deluge
Dry System
Foam Deluge
Foam Deluge
Foam Deluge
Source: Von Roll (1994)
Volume VII
11-23
External Review Draft
Do Not Cite or Quote
-------
TABLE H-4
Distribution of Cargo Losses from Full Size Tankers
During ffighway Transit hi the U.S. from 1971 to October 1986
Size of Spill
(gallons)
1
10
20
40
60
100
400
700
3,000
5,000
8,000
15,000
Number of Incidents Less
Than or Equal to Size of Spill
452
2,937
4,378
6,017
7,340
8,695
10,966
11,517
13,097
13,740
14,247
14,475
Cumulative Frequency of
Spill
0.03
•0.20
0.30
0.42
0.51
0.60
0.75
0.80
0.90
0.95
0.98
1.00
Source: USDOT, 1986.
Volume VII
11-24
External Review Draft
Do Not Cite or Quote
-------
TABLE II-5
Scenarios Selected for Quantitative Evaluation
Scenario
On-Site Spill
On-Site Fire
On-Site Mixing of Incompatible
Wastes
Off-Site Spill
Off-Site Fire
Description
Conservative Event
5,000 gallon spill due to a tanker truck
accident, resulting in volatile emissions
20,000 gallon spill in the Organic Waste
Tank Farm ignites, generating toxic products
of combustion
Accidental pumping of 5,000 gallon of wastes
from a tanker truck to a storage vessel
containing 5,000 gallons of an incompatible
waste, generating toxic gases
5,000 gallon spill along local access road,
resulting in volatile emissions
5,000 gallon spill ignites, generating toxic
products of combustion
Typical Event
100 gallon spill due to tanker truck
accident, resulting in volatile emissions
200 gallon spill ignites, generating toxic
products of combustion
200 gallons of incompatible wastes are
mixed, generating toxic gases
100 gallon spill along local access road,
resulting in volatile emissions
100 gallon spill ignites, generating toxic
products of combustion
Volume VII
11-25
External Review Draft
Do Not Cite or Quote
-------
TABLE II-6
Key Assumptions Made in the Identification of Accident Scenarios
Assumption
1. Waste will continue to be received at the
facility by truck only.
2. For off-site spill and fire scenarios, assumed
conservative spill size of 5,000 gallon; typical
spill size of 100 gallon
3. For the mixing of incompatible waste
scenarios, assumed 10,000 gallon of waste for
the conservative scenario, 200 gallon of waste
for the typical scenario
4. For on-site fire scenario, assumed 20,000
gallon of waste for conservative scenario; 200
gallon of waste of typical scenario
5. Typical spill sizes associated with on-site
accidents are comparable to the typical spill
sizes reported by U.S. DOT for off-site
accidents.
6. Off-site spills into surface water not expected
to pose significant human health risks, and
thus not quantitatively evaluated.
Basis
There are currently no proposals to U.S.
EPA to transport waste to WTI via rail or
barge. Accidents that could be associated
with rail or barge transport, if they were to
occur in the future, are not evaluated.
Based on USDOT (1995) data, 95% of all
spills are less than 5,000 gallon, and 50% of
all spills are less than 100 gallon
Conservative scenario volumes based on tank
truck and storage vessel capacities. Typical
scenario based on assumed spill from
multiple drums (four)
Conservative scenario based on storage
vessel capacities. Typical scenario based on
assumed spill from multiple drums (four)
Some failures which may lead to spills are
relevant to both on-site and off-site
scenarios. Limited data from spills at WTI
suggest that the assumption made in the
Accident Analysis is conservative, however.
Off-site spills onto the roadway more likely
to occur, and more likely to affect the off-
site community, than spills into surface
water.
Magnitude of Effect
Low
Medium
Medium
Medium
Medium
Low
Direction of Effect
Unknown
Conservative spill size likely
to overestimate, typical spill
size may over- or under-
estimate
Conservative scenario likely
to overestimate, typical
scenario may over- or
under-estimate
Conservative scenario likely
to overestimate, typical
scenario may over- or
under-estimate
Overestimate
Underestimate
Volume VII
External Review Draft
Do Not Cite ( 'e
-------
LEGEND
' A
| PROPOSED BUU.OMS «„ SKUSilr fCKCC SEE CHCIKEK< PEBSWKEL G«IE
- - T E»EStl« F.CIL1IIES E.ISTMi FENCE > BITUMtWUS PavEMENt » SIE; SLOPE
i/r- p r
cs»*«c s'c«.£
NOTES:
1 BlniDWC OIUENSIOMS BEPBEStNI ElTMEH
".MIEftLWE OF COLUMNS OR Clfll L«ES.
!'«1£ FMu O^-^IONS REPBESEHT
WilOE F«CE Of (-IWBS.
Rgure 11-1
WT1 SITE PLAN
11-27
-------
^ * -\N
•tn
.).- o
tt
NORMAL POOL Light
665
42
Res
I F E R
/> '•' I / '-
!/( - --y 3
Rgure 11-2
LOCAL ACCESS ROUTE FROM EAST
LIVERPOOL TO THE WTI FACILITY
-------
NORMAL POOL
ELEVATION .665
ASSUMED LOCATION
OF OFF-SITE SPILL
Figure II-3
LOCATION FOR THE OFF-SITE SPILL
-------
HI. CHEMICALS OF POTENTIAL CONCERN
A. Methodology
In addition to developing a list of candidate accident scenarios for consideration, the
types of waste that may be involved in each accident scenario and the specific chemicals
released into the environment must be identified. Specific chemicals to evaluate
quantitatively in each scenario hi the WTI Accident Analysis are selected according to the
following procedure:
• Development of a preliminary list of acutely hazardous substances that may be
expected to be handled at the WTI facility.
• Identification of chemicals of potential concern from the preliminary list of acutely
hazardous substances, including an initial screening of chemicals based on
availability of U.S. EPA or NIOSH acute toxicity criteria (FEMA 1993) and a
subsequent ranking of chemicals according to: 1) acute toxicity; 2) acute toxicity
and volatility; and 3) acute toxicity, volatility, and estimated maximum concentration
in waste. Acute toxicity criteria are used because they apply to the evaluation of
short-term (e.g., less than 1-day) exposures, which are the focus of hazards analysis
(U.S. EPA 1987).
• Selection of specific chemicals to be used hi evaluating each accident event, based
on the type of scenario and the chemical ranking.
These steps are described below.
B. Preliminary Identification of Chemicals of Potential Concern
Several sources of information have been used to compile a preliminary list of wastes
and chemicals of potential concern:
• Projected waste composition based on Waste Profiles from WTI.
Volume YE External Review Draft
ffl-1 Do Not Cite or Quote
-------
• Acutely hazardous wastes (i.e., "P" list hazardous wastes) as defined under Subpart
D of 40 CFR 260, Hazardous Waste Management System: General [40 CFR
§261.33(e)]; WTI has applied for acceptance of "P" wastes, but this request has not
yet been granted by U.S. EPA.
• Chemicals regulated under Section 112(r) of the Clean Air Act (CAA) as toxic or
flammable substances that could be involved in an accidental release (59 FR 4478).
• Chemicals listed as Extremely Hazardous Substances (EHSs) under Section 302 of
EPCRA.
The preliminary list of acutely hazardous substances consists of 309 chemicals. From
this list, a subset of 139 chemicals are identified which pose the greatest off-site risks in the
event of an accidental release, and for which acute toxicity criteria are available. The
chemicals selected for further analysis are presented in Table III-l. Chemicals eliminated
from further analysis are shown in Table 1 of Appendix VII-2.
A key factor in evaluating the consequences of accidental releases is the acute toxicity
criterion. The acute toxicity criterion is used hi determining the area potentially affected by
a vapor cloud resulting from an accidental release of hazardous material. The potentially
affected area as defined as the area over which the concentration of substance in the air
exceeds the selected acute toxicity criterion.
The acute toxicity criterion must be selected based on the objectives of the hazard or
consequence assessment. For example, if the objective of the hazard assessment is to
determine the area where fatalities are most likely to occur, then the acute to lethal criterion
used in the assessment should be based on the lethal concentrations. Conversely, if the
purpose is to assess irritation or odor detection, the criterion used must reflect a
concentration where irritation or odor detection is likely to occur.
The purpose of the WTI Accident Analysis is to determine the areas where, if an
accidental release were to occur, serious irreversible health effects are possible. This type of
evaluation is often conducted for emergency preparedness and planning activities, and is
nearly identical to the hazard assessment required for risk management program and planning
regulations soon to be promulgated under Clean Air Act (CAA) Section 112(r). Note,
however, that the results of this evaluation cannot be used to confidently predict health
effects during an actual accidental release because weather, atmospheric dispersion and
human exposure conditions may be much different than those assumed hi the Accident
Analysis. The uncertainties associated with this Accident Analysis are discussed in Chapter
VII.
Volume VH External Review Draft
HI-2 ' Do Not Cite or Quote
-------
Immediately Dangerous to Life or Health (IDLH) values established by the National
Institute for Occupational Safety and Health (NIOSH) are used in the Accident analysis as the
acute toxicity criteria for evaluating potential off-site consequences, because they represent a
consistent, relatively comprehensive set of criteria for assessing the acute effects of short-
term exposures. IDLH values are defined by NIOSH as the maximum airborne contaminant
concentrations from which an individual could escape within 30 minutes without any escape-
impairing symptoms or any irreversible health effects (FEMA 1993). This definition is
consistent with the purpose of the Accident Analysis. Although the IDLH is primarily used
for selection of occupational respiratory protection levels, the IDLH values represent a
consistent, relatively comprehensive set of criteria that can be used to estimate the areas in
an accidental release situation where people may be potentially exposed to harmful
concentrations of hazardous substances. The IDLH values used in the Accident Analysis can
be found in U.S. EPA (1995c).
In addition to the IDLH values, Level of Concern (LOG) values developed by U.S. EPA
under the Emergency Planning and Community Right to Know Act of 1986 (EPCRA) are
used and compared in a sensitivity analysis to the results obtained using IDLH values
(Chapter VII). LOG values were created to guide local emergency planning personnel for
screening and prioritizing acute hazards for purposes of community emergency preparedness
and response. LOC values are generally derived by dividing the IDLH, or an estimate of the
IDLH if none is available, by 10 (U.S. EPA 1987). The LOCs have been peer reviewed and
accepted for the purposes of emergency planning assessments since 1987.
Alternatively, Emergency Response Planning Guideline (ERPG) levels could have been
used hi the Accident Analysis for the acute toxicity criteria. ERPGs are prepared by the
American Industrial Hygiene Association (AIHA) and represent concentrations of hazardous
substances in air above which some members of the public may begin to experience adverse
effects if exposed for greater than 60 minutes. U.S. EPA is considering requiring the use of
ERPG values, followed by the IDLH if there is no ERPG, for hazard assessments under the
CAR Section 112(r) risk management program and planning regulations. However, only a
portion of the substances considered for quantitative evaluation hi the Accident Analysis have
published ERPG levels. Consequently, the results of the off-site consequence evaluation
would be based on a 60 minute exposure concentration (ERPG) for some substances and a 30
minute exposure concentration (IDLH) for others. U.S. EPA chose to use the IDLH values
for the quantitative evaluation to generate consistent, comparable results.
To assist in selecting chemicals from Table III-l to evaluate quantitatively in each
accident event, chemicals are ranked according to the following criteria:
Volume VII External Review Draft
ffl-3 Do Not Cite or Quote
-------
Acute toxicitv. as represented by IDLH value:
= IDLH
This ranking identifies chemicals of greatest concern with respect to toxicity
only. Chemicals with low IDLHs (and thus low values of RJ are the most
highly ranked. For chemicals without IDLH values, but for which U.S. EPA
has established an LOG, the LOG multiplied by a factor of 10 is used in ranking
according to acute toxicity.
Acute toxicitv and volatility. Chemicals are ranked as follows:
where VP represents the vapor pressure of the chemical. This ranking considers
both the acute toxicity and release potential (for example, hi the event of an on-
site or off-site spill). Chemicals with a combination of a low IDLH value and
high volatility would have the lowest R2 values, and thus be the most highly
ranked.
• Acute toxicitv. volatility and concentration. Chemicals are ranked as follows:
IDLH
(VP)(Q
where C represents the concentration reported hi waste streams expected to be
received at the WTI facility. Specifically, the concentration is calculated for
each chemical where data are available as the average of the maximum
concentrations reported for individual waste streams containing that chemical.
Chemicals with a combination of a low IDLH value, high volatility, and high
concentrations in waste would have the lowest R3 values, and thus be the most
highly ranked. Concentrations, expressed as a percent composition, are
Volume VII External Review Draft
IH-4 Do Not Cite or Quote
-------
estimated from information provided in waste profiles from WTI's first year of
operation (see Appendix III-l). It should be noted that concentration data are
available for only a relatively limited number of possible chemicals of concern.
The acute toxicity values, vapor pressure data and concentration data used in ranking
each chemical are presented hi Table ffl-1. The results of the rankings are presented in
Table 2 of Appendix VII-2.
C. Selection of Specific Chemicals for Each Accident Event
1. On-Site Spill
Two chemicals, formaldehyde and acetone, are selected for evaluation hi the on-site
spill scenario. Formaldehyde is selected as a "worst-case" chemical for evaluating spills
of a conservative waste; acetone is selected as a "typical" chemical for evaluating more
typical waste spills.
In the spill scenario, the combined ranking of acute toxicity, volatility and
concentration is most significant, because it considers both the toxicity of the chemical
and the potential magnitude of exposure. Of all chemicals of potential concern,
formaldehyde is the second most highly ranked chemical on the basis of acute toxicity,
volatility and concentration combined. The most highly ranked chemical was hydrogen
chloride (HC1), largely because of the extremely high vapor pressure of pure phase HC1
(31,000 mm Hg at 20°C). However, HC1 would not be expected to be received hi
significant concentrations, except in aqueous mixtures, where its vapor pressure is
greatly reduced. For example, according to Perry and Green (1984) the vapor pressure
of HC1 in a 20% aqueous solution is only 0.2 mm Hg at 20°C. (The concentration of
HC1 used hi the ranking is 18%). While the vapor pressure of formaldehyde is also
greatly reduced hi an aqueous solution (Gallant 1968), formaldehyde may also be present
hi an organic solution.
While formaldehyde ranks about 35th out of 133 chemicals of potential concern
based on acute toxicity alone, it ranks 7th out of 108 chemicals according to acute
toxicity and volatility combined. The 6 chemicals ranked more highly than
formaldehyde on the basis of toxicity and vapor pressure (i.e., arsine, diborane, nitrogen
oxide, hydrogen chloride, chlorine and hydrogen selenide) usually exist in gaseous form
and are, therefore, highly unlikely to be present at high concentrations hi large quantities
of liquid waste. Thus, on the basis of toxicity and volatility alone, formaldehyde would
also be appropriate as a "worst-case" chemical for modeling in the spill scenario.
Volume VII External Review Draft
III-5 Do Not Cite or Quote
-------
It should be recognized, however, that formaldehyde is a relatively minor constituent
hi the overall waste feed at the WTI facility. Based on waste profiles for the first year
of WTI operations, the ten constituents estimated as being received hi the largest
quantities in pumpable waste at the WTI facility are listed hi Table III-2. According to
the waste profile data for the first nine months of operation at the WTI facility,
approximately 100,000 Ib/yr of formaldehyde were estimated to be received, constituting
approximately 0.5% of the pumpable waste at the WTI facility. As shown hi Table 2 of
Appendix VII-2, of the ten chemicals reported hi the largest quantities hi the liquid
waste, acetone is ranked highest on the basis of both: 1) acute toxicity and volatility;
and 2) acute toxicity, volatility and concentration. Overall, on the basis of acute
toxicity, volatility and concentration, acetone ranks 9th of the 47 chemicals of potential
concern for which data on acute toxicity, volatility, and concentration are available.
Thus, acetone was also selected as a "typical" constituent for evaluating the spill
scenarios.
A mixture containing 10% formaldehyde was selected as a reasonable "worst-case"
waste for spill scenarios. This is approximately equal to the combined average of the
maximum (i.e., highest) concentrations reported for individual waste streams containing
formaldehyde. For the purpose of modeling formaldehyde emissions, the remaining
90% of the waste is assumed to be methanol, a chemical hi which formaldehyde is
soluble, and which is projected to be received in high quantities at the WTI facility (see
Table III-2). Methanol is selected only to provide representative waste mixture
properties for estimating formaldehyde emissions; hi reality, wastes are typically
composed of many individual chemicals. The selection of methanol is relatively
conservative, i.e., more likely to overestimate than underestimate formaldehyde
emissions. However, formaldehyde emissions from a more complex waste mixture with
physical/chemical properties similar to methanol would be approximately the same as
assuming a 10% formaldehyde/90% methanol mixture. For example, the formaldehyde
emission rate from a 10% formaldehyde/90% toluene mixture would be lower than from
a 10% formaldehyde/90% methanol mixture because the vapor pressure of the
formaldehyde/toluene mixture is lower than the formaldehyde/methanol mixture.
A mixture containing 10% acetone was selected as a reasonable "typical" waste for
spill scenarios. A concentration of 10% is approximately equal to the combined average
of the mean concentrations of acetone reported for individual waste streams containing
acetone. The remainder of the waste stream was assumed to consist of toluene to
estimate waste mixture properties for the purposes of predicting acetone emission rates.
Like methanol, toluene has been reported to be received hi high quantities in the
pumpable wastes (See Table III-2). The selection of other commonly received chemicals
Volume VT1 External Review Draft
HI-6 Do Not cite or Quote
-------
from Table III-2 to determine waste mixture properties would not substantially affect
acetone emission rates.
In evaluating the on-site spill scenario, four cases are examined:
• Conservative spill (5,000 gallons) of a worst-case Waste (10% formaldehyde in
methanol).
• Conservative spill (5,000 gallons) of a typical waste (10% acetone in toluene).
• Typical spill (100 gallons) of a worst-case waste (10% formaldehyde in
methanol).
• Typical spill (100 gallons) of a typical waste (10% acetone in toluene-like
chemicals).
These events were developed to bracket the types of credible on-site spills at the
WTI facility.
2. On-Site Fire
Typical combustion products that could result from a fire include CO2, NOX, S02,
HC1 and phosgene. Phosgene and HC1 were selected as the chemicals to be modeled in
the on-site fire scenario.
Phosgene is one of the most highly ranked chemicals on the basis of both acute
toxicity alone (tied for 18th of 133 chemicals) and acute toxicity and volatility combined
(8th of 108 chemicals with both IDLH and vapor pressure data). However, based on
O'Mara et al. (1971) and Sjoberg (1952), phosgene emissions would be expected to be at
least 20-fold lower than HC1 emissions when common chlorinated compounds are
burned. Based on Sjoberg (1952), higher emissions of phosgene relative to HC1 are
possible, but only at thermal decomposition temperatures well below those expected hi
an open fire. Thus, HC1, which ranked 65th of 133 chemicals on the basis of acute
toxicity, and 4th of 108 chemicals on the basis of acute toxicity and volatility combined,
is also assessed.
Phosgene and HC1 may be produced when chlorinated wastes are burned. Sjoberg
(1952) measured the amount of HC1 and phosgene formed when seven different
chlorinated substances were placed in contact with an open flame. Of the chemicals
listed on Table ni-3, four (carbon tetrachloride, chloroform, tetrachloroethene and
trichloroethene) are among the 50 chemicals received hi pumpable wastes hi the highest
Volume VII External Review Draft
IE-? Do Not Cite or Quote
-------
quantities, according to waste profile sheets from the first year of operation. Each of the
four are estimated to represent approximately 0.5% of the pumpable waste.
Furthermore, the concentrations of each of the four chemicals hi individual waste
streams are also similar (see Table ffl-1). Since the quantities and concentrations of the
four chemicals are comparable, tetrachloroethene was selected to quantitatively evaluate
the fire scenario based on its relatively high formation rates for both phosgene and HC1.
According to the waste profiles estimated for the first year of operation, the average
of the maximum tetrachloroethene concentrations reported for individual waste streams
containing tetrachloroethene is about 15%. Thus, a waste consisting of 15%
tetrachloroethene was assumed for the fire scenarios. The remainder of the waste was
assumed to be toluene, a highly flammable chemical projected to be received in large
quantities in pumpable waste at the WTI facility.
3. On-Site Mixing of Incompatible Wastes
ASTM (1986) has proposed guidelines for estimating the incompatibility of selected
hazardous wastes. The ASTM guidelines provide a systematic method for determining
the incompatibility of most binary combinations of hazardous wastes. The consequences
of mixing various "reactivity" classes of chemical compounds (e.g., amines, halogenated
organics, metals) are summarized here.
A review of various hazardous chemical handbooks (Bretherick 1985; Sax and Lewis
1989), indicates that the chlorinated chemical most likely to be generated by the mixing
of incompatible wastes is HC1. According to ASTM (1986), HC1 formation can occur
when chlorinated hydrocarbons are mixed with mineral acids (oxidizing or nonoxidizing)
or strong oxidizing agents. For this event, the production of HC1 resulting from the
mixing of tetrachloroethene (a hydrocarbon with high chlorine content that is reportedly
received at the WTI facility) with a 70% nitric acid solution (an oxidizing mineral acid)
is quantitatively evaluated. The selection of tetrachloroethene is reasonably conservative,
i.e., is more likely to overestimate than underestimate HC1 emissions, because of its high
chlorine content relative to other common chlorinated hydrocarbons, e.g.,
dichloroethene, trichloroethene and trichloroethane. In the 1993 Toxic Release
Inventory, nitric acid is listed among the top ten chemicals managed via off-site waste
treatment, including incineration (USEPA 1995d), and thus can reasonably be assumed
to be among the wastes to be received by WTI. Sulfuric acid, which is also listed
among the top ten chemicals hi the 1993 Toxic Release Inventory, could be used in place
of nitric acid hi evaluating this accident scenario. Using sulfuric acid would, however,
not affect the results, since the HC1 release is dependent upon the amount of chlorine
available hi the tetrachloroethene solution. HC1 is selected on the basis of toxicity and
Volume VII External Review Draft
III-8 Do Not Cite or Quote
-------
volatility ranking, compared to other gases (such as chlorine) that may be produced
during mixing of incompatible wastes. The organic waste stream is assumed to contain
15% tetrachloroethene, based on projected estimates from the first year of operation at
the WTI facility.
4. Off-Site Tanker Truck Spill
As in the on-site spill scenario, mixtures of 10% formaldehyde/90% methanol and
10% acetone/90% toluene are both evaluated in the off-site spill scenario. The basis for
these selections is the same as for the on-site spill scenario, since the critical chemical-
specific factors affecting exposure and the potential for acute adverse health effects are
identical.
5. Off-Site Tanker Truck Spill with Fire
Phosgene and HC1 are selected for evaluation of the off-site tanker truck spill with
fire. The rationale for selection of phosgene and HC1 for the off-site fire scenario is the
same as for the on-site fire scenario. As in the on-site fire scenario, the type of waste
selected for evaluation is a mixture of 15% tetrachloroethene and 85% toluene.
D. Summary of Results and Key Assumptions
The wastes and chemicals selected to be evaluated for the accident scenarios are
summarized in Table IH-4.
Major assumptions made in selecting the chemicals to be quantitatively evaluated in the
Accident Analysis are summarized in Table III-5.
Volume VII External Review Draft
III-9 Do Not Cite or Quote
-------
TABLE III-l
Summary of Chemicals of Potential Concern for Short-Term Exposures"
CAS
Number1
107-20-0
640-19-7
62-74-8
67-64-1
107-2-8
107-13-1
116-6-3
309-0-2
107-18-6
20859-73-8
2763-96-4
504-24-5
7664-41-7
62-53-3
506-61-6
1327-53-3
1303-28-2
7784-34-1
7784-42-1
71-43-2
108-98-5
100-44-7
71-36-3
75-15-0
56-23-5
Substance
Acetaldehyde, chloro-
Acetamide, 2-fluoro-
Acetic acid, fluoro-, sodium salt
Acetone
Acrolein
Acrylonitrile
Aldicarb
Aldrin
Allyl alcohol
Aluminum phosphide
Aminomethyl-3-isoxazolol, 5-
Aminopyridine, 4-
Ammonia
Aniline
Argentate(l), bis(cyano-C)-, potassium
Arsenic oxide
Arsenic pentoxide
Arsenous trichloride
Arsine
Benzene
Benzenethiol
Benzyl chloride
Butanol
Carbon disulfide
Carbon tetrachloride
Basis2
B
B
B
A
B.C.D
A, C, D
B, D
B, D
B, C, D
B,D
B
B
C
A, D
B
B
B, D
C
C
A
B
B, D
A
A, B, C, D
A
IDLH3
(g/m3)
0.1442
0.058
0.0025
5.9
0.0046
0.1842
0.003
0.025
0.0474
0.2
0.17
0.2
0.2082
0.38
0.2
0.014
0.08
0.012
0.0095
1.59
0.014
0.005
4.234
1.553
1.256
Vapor Pressure4
(mm Hg @20°C)
100
NA
NA
180
220
83
0.0001 (25 °C)
0.000075
17
NA
NA
0.00037 (25 °C)
6500
0.6
NA
NA
NA
10 (23.5°C)
11000 (21 °C)
75
2 (25"C)
1
6
300
91
Conservative
Percent
Composition5
NA
NA
NA
21
NA
3
NA
NA
NA
NA
NA
NA
NA
7
NA
NA
NA
NA
NA
7
NA
NA
19
19
17
Volume VII
External Review Draft
Do Not Cite o \
-------
TABLE III-l
Summary of Chemicals of Potential Concern for Short-Term Exposures9
CAS
Number1
57-74-9
7782-50-5
10049-4-4
67-66-3
542-88-1
5344-82-1
542-76-7
8001-58-9
95-48-7
4170-30-3
98-82-8
506-77-4
110-82-7
108-94-1
19287-45-7
95-50-1
541-73-1
106-46-7
696-28-6
84-66-2
297-97-2
55-91-4
60-51-5
540-73-8
77-78-1
Substance
Chlordane
Chlorine
Chlorine dioxide
Chloroform
bis-Chloromethyl ether
1 -(o-Chloropheny l)thiourea
Chloropropionitrile, 3-
Creosote (coal tar)
Cresol, 2-
Crotonaldehyde
Cumene
Cyanogen chloride
Cyclohexane
Cyclohexanone
Diborane
Dichlorobenzene, 1,2-
Dichlorobenzene, 1,3-
Dichlorobenzene, 1,4-
Dichlorophenylarsine
Diethylphthalate
Diethyl O-pyrazinyl phosphorothioate, O,O-
Diisopropylfluorophosphate (DFP)
Dimethoate
Dimethylhydrazine
Dimethyl sulfate
Basis2
D
C
C
A, C, D
C
B
B
A
A, D
A, C, D
A
B, C
A
A
C
A
A
A
B
A
B
B
B.D
A, C, D
A, D
IDLH3
(e/m3)
0.5
0.0289
0.0138
2.437
0.0025
0.046
0.09
NA
1.104
0.143
4.416
3.6
4.468
2.806
0.017
1.2
NA
0.9
0.4
NA
0.035
0.036
0.3
0.037
0.036
Vapor Pressure4
(mm He ©20°C)
0.00001
5200
760
160
30 (22°C)
NA
5 (46°C)
NA
0.31 (25°C)
19
8
1010
78
5
30000 (17°C)
1
2.3 (25°C)
1.3
0.087 (25 °C)
0.00165 (25°C)
0.003 (30°C)
0.579
8.3E-06 (25°C)
68 (24.5°C)
0.5
•
Conservative
Percent
Composition5
3
NA
NA
8
NA
NA
NA
8
20
3
8
NA
13
19
NA
19
11
4
NA
3
NA
NA
NA
3
4
Volume VII
III-11
External Review Draft
Do Not Cite or Quote
-------
CAS
Number1
534-52-1
88-85-7
123-91-1
152-16-9
107-49-3
298-4-4
541-53-7
115-29-7
72-20-8
106-89-8
16752-77-5
64-17-5
110-80-5
140-88-5
100-41-4
151-56-4
82-41-4
640-19-7
50-0-0
142-82-5
302-1-2
79-19-6
74-90-8
7647-1-0
7664-39-3
TABLE III-l
Summary of Chemicals of Potential Concern for Short-Term Exposures9
Substance
Dinitro-o-cresol, 4,6- & salts (2)
Dinoseb
Dioxane, 1,4-
Diphosphoramide, octamethyl-
Diphosphoric acid, tetraethyl ester
Disulfoton
Dithiobiuret
Endosulfan
Endrin, & metabolites
Epichlorohydrin
Ethanimidothioic acid, N-[[(methylamino)carbonyl]oxy]-,
methyl ester (Methomyl)
Ethanol
Ethoxyethanol, 2-
Ethyl acrylate
Ethylbenzene
Ethyleneimine'
Fluorine
Fluoroacetamide
Formaldehyde
Heptane
Hydrazine
Hydrazinecarbothioamide
Hydrocyanic acid
Hydrogen chloride
Hydrogen fluoride
Basis2
B, D
B, D
A
B, D
B
B, D
B, D
B, D
B, D
A, C,D
B
A
A
A
A
B.C.D
B, C, D
B,D
A, C, D
A
A, C, D
B
B, C, D
C
C
IDLH3
(slm3)
0.005
0.045
1.798
0.008
0.005
0.02
0.05
0.008
0.002
0.283
0.1
6.209
1.839
1.226
3.468
0.176
0.039
NA
0.0245
3.067
0.0655
0.092
0.0551
0.0745
0.0245
Vapor Pressure4
(mm Hg @20°C)
0.00032
0.075
29
0.001 (25°C)
0.0002
0.00018
NA
1E-05 (25 °C)
0.000003
13
5E-05 (25 °C)
44
4
29
7
160
76
NA
3883 (25 °C)
40 (22°C)
10
NA
630
31000
783
Conservative
Percent
Composition5
NA
NA
12
NA
NA
NA
NA
NA
1
6
NA
24
24
3
20
NA
NA
NA
11
17
3
NA
NA
18
3
Volume VII
External Revie-
Do Not Cite;
-------
TABLE III-l
Summary of Chemicals of Potential Concern for Short-Term Exposures9
CAS
Number1
7783-7-5
7783-6-4
13463-40-6
78-83-1
465-73-6
62-38-4
62-75-9
67-56-1
78-93-3
60-34-4
108-10-1
624-83-9
75-86-5
298-0-0
91-20-3
86-88-4
13463-39-3
54-11-5
98-95-3
10102-44-0
10102-43-9
79-46-9
62-75-9
20816-12-0
56-38-2
Substance
Hydrogen selenide
Hydrogen sulfide
Iron, pentacarbonyl-
Isobutanol
Isodrin
Mercury, (acetato-O)phenyl-
Methanamine, N-methyl-N-nitroso-
Methanol
Methyl ethyl ketone (2-Butanone)
Methyl hydrazine
Methyl isobutyl ketone (2-Methyl-4-pentanone)
Methyl isocyanate
Methylactronitrile, 2-
Methyl parathion
Naphthalene
Naphthylthiourea, alpha-
Nickel carbonyl
Nicotine, & salts (2)
Nitrobenzene
Nitrogen dioxide
Nitrogen oxide NO
Nitropropane, 2-
N-nitrosodimethylamine
Osmium oxide Os04, (T-4)-
Parathion
Basis2
c
c
c
A
B, D
B
B
A
A
B, C, D
A
B, C, D
B
B
A
B
B,C, D
B, D
A, D
B, D
B, C, D
A
B, D
B
B, D
IDLH3
(g/m3)
0.0033
0.139
0.008
4.839
0.07
0.22
0.19
7.861
8.829
0.0376
2.045
0.007
0.12
0.0034
1.308
0.1
0.0139
0.005
1.005
0.0376
0.1224
0.364
0.19
0.001
0.01
Vapor Pressure4
(mm Hg @20°C)
7200 (21 °C)
13000
40 (31°C)
9
0.000006
0.00012 (25°C)
3
96
- 77.5
38
16
348
0.8
0.00001
0.08
NA
315
0.08
0.27
720
26000
13
2.7
L 7
0.00004
Conservative
Percent
Composition5
NA
NA
NA
20
NA
NA
NA
20
34
NA
19
NA
NA
NA
9
NA
NA
NA
25
NA
NA
20
NA
NA
NA
Volume VII
m-13
External Review Draft
Do Not Cite or Quote
-------
TABLE III-l
Summary of Chemicals of Potential Concern for Short-Term Exposures3
CAS
Number1
108-95-2
62-38-4
103-85-5
298-2-2
75-44-5
7806-51-2
151-50-8
506-61-6
107-12-0
75-55-8
110-86-1
26628-22-8
143-33-9
57-24-9
7783-60-0
7446-11-9
7446-18-6
95-94-3
127-18-4
3689-24-5
78-0-2
109-99-9
509-14-8
1314-32-5
39196-18-4
Substance
Phenol
Phenylmercury acetate
Phenylthiourea
Phorate
Phosgene
Phosphine
Potassium cyanide
Potassium silver cyanide
Propanenitrile
Propylenimine, 1,2-
Pyridine
Sodium azide
Sodium cyanide
Strychnidin- 10-one, & salts (2)
Sulfur tetrafluoride
Sulfur trioxide
Sulfuric acid, dithallium (1 +) salt
Tetrachlorobenzene (assumed 1,2,4,5-)
Tetrachloroethylene
Tetraethyldithiopyrophosphate
Tetraethyl lead
Tetrahydrofuran
Tetranitromethane
Thallic oxide
Thiofanox
Basis2
A, D
B,D
B, D
B.D
B.C.D
B, C, D
B, D
B, D
B, C
B, C, D
A
B,D
B, D
B,D
C
C
B
A
A
B
B, D
A
B, C, D
B
B.D
IDLH3
(e/m3)
0.96
0.22
0.03
0.001
0.0081
0.069
0.025
0.2
0.037
0.233
3.229
0.2
0.025
0.003
0.092
0.03
0.02
NA
1.015
0.01
0.04
5.886
0.032
0.02
0.085
Vapor Pressure4
(mm Hg @20°C)
0.4
9E-06 (35 °C)
NA
0.0008
1215
NA
NA
NA
35
112
16
NA
NA
NA
8000 (21 °C)
344 (25 °C, beta)
NA
40 (146°C)
14
0.00017
0.2
132
8
NA
0.00017 (25°C)
Conservative
Percent
Composition5
10
NA
NA
NA
NA
NA
NA
NA
NA
NA
17
NA
NA
NA
NA
NA
NA
10
13
NA
NA
16
NA
NA
NA
Vo1»me VII
External Revi
Do Not Cite
>te
-------
TABLE III-l
Summary of Chemicals of Potential Concern for Short-Term Exposures3
CAS
Number1
108-98-5
79-19-6
5344-82-1
755045-0
108-88-3
584-84-9
91-8-7
8001-35-2
71-55-6
79-1-6
1314-62-1
1330-20-7
81-81-2
1314-84-7
Substance
Thiophenol
Thiosemicarbazide
Thiourea, (2-chlorophenyl)-
Titanium tetrachloride
Toluene
Toluene-2 ,4-diisocy anate
Toluene-2,6-diisocyanate
Toxaphene
Trichloroethane, 1,1,1-
Trichloroethylene
Vanadium oxide
Xylene
Warfarin, & salts, when > 0.3% (2)
Zinc phosphide, when > 10%
Basis2
B, D
B, D
B, D
C
A
A, C, D
A, C, D
B
A
A
B, D
A
B, D
B, D
IDLH3
(fi/m3)
0.014
0.092
0.046
0.01
1.88
0.0178
0.009
0.2
3.811
5.363
0.035
NA
0.1
0.12
Vapor Pressure4
(mm He @20°C)
2 (25 °C)
NA
NA
NA
21
0.01
0.02
0.4 (25 °C)
100
57.9
NA .
8.763 (25°C)
0.09
NA
Conservative
Percent
Composition5
NA
NA
NA
NA
24
4
4
1
16
17
NA
22
NA
NA
Volume VII
HI-15
External Review Draft
Do Not Cite or Quote
-------
CAS
Number1
Substance
Basis2
IDLH3
(e/m3)
Vapor Pressure4
1mm Hg @20°C)
Conservative
Percent
Composition5
TABLE III-l
Summary of Chemicals of Potential Concern for Short-Term Exposures'
Notes:
' 139 chemicals were selected for further analysis.
1 CAS Number given for parent compound only.
2 A — Wastes projected to be received by WTI during first year of operation
B — Constituents listed as "P" wastes (acutely hazardous according to RCRA)
C — Acutely toxic chemicals identified in CAA 112(r)
D — Extremely hazardous substances from EPCRA
3 Immediately Dangerous to Life or Health (IDLH) value (U.S. EPA 1995c). For chemicals without an IDLH value, but for which a Level of Concern
(LOG) value has been established by U.S. EPA, the LOG multiplied by a factor of 10 was used in place of the IDLH.
4 Vapor Pressure data compiled from the following sources:
Hazardous Substances Data Bank (HSDB). 1991. National Library of Medicine.
Howard, P. H. 1989. Handbook of environmental fate and transport data (Vol. I. Large production and priority pollutants). Chelsea, MI: Lewis
Publishers
Howard, P. H. 1990. Handbook of environmental fate and transport data (Vol. II. Solvents). Chelsea, MI: Lewis Publishers.
Montgomery, J.H., and L.M. Welkom. 1990. Groundwater chemicals desk reference. Chelsea, MI: Lewis Publishers.
5 Average of the maximum concentrations reported for all waste streams containing the compound, according to WTI waste profiles for first year of
operations.
NA Not available.
Volume VII
External Revie- nraft
Do Not Cite ( te
-------
TABLE in-2
Constituents Received in Largest Quantities in Pumpable Waste at the WTI Facility
Constituent
1. Hydrocarbon (unspecified)
2. Cresol
3. Toluene
4. Methyl Ethyl Ketone
5. Methanol
6. Acetone
7. Cyclohexanone
8. Ethyl Acrylate
9. Butanol
10. Xylene
Approximate Quantity in
Pumpable Waste (Ib/yr)
3,200,000
1,000,000
770,000
680,000
590,000
560,000
480,000
470,000
460,000
450,000
Percent of Total
Pumpable Waste
16.8%
5.2%
4.-0%
3.5%
3.1%
2.9%
2.5%
2.4%
2.4%
2.3%
Note:
Source: Appendix 1, Volume III
Volume VII
HI-17
External Review Draft
Do Not Cite or Quote
-------
TABLE lH-3
Hydrogen Chloride and Phosgene Formation from
Decomposition of Chlorinated Hydrocarbons hi
Contact with Flame3
Substance
Carbon tetrachloridei
Chloroform2
Dichloroethane2
Pentachloroethane2
Tetrachloroethane2
Tetrachloroethene2
Trichloroethene2
HC1 Formed
(mg/g chemical combusted)
199
138
240
332
326
238
266
Phosgene Formed
(mg/g chemical combusted)
8
6
ND
2
3
7
1
Notes:
1 Average of three trials.
2 Average of two trials.
3 Source: Sjoberg (1952)
Volume VII
111-18
External Review Draft
Do Not Cite or Quote
-------
TABLE m-4
Wastes and Chemicals Evaluated
Scenario
On-Site Spill
On-Site Fire
On-Site Mixing of Incompatible Wastes
Off-Site Spill
Off-Site Fire
Waste/Chemical Evaluated
Waste consists of 90% methanol/10%.
formaldehyde ("worst-case" waste) or 90%
toluene/10% acetone ("typical" waste).
Consequences of formaldehyde and acetone
releases are assessed.
Waste consists of 15% tetrachloroethene/
85% toluene. Consequences of HC1 and
phosgene releases are assessed.
Waste consisting of 15%
tetrachloroethene/85% methanol mixed with
waste consisting of 70% nitric acid.
Consequences of HC1 releases are assessed.
Waste consists of 90% methanol/10%
formaldehyde ("worst-case waste) or 90%
toluene/10% acetone ("typical" waste).
Consequences of formaldehyde and acetone
releases are assessed.
Waste consists of 85% toluene/15%
tetrachloroethene. Consequences of HC1 and
phosgene releases are assessed.
Volume VII
111-19
External Review Draft
Do Not Cite or Quote
-------
TABLE III-5
Key Assumptions Made in Selecting Chemicals of Potential Concern
Assumption
1. Waste composition data from WTI waste
profile sheets for first year of operations
adequately characterizes future waste.
2. Chronic human impacts off-site could be
avoided through mitigation measures.
3. IDLH values can be used to evaluate the
potential for acute health effects. The more
stringent LOG values were evaluated in a
sensitivity analysis.
4. Substances for which acute data are not
available are less toxic than those for which
data are available.
5. Use of vapor pressure to reflect release
potential.
6. Selection of tetrachloroethene and toluene as
the chemicals of concern for fire scenarios.
7. Selection of HC1 as the chemical of concern for
mixing of incompatible wastes.
Basis
Site-specific waste profile information. The potential
for underestimating risk is reduced by making
conservative assumptions in calculating chemical
concentrations in waste from the information in the
profiles.
Mitigation measures in effect at the WTI facility will
limit migration of spilled wastes and duration of fire
scenarios.
IDLH yalues represent a consistent, relatively
comprehensive set of criteria for assessing the acute
effects of short-term exposures.
Chemicals for which no acute toxicity data are
available are ranked below chemicals with acute
toxicity data.
Represents a consistent basis for comparison.
Selection of toluene for examining heat effects is
believed to be appropriate, given its high
flammability, and high quantity in pumpable waste.
Selection based on review of WTI waste profile and
evaluation of toxic byproducts of combustion.
HC1 represents a high hazard chemical given its
relatively high acute toxicity.
Magnitude of Effect
Medium
Low
High
Low
Low
High
High
Direction of Effect
Unknown
May underestimate
May over or underestimate risk,
depending on the basis for and
uncertainty associated with the
IDLH for a specific chemical.
Unknown
Unknown
Probably overestimates risk,
given high HC1 and phosgene
formation rates for
tetrachloroethene. Selection of
toluene for examining heat
effects is believed to be
appropriate, given its high
flammability, and high quantity
in pumpable waste.
Overestimates
Volume V"
Do
"1 Review Draft
'te or Quote
-------
IV. CHARACTERIZATION OF ACCIDENTAL RELEASES
A. Methodology
Atmospheric release rates for the chemicals of primary concern are estimated for each
accident scenario selected for quantitative evaluation. Release rates and durations are
developed for specific constituents based on facility-specific parameters (e.g., tank volumes,
dike sizes), and short-term modeling techniques. The models account for the
physical/chemical properties of the chemicals (e.g., volatility, density, liquid or gas phase),
and the presence of passive mitigation devices (e.g., concrete dikes and berms). As
discussed hi Chapter II, two release scenarios are evaluated for each on-site accident event:
• No active or automatic mitigation devices (e.g., nitrogen blankets or sprinkler
systems) assumed. Passive mitigation (e.g., dikes, berms) are assumed to be
effective, however.
• Active or automatic mitigation devices are assumed to control emissions. The effect
of mitigation is evaluated through two separate cases, with assumed response times
of ten minutes and one hour, respectively (see Chapter VII).
For the off-site accident events, only scenarios without any active mitigation are
considered.
Wastes consisting of a mixture of chemicals are modeled for all of the events in this
Accident Analysis. Physical and chemical properties for these mixtures are estimated from
the properties of the pure chemicals, weighted by the mass fraction of each chemical
constituent. The procedures used to estimate chemical emission rates for each accident
scenario are summarized below. Details regarding the calculations are presented in
Appendix VII-3.
B. Chemical-Specific Release Rate Calculations
1. On-Site Spill
The on-site spill scenario selected for quantitative evaluation results from a collision
involving one tanker truck hauling liquid waste. To model the single-phase release of a
Volume VII . External Review Draft
rV-1 Do Not Cite or Quote
-------
liquid waste and the subsequent evaporation of the resulting liquid pool, two emission
rates must be determined and compared — the liquid release rate from the truck, £, and
the rate of evaporation from a liquid pool, Epool. The liquid release rate from the truck is
estimated (U.S. EPA 1993b) assuming that the temperature of the liquid after release is
the same as the ambient temperature. The liquid release rate is compared to the.
evaporation rate of a liquid pool, as calculated based on U.S. EPA (1993). Comparing
these two emission rates determines the rate of release to the atmosphere.
In modeling emission rates, the ambient temperature is assumed to be 68 °F (or
20°C), which may underestimate emission rates somewhat on very hot days, and
overestimate emission rates somewhat on very cold days. The annual average
temperature in Pittsburgh is 50°F (or 10°C); the average of the daily maximum
temperatures during July, the hottest month of the year, is 83°F (or 28°C), according to
the historical climatic data (1961-1990) published by the U.S. Department of Commerce
(U.S. DOC 1993). While the temperature of 68°F (or 20°C) used in the emission
modeling may not cover all the possible high temperatures that could occur at the WTI
site, the value is considered adequate for characterizing the ambient temperature in the
WTI vicinity.
In general, if the boiling point of a waste mixture is greater than normal ambient
temperatures, the evaporation rate from the pool determines the rate at which the
chemical enters the atmosphere (U.S. EPA 1993b). In this analysis, the boiling points of
both the formaldehyde/methanol mixture, 97°F (or 36°C) and the acetone/toluene
mixture 201 °F (or 94°C), are well above ambient temperatures. Thus, chemical
emission rates can be estimated by multiplying the total pool evaporation rate, E^,, by
the mass fraction of the chemical in the vapor.
The size of the pool being formed depends on the release rate and duration, and the
presence of containment barriers (e.g., dikes, speed bumps, building walls, etc.) in the
spill vicinity. In the spill scenario, the tanker is assumed to be 9.5 m long and 1.6 m hi
diameter. The area of the hole hi the tanker is assumed to be 0.009 m2 (approximately
equivalent to a 1 V4-inch diameter hole), and is located at the bottom of the tank such that
the full content could be released in 10 minutes, consistent with the Accidental Release
Prevention Requirements: Risk Management Programs under Clean Air Act, Section
112(r)(7); Proposed Rule (40 CFR Pan 68) (U.S. EPA 1995a). For the conservative
case, assuming the 5,000 gallon spill (the assumed volume for one truck) is contained
within the berms hi the truck unloading area, the area of the liquid pool would be
approximately 418 m2. For the typical case, assuming the 100 gallon spill spreads to a
depth of 1 cm, the area of the liquid pool would be approximately 38 m2. Calculations
Volume VII External Review Draft
IV-2 Do Not Cite or Quote
-------
of spill areas and formaldehyde and acetone release rates for the spill scenarios are
described hi Appendix VII-3.
2. On-Site Fire
The on-site fire scenario selected for quantitative evaluation is a storage tank rupture
in the Organic Waste Tank Farm hi the presence of an ignition source, resulting in a
pool fire. The contents of the storage tanks are a mixture of 15 % tetrachloroethene and
85 % toluene, as discussed hi Chapter III. The total burning rate is estimated from two
factors: 1) the burning velocity; and 2) the size of the burning pool. The burning
velocity for a liquid with a boiling point above ambient temperature is given by FEMA
(1993) and Burgess et al. (1961). The pool size is defined by the size of the secondary
containment area hi the building, or 180 m2 hi this scenario.
Combustion products that may be emitted during a fire include NOX, SO2 or HC1.
Phosgene emissions are also possible as a product of incomplete combustion. O'Mara et
al. (1971) reported that the potential for phosgene formation during combustion of
chlorinated hydrocarbons could be evaluated based on the following parameter:
Number of Chlorine Atoms - Number of Hydrogen Atoms
Number of Carbon Atoms
Phosgene formation is likely when a>0.4. Thus, for example, phosgene could be
formed during the combustion of carbon tetrachloride (a =4), chloroform (a=2),
tetrachloroethene (fl=2), and trichloroethene (c=l), but would not be expected during
the combustion of chlorobenzene (fl=-0.7), dichlorobenzene (a=-0.3), or trichloroethane
(a=0). The formation of HC1 and phosgene from the combustion of several chlorinated
hydrocarbons was estimated by Sjoberg (1952), as discussed hi Chapter III. According
to Sjoberg (1952), combustion of tetrachloroethene is estimated to form 238 mg/g of
HC1, and 7.0 mg/g of phosgene. These values were used for estimating HC1 and
phosgene releases. Details regarding the calculation of HC1 and phosgene release rates
are presented hi Appendix VII-3.
In the WTI Accident Analysis, the Automated Resource for Chemical Hazard
Incident Evaluation (ARCHIE) model developed by FEMA (1993) is used to assess heat
effects of fires. For fires and explosions, ARCHIE can be used to estimate the size of a
pool of burning substances, the height of the expected resulting flame, the radius from
the center of the burning pool within which individuals could be potentially fatally
Volume VII External Review Draft
FV-3 Do Not Cite or Quote
-------
burned, and the radius from the center of the burning pool within which individuals
could potentially experience second degree burns or severe pain. ARCHIE modeling is
performed to examine the heat impacts resulting from a fire ignited both immediately
after a spill, and after a pool achieves its maximum size. The radius of the fire, the
fatal zone radius, and the injury zone radius are calculated.
The hazards associated with a possible fireball incident are also estimated using the
ARCHIE model. A fireball could be formed if a sealed or inadequately vented container
of a flammable liquid or liquefied compressed gas is exposed to an external fire or other
source of heat sufficient to cause explosion or violent rupture of the container (FEMA
1993). If the container is fairly full and is fitted with a pressure relief device, it may
vent a considerable portion of its contents before the occurrence of a boiling liquid
expanding vapor explosion (BLEVE).
The fireball scenario can occur if (1) the container releases only a portion of its
content (e.g. a hole one foot below the liquid level); (2) the spill ignites immediately
after the spill; and (3) the container's ventilation system malfunctions. It is highly
unlikely that all three of these conditions would occur during an on-site or off-site
accident. Nazario (1988) indicates that the critical parameter for a BLEVE to occur is
the degree of vaporization of the chemical inside the container. If more than 10% of the
vessel contents will vaporize when depressurized (or pressure-relief-valve setpoint), the
vessel has the potential for a BLEVE (Nazario 1988). Based on the relatively low vapor
pressures of tetrachloroethene and toluene and the storage conditions for the chemicals, it
is unlikely that a BLEVE would occur during a fire incident involving only a contained
on-site storage tank or an off-site tanker truck. However, a fireball scenario may occur
if an on-site (or off-site) spill spreads, ignites, and the flames engulf another tank (or
tanker truck) with sufficient heat to cause an explosion.
In assessing fireballs, ARCHIE assumes that the fuel is similar hi characteristics
(both physical and chemical) to liquefied compressed propane and treats the fuel as if it
were liquefied propane. Propane has a boiling point much lower than a
tetrachloroethene/toluene mixture and is normally stored under pressure. A
tetrachloroethene/toluene spill, where the liquid has a boiling point greater than the
ambient temperature and is stored under ambient temperature and pressure, is not
expected to result hi a fireball. A large amount of heat would be required to raise the
tetrachloroethene/toluene temperature to the boiling point and to transfer the liquid-phase
chemical to the gas-phase, so that vapors can be formed rapidly. In addition,
tetrachloroethene/toluene vapors will continue to escape from the tank during the heating
through the ventilation system, reducing the quantity of chemical available for a possible
fireball scenario if the tank temperature actually reached the chemical boiling point..
Volume VII External Review Draft
IV-4 Do Not Cite or Quote
-------
Detailed information regarding the ARCHIE modeling and the heat impacts due to
fires is presented in Appendix VII-3.
3. On-Site Mixing of Incompatible Wastes
The on-site mixing of incompatible wastes scenario selected for quantitative
evaluation results from an accidental pumping of incompatible waste into an improper
storage vessel. This assumes pumping of 5,000 gallons of a mixture of chlorinated
hydrocarbons (15% tetrachloroethene/85% methanol mixture) into a storage vessel
containing 5,000 gallon of mineral acids (70% nitric acid solution). The mixing results
in the release of gaseous hydrogen chloride (ASTM 1986).
To model the release of HC1 resulting from the mixing of incompatible wastes, it is
assumed that as the two wastes mix inside the storage vessel, the reaction between the
two wastes to produce HC1 is instantaneous. The pumping rate of the contents of the
tanker truck into the storage vessel is estimated to be 250 gallon/mm (Victorine 1995b).
The release of HC1 into the atmosphere is assumed to occur at ambient temperature and
pressure through the vapor recovery system and vent.
The total amount of HC1 released is calculated by assuming that all chlorine hi the
waste reacts instantaneously to form HC1. Using this approachresults hi a potentially
significant overestimate of HC1 releases. Details regarding the calculation of HC1
emissions are presented hi Appendix VII-3.
4. Off-Site Tanker Truck Spill
The size of the off-site spill depends on the release rate and duration, and the
presence of containment barriers (e.g., street curbs, speed bumps, building walls, etc.)
hi the spill vicinity, if any. As hi the case of the on-site spill, chemical emission rates
would be determined by the rate of evaporation from the liquid pool.
Assuming the road on which the spill occurs is flat and has no curbs that are capable
of acting as a containment barrier, the liquid pool resulting from the conservative
5,000-gallon spill is assumed to reach a maximum length of approximately 49 m,
assuming pool depth of 1 cm (see Appendix VII-3). This assumes the pool spreads in all
directions at an equal rate, with liquids reaching the edge of the road running off onto
soil or into a ditch. Assuming that the road is not sloped from the center line to the
sides is conservative; hi reality, it is likely that liquid would run off from the center of
the road to the sides, reducing the size of the spill. The assumption of no roadway curbs
appears to be appropriate for the local access route based on observations made during a
site visit. Assuming the width of die road is 15 m, the area of the pool is approximately
Volume VII External Review Draft
IV-5 Do Not Cite or Quote
-------
735 m2 (Figure IV-1). In the typical 100-gallon spill case, the pool size is approximately
38 m2 (assuming a pool depth of 1 cm), and would not reach the edge of the road.
Details regarding emission calculations for the off-site soil scenario are provided hi
Appendix VII-3.
5. Off-Site Tanker Truck Spill with Fire
The off-site fire, scenario is similar to the off-site spill scenario, with the additional
presence of an ignition source. Chemical emission rates are calculated using the same
approach as for the on-site fire scenario. Details regarding emission calculations are
presented in Appendix VII-3.
The ARCHIE model is used to estimate the heat effect posed by the off-site fire
scenario. Detailed information regarding the ARCHIE modeling and the heat impacts is
presented in Appendix VII-3.
C. Summary of Results and Key Assumptions
The chemical-specific emission rates calculated for each accident scenario are
summarized in Table IV-1. The major assumptions made hi estimating chemical emission
rates hi the Accident Analysis are summarized hi Table IV-2.
Volume VII External Review Draft
IV-6 Do Not Cite or Quote
-------
TABLE V-6
Summary of Downwind Air Concentrations for the Off-Site Fire Scenarios
Chemical of
Concern
Phosgene
HC1
Phosgene
HC1
Spill Volume
(gal)
5,000
5,000
100
100
Meteorology
Typical
Conservative
Calm/Inversion
Typical
Conservative
Calm/Inversion
Typical
Conservative
Calm/Inversion
Typical
Conservative
Calm/Inversion
Downwind Concentration (ppm)2
100m
0.011
2.6
NE1
1.0
243
NE
0.001
0.26
NE
0.10
24.3
NE
500m
0.0062
0.42
NE
0.57
39
NE
0.0006
0.042
NE
0.057
3.9
NE
1000m
0.0014
0.25
NE
0.13
23
NE
0.0001
0.025
NE
0.013
2.3
NE
2000m
0.00063
0.11
NE
0.058
10
NE
0.00006
0.011
NE
0.0058
1.0
NE
Notes:
1 ME: Not Evaluated.
2 Downwind distance from the edge of the fire.
Volume VII
V-10
External Review Draft
Do Not Cite or Quote
-------
TABLE V-5
Summary of Downwind Air Concentrations for the On-Site Fire Scenario
Chemical of
Concern
Phosgene
HC1
Phosgene
HC1
Spill Size
(gal)
20,000
20,000
100
100
Meteorology
Typical
Conservative
Calm/Inversion
Typical
Conservative
Calm/Inversion
Typical
Conservative
Calm/Inversion
Typical
Conservative
Calm/Inversion
Downwind Concentrations (ppm)1
100m
3
—
NE1
-
-
NE
-
-
NE
-
-
NE
500m
—
0.0080
NE
--
0.72
NE
--
0.0008
NE
-
0.07
•NE
1000m
0.0046
0.14
NE
0.42
12.8
NE
0.0005
0.014
NE
0.04
1.3
NE
2000m
0.0043
0.053
NE
0.40
4.9
NE
0.0004
0.005
NE
0.04
0.5
NE
Notes:
1 NE: Not Evaluated.
2 Downwind distance from the property line to the east or west across the Ohio River to the south, or the existing railroad to the north, whichever is
closer to the location of the release. For the on-site fire, maximum downwind distance was calculated from the railroad to the north, approximately
75 m from the edge of the fire.
' --: Concentration less than 0.000 1 ppm.
Volume VII
/ \
External Review Draft
Do Not Cite f ^te
-------
TABLE V-4
Summary of Downwind Air Concentrations for the Off-Site Spill Scenarios
Chemical of
Concern
Formaldehyde
Acetone
Formaldehyde
Acetone
SpiU Volume
(gal)
5,000
5,000
100
100
Meteorology
Typical
Conservative
Calm/Inversion
Typical
Conservative
Calm/Inversion
Typical
Conservative
Calm/Inversion
Typical
Conservative
Calm/Inversion
Downwind Concentration (ppm)1
100m
660
6100
6700
64
450
1,000
25
260
280
5.4
42
82
Note:
1 Downwind distance from edge of spill
500m
61
830
1000
6.0
63
175
1.5
27
55
0.32
5.3
14.9
1000m
19
280
440
1.9
28
81
0.5
9.3
22
0.10
2.2
6.6
2000m
5.7
100
170
0.56
12
37
0.1
2.7
6.8
0.03
0.9
2.5
Volume VII
V-8
External Review Draft
Do Not Cite or Quote
-------
TABLE V-3
Summary of Downwind Air Concentrations for the On-Site Mixing of Incompatible Wastes Scenario
Chemical of Concern
HC1
HC1
Waste Volume
(gal)
5,000
200
Meteorology
Typical
Conservative
Calm/Inversion
Typical
Conservative
Calm/Inversion
Downwind Concentration (ppm)1
100m
260
4100
3700
11
120
170
500m
78
600
920
1.5
25
51
1000m
26
260
420
0.5
9.5
22
2000m
8.1
100
170
0.15
3.0
7.5
Note:
1 Downwind distance from the property line to the east or west across the Ohio River to the south, or the existing railroad to the north, whichever is
closer to the location of the release. For the on-site spill mixing of incompatible waste, maximum downwind distance was calculated from the railroad
to the north, approximately 75 m from the edge of the spill.
-7
Vol"me VII
/ \
External Review Hraft
Do Not Cite \e
-------
TABLE V-2
Summary of Downwind Air Concentrations for the On-Site Spill Scenario
Chemical of
Concern
Formaldehyde
Acetone
Formaldehyde
Acetone
Spill Size
(gal)
5,000
5,000
100
100
Meteorology
Typical
Conservative
Calm/Inversion
Typical
Conservative
Calm/Inversion
Typical
Conservative
Calm/Inversion
Typical
Conservative
Calm/Inversion
Downwind Concentrations (ppm)1
100m
194
2016
3465
19
140
370
9.7
120
160
2.0
21
45
500m
30
491
868
2.7
35
100
1.2
22
46
0.25
4.3
13
1000m
10
224
404
1.0
16
51
0.40
8.1
20
0.08
2.0
6.0
2000m
3
82
159
0.3
7.2
25
0.12
2.6
6.4
0.03
0.81
2.3
Note:
1 Downwind distance from the property line to the east or west across the Ohio River to the south, or the existing railroad to the north, whichever is
closer to the location of the release. For the on-site spill, maximum downwind distance was calculated from the railroad to the north, approximately 75
m from the edge of the spill.
Volume VII
V-6
External Review Draft
Do Not Cite or Quote
-------
TABLE V-l
Stability Wind Speed Combinations Used
to Detennine "Conservative" Meteorological Conditions
Atmospheric
Stability
Categories
A
B
C
D
E
F
Wind Speed (meters/sec)
1
*
*
*
*
*
*
1.5
*
*
*
*
*
*
2
*
*
*
*
*
*
2.5
*
*
*
*
*
*
3
*
*
*
*
*
*
3.5
*
*
*
*
*
4
*
*
*
*
*
4.5
*
*
*
*
5
*
*
*
*
8
*
*
10
*
*
15
*
.20
*
Note:
Matrix of conditions taken from U.S. EPA 1992b. It is only necessary to consider the stability-wind speed conditions
relevant to the WTI site, which are marked with an asterisk (*).
Volume VII
V-5
External Review Draft
Do Not Cite or Quote
-------
C. Summary of Results and Key Assumptions
Tables V-2 through V-4 summarize the downwind concentrations at four downwind
distances for the accident scenarios evaluated using the SLAB model (on-site spill, on-site
mixing of incompatible wastes, and off-site spill). Complete SLAB model outputs and
modeling parameters are presented hi Appendix ¥11-4 and associated attachments. .
The one-hour average concentrations predicted by the ISC-COMPDEP model for the
typical meteorology and each of the 54 screening meteorological conditions are presented in
Appendix VIM for both the on-site and off-site fire accident scenarios. Tables V-5 and V-6
summarize the downwind concentrations at four downwind distances for the two fire
scenarios evaluated. In the Accident Analysis, concentrations resulting from the fire
scenarios associated with large quantity releases (on-site 20,000-gallon spill and off-site
5,000-gallon spill) are modeled directly using ISC-COMPDEP. Fire scenarios associated
with the small quantity releases (on-site spill of 200 gallons, and off-site spill of 100 gallons)
can not be reliably modeled using ISC-COMPDEP because the releases associated with such
small fires are short-lived and should not be treated as continuous plumes. However, the
off-site impacts associated with the small quantity fire scenarios can be estimated from the
ISC-COMPDEP results for the large quantity fire scenarios. As discussed in Appendix VII-
4, the off-site concentrations resulting from the large volume fire scenarios, based on the
considerations of source size, emission rate, emission duration, and concentration averaging
time are predicted to be at least 10-fold lower than concentrations resulting from small
volume fire scenarios. Thus, in the Accident Analysis, air concentrations for the typical fire
events are conservatively estimated to be 10-fold lower than the concentrations modeled
using ISC-COMPDEP for the large fire scenarios.
The major assumptions made hi order to perform the SLAB or ISC-COMPDEP
dispersion modeling are listed in Table V-7.
Volume VII External Review Draft
V-4 Do Not Cite or Quote
-------
same stack. Thus, only by screening all 54 conditions can the worst-case meteorology
and maximum ground-level concentration be identified at each downwind distance. In
general, however, the conservative meteorological condition reflects a stable atmosphere
with low windspeed, e.g., a windspeed of 1.5 m/sec and Stability Category F, as
indicated in U.S. EPA (1987).
As a sensitivity analysis, ISC-COMPDEP is also used in conjunction with the one-
year real-tune meteorological data to further evaluate the off-site impacts of the fire
scenarios during conservative meteorology. A more detailed discussion of the SLAB and
ISC-COMPDEP modeling of conservative meteorological conditions is presented in
Appendix ¥11-4.
3. Calm/Inversion Conditions
Calm/inversion meteorology represents the most stable meteorological condition that
may occur at the WTI site, and thus results hi the highest off-site concentrations hi air hi
the event of an accidental release. This hypothetical meteorology assumes that
emissions accumulate hi the air immediately above the source for one hour during calm
conditionsand stable atmosphere, and are then transported downwind under low wind
speeds. Additional emissions from the spill, if there is sufficient quantity for further
volatilization after the calm hour, would travel downwind as a continuous plume.
The limited mixing hi the surface layer imposed by the temperature inversion is
represented by a mixing height of 100 m hi the SLAB model, and the worst-case
meteorology is represented by the combination of low wind speed (1 m/sec) and stable
atmosphere (Monin-Obukov length of 8.3m, approximately equivalent to Pasquill-Gifford
atmospheric stability of E or F based on the Liu-Durran regression equation, as
referenced by Randerson (1984). It is similar, hi theory, to the calm meteorological
condition evaluated for the routine stack and fugitive emissions study for WTI, where
emissions during the calm hours are accumulated and released at the end of the calm
period (see Volume IV).
As previously stated, the ISC-COMPDEP model is not appropriate for use when
evaluating atmospheric dispersion of accidental releases under calm wind conditions.
Potential releases associated with the on-site and off-site fire scenarios under
calm/inversion conditions have therefore not been evaluated. However, the impacts for
the fire scenarios under this calm/inversion meteorological condition are not expected to
differ significantly from those predicted for the conservative meteorology.
Volume VII External Review Draft
V-3 Do Not Cite or Quote
-------
with the health-based reference concentrations. The 30-minute average concentrations are
obtained by multiplying the ISC-COMPDEP results by a factor of 1.15 (U.S. EPA 1992b,
Turner 1967).
The three meteorological conditions evaluated in the Accident Analysis are described
below.
1. Typical Conditions
A hybrid surface meteorological data set was developed for use in the dispersion
modeling of the stack and fugitive emissions from the WTI facility (see Volume IV).
This database represents meteorological conditions from April, 1992 through March,
1993. Based on these data, a "typical" meteorological condition was determined to be
neutral atmosphere (Pasquill-Gifford Stability Category D) with average wind speed (3.2
m/sec). Specifically, neutral atmospheric conditions (Stability Category D) are the most
frequently measured at the WTI facility, occurring approximately 57% of the time, and
the average windspeed during non-calm hours at the WTI facility is 3.2 m/sec (see
Volume IV). This set of conditions was used to represent typical conditions using both
the SLAB model (for non-fire scenarios) and the ISC-COMPDEP model (for fire
scenarios). As a sensitivity analysis, ISC-COMPDEP is also used in conjunction with
the one-year real-time meteorological data to evaluate the off-site impacts of the fire
scenarios during typical meteorology. The selection of the wind speed and atmospheric
stability characterizing the typical meteorological condition is discussed in Appendix
VIM.
2. Conservative Conditions
For each accident scenario, 54 combinations of atmospheric stability and wind speed
are evaluated to determine which combination results in the maximum downwind ground
level concentrations off-site. These combinations correspond to non-calm meteorological
conditions at the WTI site, and are identified from the matrix of possible conditions
presented hi U.S. EPA (1992b). The 54 combinations shown in Table V-l are evaluated
to determine the conservative meteorological conditions and resulting concentrations
using both the SLAB model (for non-fire scenarios) and the ISC-COMPDEP model (for
fire scenarios).
It is necessary to examine all 54 meteorological conditions to determine the
maximum ground-level concentrations at different downwind distances. For example,
the maximum ground-level concentration for a receptor far from a stack would occur
during a stable low-wind condition, while an unstable high-wind condition would result
hi the highest ground-level concentration for a receptor immediately downwind of the
Volume VII External Review Draft
V-2 Do Not Cite or Quote
-------
V. ATMOSPHERIC DISPERSION MODELING
A. Model Selection
In the Accident Analysis, atmospheric dispersion modeling of accidental releases was
performed using the SLAB and ISC-COMPDEP models. SLAB is selected for modeling
vapor releases from the spill and mixing of incompatible waste scenarios. It is a fully-
documented model released by Lawrence Livermore National Laboratory (Ermak 1990), and
listed by the U.S. EPA for use hi modeling hazardous/toxic air pollutant releases (U.S. EPA
1993b). The model simulates both neutral and denser-than-air releases, and. allows for
continuous, finite duration, and instantaneous releases as well as automatic transition of
continuous plume into transient plume with various tune-averaged concentrations at the
receptor locations.
The ISC-COMPDEP model is selected for modeling the on-site and off-site fire scenarios
for several site-specific reasons. ISC-COMPDEP is a steady-state Gaussian model that can
be used for both simple and complex terrain situations. Because of the high temperatures
associated with the fire scenarios, the ability to model plume rise is critical. In addition,
unlike SLAB, ISC-COMPDEP incorporates buoyant plume rise algorithms that allow the
gradual or transitional rise of plumes to be computed. A complete description of ISC-
COMPDEP is provided hi Volume IV (Ah- Dispersion Analyses).
Details regarding the use of the SLAB and ISC-COMPDEP models in the Accident
Analysis are provided hi Appendix VIM.
B. Meteorological Conditions
For the accident scenarios modeled using SLAB (on-site and off-site spills, and on-site
mixing of incompatible wastes), off-site chemical concentrations hi air are evaluated for three
meteorological conditions: 1) "typical;" 2) "conservative;" and 3) calm/inversion. For each
meteorological condition, 30-minute average concentrations were calculated using SLAB, to
allow for a direct comparison of IDLH values. For the on-site and off-site fire accident
scenarios modeled using ISC-COMPDEP, "typical" and "conservative" meteorological
conditions are evaluated. The ISC-COMPDEP model is not appropriate for use when
calculating atmospheric dispersion under calm/inversion conditions because the basic
Gaussian steady-state assumption becomes invalid. The one-hour average concentrations
predicted by the ISC-COMPDEP model are converted to 30-minute averages for comparison
Volume VII External Review Draft
V-l Do Not Cite or Quote
-------
\
\
Area of off-site
spill = 735 m2
\
Figure IV-1
WTI ACCIDENT ANALYSIS, OFF-SITE SPILL ANALYSIS
AREA OF OFF-SITE SPILL
IV-9
-------
TABLE IV-2
Key Assumptions Made in Estimating Chemical Emission Rates
Assumption
Basis
Magnitude of Effect
Direction of Effect
1. All chlorine in the waste is converted to
HC1 in the mixing of incompatible waste
scenario.
Conservative assumption due to lack of data
regarding actual conversion rates. A fraction of
the chlorine would be expected to react to form
less hazardous compounds.
High
Overestimates
2. Ambient temperature assumed to be 68°F
(or 20'C).
Typical temperatures in the East Liverpool area.
Low
Likely to overestimate
emissions expected on
most days, while
underestimating emissions
on some days.
3. Roadway is assumed to be flat for the off-
site spill scenario.
Conservative assumption due to variability in
actual in actual road conditions.
Medium
Likely to overestimate
emissions in most cases.
If hilly, could
overestimate if near
bottom of hill; or could
underestimate if near top
of hill. A peaked road
would likely reduce the
size of the pool.
4. The limited available data from Sjoberg
(1952) can be used to quantify emissions
of HC1 and phosgene in the event of a fire.
The Sjoberg (1952) is an older investigation, but
provides the most complete data for quantifying
emissions in the event of a fire involving
chlorinated waste.
Medium
Unknown
5. Spills will spread to a depth of 1 cm.
U.S. EPA (1987); Moorhouse and Carpenter
(1986)
Low
Expected to somewhat
overestimate emissions if
surface is not flat, or if
berms or drains are
present.
6. Ambient wind speed assumed to be 3.2
. m/sec.
Average windspeed at the WTI facility based on
site-specific data.
Medium
Likely to overestimate
emissions under low wind
or calm conditions.
Volume VII
IV-8
External Review Draft
Do Not Cite or Quote
-------
TABLE IV-1
Chemical-Specific Emission Rates
Scenario
On-Site Spill
• Formaldehyde
• Acetone
On-Site Fire
• HC1
• Phosgene
On-Site Mixing of
Incompatible Wastes
• HC1
Off-Site Spill
• Formaldehyde
• Acetone
Off-Site Fire
• HC1
• Phosgene
Conservative Event
Average
Emission Rate
(kg/min)
62.4
27.9
21.6
0.62
107.4
110.4
49.1
88.2
2.6
Duration
(min)
52
304
117
117
20
29
172
7.2
7.2
Typical Event
Average
Emission Rate
(kg/min)
5.7
2.5
9.1
0.27
4.3
5.6
2.5
4.5
0.13
Duration
(min)
11
66
2.8
2.8
10
11
66
2.8
2.8
Volume VII
rv-7
External Review Draft
Do Not Cite or Quote
-------
TABLE V-7
Key Assumptions Made in Dispersion Modeling
Assumption
Basis
Magnitude of Effect
Direction of Effect
SLAB Modeling
1. Source temperature assumed to be 20°C
2. Source height assumed to be 0.
3. Receptor elevation assumed to be 0.
4. Building wake effect not considered.
5. Typical meteorology represented by D-
stability and 3.2 m/sec winds.
6. Conservative meteorology defined by
screening meteorology
7. Calm/Inversion meteorology assumed to be
calm hours followed by stable low wind
condition.
Reflects typical temperatures in the East
Liverpool Area. The source temperature
variation is insignificant in the dispersion
analysis.
Simplifying assumption.
Simplifying assumption. May overestimate
downwind concentrations.
Simplifying assumption.
Site-specific meteorology data.
Approach outlined in U.S. EPA (1992b), allows
for selection of meteorology which results in
maximum concentrations under different
accident scenarios
Simplifying assumption.
ISC-COMPDEP Modeling
1 . Highest terrain elevation assumed for
receptors of the same downwind distance.
2. 30-minute average concentrations converted
from 60-minute averages calculated by ISC-
COMPDEP Model.
Simplifying assumption.
Required to allow comparison to IDLH values.
Low
Low
Low
Medium
Low
Low
Low
Unknown
Overestimates
Overestimates. The
overestimation is not
significant based on the
terrain elevations in the area
near the WTI facility.
May over or underestimate
downwind concentrations
for elevated stack release.
May overestimate
.downwind concentrations
for ground-level spill.
Unknown. May over or
underestimate during any
given event.
Overestimates for almost all
meteorologic conditions
Significant overestimates for
almost all meteorologic
conditions
Low
Low
Likely overestimates
Likely overestimates
Volume VII
V-ll
External Review Draft
Do Not Cite or Quote
-------
VI. SEVERITY OF CONSEQUENCES AND PROBABILITY OF
OCCURRENCE
The results of the Accident Analysis for the WTI facility are characterized in terms of
both severity of consequence and probability of occurrence. This approach is consistent with
the guidance established by U.S. EPA (1987) and FEMA (1993), as discussed in Chapter I.
As shown in Table VI-1, the severity of consequence is ranked as minor, moderate.
major, or catastrophic, based on the distance over which predicted concentrations in
potentially inhabited areas could potentially exceed the NIOSH Immediately Dangerous to
Life or Health (IDLH) values. For on-site accident scenarios, the nearest inhabited areas are
conservatively assumed to be the property line to the east or west, across the Ohio River to
the south, or across the existing railroad tracks to the north. In each case, the nearest
inhabited area is at least 75 m from the location of the on-site accident. For off-site accident
scenarios, inhabited areas are assumed to be immediately adjacent to the location of release.
These assumed locations of inhabited areas are conservative because they represent the
closest possible resident; in most situations, the closest resident would be further away from
the release.
In develop ing the criteria shown in Table VI-1, the guidelines presented in FEMA
(1993) have been modified to correspond to distances over which IDLH values are predicted
to be exceeded. This involves a consideration of the population density within specific
distances of the site, and the width of a contaminant plume in air as it moves away from the
source. Based on 1990 census data approximately 25 to 50 people live within about 175 m
of the facility, and approximately 1,000 to 1,500 people live within about 1,100 m of the
facility. As a plume moves away from the source, its width (as described as concentrations
within one standard deviation of the maximum, centerline concentration) would cover an arc
of about 5° to 10°.
For example, given the location of the WTI facility along the Ohio River, it can be
assumed that approximately 1,000 to 1,500 people live within a rough semicircle (a 180°
arc) with a radius of 1,100 m. Assuming that a contaminant plume with concentrations
higher than IDLH values has a width of 10°, the average number of individuals within
1,100 m who would be exposed to concentrations in excess of the IDLH would be
approximately 50 to 100. Within 175 m of the site, the average number of individuals
exposed to concentrations in excess of the IDLH would be less than 10. In the Accident
Volume VII External Review Draft
VI-1 Do Not Cite or Quote
-------
Analysis, it was assumed that an exceedance of an IDLH value in inhabited areas would have
the potential to cause injuries. Thus, the consequence of any event for which IDLH values
are predicted to be exceeded up to a distance of 100 m into inhabited areas (i.e., about
175 m from the source for on-site events, or 100 m from the source for off-site events) is
ranked as moderate, corresponding to less than 10 people on average exposed to
concentrations exceeding the IDLH. The consequence of any event for which IDLH values
are predicted to be exceeded up to a distance of 1,000 m into inhabited areas is ranked as
major, corresponding to up to 100 people on average exposed to concentrations exceeding the
IDLH. Events which do not result in exceedances of IDLH values are ranked as minor.
whereas events where IDLH values are exceeded to distances greater than 1,000 m are
ranked as catastrophic.
Ranking by probability of occurrence is performed using the general criteria presented in
FEMA (1993) and shown in Table VI-2. As indicated in Table VI-2, probability of
occurrence has been ranked as common, likely, reasonably likely, unlikely, or very unlikely.
based on the likelihood of the accident event, the composition of the waste, and the
meteorological conditions. FEMA (1993) presents the following guidelines for evaluating
accident probability: common, expected to occur one or more tunes each year on average;
likely, expected to occur at least once every 10 years on average; reasonably likely.
predicted to occur between once every 10 years and once every 100 years on average;
unlikely, predicted to occur between once every 100 years and once every 1,000 years on
average; and very unlikely, predicted to occur less than once hi 1,000 years.
A. Severity of Consequences
The consequence rankings developed for the various accident scenarios are summarized
for on-site and off-site events hi Tables VI-3 and VI-4, respectively. The basis for these
rankings is discussed below.
1. On-Site Spill
For the on-site spill scenario, four separate events are evaluated:
• Conservative spill (5,000 gallon) of formaldehyde-containing waste.
• Conservative spill (5,000 gallon) of acetone-containing waste.
• Typical spill (100 gallon) of formaldehyde-containing waste.
• Typical spill (100 gallon) of acetone-containing waste.
Volume VII External Review Draft
VT-2 Do Not Cite or Quote
-------
The results of the consequence analysis for these events are summarized in Table
VI-5, and are discussed below.
a) Conservative Spill of Formaldehyde-Containing Waste
In the event of a 5,000 gallon spill of liquid waste containing 10%
formaldehyde, and assuming no active or automatic mitigation measures or
emergency response, exceedances of the IDLH value were predicted to occur up to
640 meters (m) downwind in potential receptor areas under typical meteorological
conditions. Under conservative and calm/inversion meteorological conditions,
exceedances of the IDLH for formaldehyde are predicted to occur up to 4,800 m
and 8,500 m downwind, respectively.
Given the large distance over which the IDLH value for formaldehyde could
potentially be exceeded, the severity of consequence for this scenario is judged to be
major to catastrophic, depending on the meteorological conditions.
b) Conservative Spill of Acetone-Containing Waste
In the event of a 5,000 gallon spill of liquid waste containing 10% acetone,
exceedances of the IDLH value for acetone are not predicted to occur at any off-site
inhabited locations. Thus, the severity of consequence for this event is judged to be
minor.
c) Typical Spill of Formaldehyde-Containing Waste
In the event of an on-site spill of 100 gallons of liquid waste containing 10%
formaldehyde, exceedances of the IDLH value are predicted to occur up to about 40
m downwind hi potentially inhabited areas under typical meteorological conditions,
assuming no active mitigation or emergency response. Under conservative and
calm/inversion meteorological conditions, exceedances of the IDLH for
formaldehyde are predicted to occur up to 550 m and 1,000 m downwind,
respectively.
Given the areas over which IDLH values are predicted to be exceeded, the
severity of consequences for this event is judged to be moderate to major, depending
on the meteorology at the tune of the spill.
d) Typical Spill of Acetone-Containing Waste
Off-site exceedances of IDLH values are not predicted under any set of
meteorological conditions. Thus, the severity of consequence is judged to be minor.
Volume VII . External Review Draft
VI-3 Do Not Cite or Quote
-------
2. On-Site Fire
For the cm-site fire scenario, two events are evaluated:
• A fire involving a spill of 20,000 gallons of waste containing 15 %
tetrachloroethene and 85 % toluene.
• A fire involving a spill of 200 gallons of waste containing 15 %
tetrachloroethene and 85 % toluene.
The results of these events are summarized in Table VI-6, and are discussed below.
a) Conservative Fire Event
In the conservative fire event, exceedances of the IDLH values for HC1 and
phosgene are not expected off-site under either typical or conservative meteorology.
Based on the ARCHIE model, an on-site fire involving the 20,000 gallon release
assumed for this scenario could potentially result hi a heat effect fatality zone radius
of 20 m, and an injury zone radius of 28 m. The fatality zone radius is defined as
the distance from the center of the pool within which individuals may suffer from
third-degree burns likely to be fatal. The injury zone radius is defined as the
distance from the center of the pool within which individuals may suffer from
second-degree burn injuries or severe pain on bare skin. Because inhabited areas
are at least 75 m from the fire location, neither fatalities nor injuries would be
expected off-site, although on-site impacts might occur.
The consequences of a fireball, which would be less likely to occur than a
simple fire, could be more significant. According to the ARCHIE model, the
fatality zone radius would be 365 m, or possibly extending nearly 300 m into
inhabited off-site areas. The injury zone radius would be 695 m, or possibly
extending to almost 625 m hi inhabited off-site areas.
On the basis of potential vapor emissions only, the severity of consequences for
the large on-site spill would be minor. When the heat effects are considered, the
severity of consequence would remain minor. However, the severity of consequence
in the unlikely event a fireball should form is classified as major.
The severity of consequence for this event does not change whether ignition
occurs during the release, or after the pool reaches its maximum size (see Appendix
VII-3 for details).
Volume VII External Review Draft
VI-4 Do Not Cite or Quote
-------
b) Typical Fire Event
In the typical fire event, off-site exceedances of IDLH values are not predicted
for either HC1 or phosgene under either typical or conservative meteorology.
For the on-site fire involving a 200 gallon spill, the fatality zone radius for heat
effects from a pool fire is 13 m, and the injury zone radius is 18 m, assuming that ,
the fire did not occur until the spill area reached its maximum size. If the waste
were to ignite upon discharge, both radii would be less. Thus, while on-site impacts
might occur, neither fatalities nor injuries are expected off-site.
For a fireball, the calculated fatality zone radius is about 30 m, and the
calculated injury zone radius is about 65 m. Given that the closest inhabited areas
are over 75 m from the on-site fire location, neither fatalities nor injuries would be
expected off-site. As discussed hi Chapter IV of this report, it is highly unlikely
that a fireball could occur, given the wastes expected to be received at the WTI
facility.
Based on the results, the severity of consequence for the typical on-site fire is
judged to be minor.
3. On-Site Mixing of Incompatible Wastes
Two on-site events involving mixing of incompatible wastes are evaluated:
• Mixing of a total of 10,000 gallons of incompatible wastes (by inadvertently
pumping 5,000 gallons of waste, at a rate of 250 gallons/mm, into a tank which
contains 5,000 gallons of an incompatible waste), resulting in the generation of
HC1 emissions.
• Mixing of a total of 200 gallons of incompatible wastes, resulting hi the
generation of HC1 emissions.
The results of these events are summarized hi Table VI-7, and are discussed below.
a) High Volume Mixing Event
In the Accident Analysis, HC1 emissions are calculated using a simple mass
balance, assuming that 100% of the chlorine hi the waste reacts instantaneously to
form HC1, and are likely to be significant overestimates. Based on this assumption,
in the mixing event involving 10,000 gallons of incompatible wastes, exceedances of
the IDLH for HC1 are predicted to occur to a distance of about 680 m downwind in
potentially inhabited areas under typical meteorological conditions, assuming no
Volume VII External Review Draft
VI-5 Do Not Cite or Quote
-------
active mitigation or emergency response. Under conservative and calm/inversion
meteorological conditions, exceedances were predicted to occur up to distances of
about 3,200 m and 4,600 m, respectively.
Based on the assumptions of this analysis, the severity of consequence for this
event is judged to be major to catastrophic, depending on the meteorological
conditions.
b) Typical Volume Mixing Event
In the typical volume mixing event involving 200 gallons of waste, no
exceedance of the IDLH is predicted under typical meteorology. Exceedances of the
IDLH for HC1 are predicted to occur up to approximately 270 m downwind in
potentially inhabited areas under conservative meteorological conditions. Under
calm/inversion meteorological conditions, exceedances of the IDLH are predicted for
off-site distances up to about 500 m.
Based on the areas over which potential exceedances of the IDLH are predicted,
the severity of consequence for this event is judged to be minor to major, depending
on the meteorology at the tune of the accident. As previously noted with respect to
the conservative mixing scenario, emissions of HC1 were estimated using a mass
balance approach, and are likely to be a significant overestimate.
4. Off-Site Spill
Four off-site spill events are evaluated:
• Conservative off-site spill of 5,000 gallons of liquid waste consisting of a 10%
formaldehyde/90% methanol mixture.
• Conservative off-site spill of 5,000 gallons of liquid waste consisting of a 10%
acetone/90% toluene mixture.
• Typical off-site spill of 100 gallons of liquid waste consisting of a 10%
formaldehyde/90% methanol mixture.
• Typical off-site spill of 100 gallons of liquid waste consisting of a 10%
acetone/90% toluene mixture.
The results of these events are summarized in Table VI-8, and are discussed below.
Volume VII External Review Draft
VI-6 Do Not Cite or Quote
-------
a) Conservative Spill of Formaldehyde-Containing Waste
Under the typical meteorological conditions, exceedances of the IDLH for
formaldehyde are predicted up to approximately 1,000 m downwind of the spill.
Exceedances of the IDLH are predicted up to about 5,100 m and 8,600 m downwind
under conservative and calm/inversion meteorological conditions, respectively.
Based on the large area over which the IDLH could potentially be exceeded,
and the magnitude of the exceedances of the IDLH value, the severity of
consequence of this event is judged to be major to catastrophic, depending on the
meteorological conditions.
b) Conservative Spill of Acetone-Containing Waste
In the event of a large spill of acetone-containing waste, IDLH values are
predicted to be exceeded only immediately adjacent to the spill under both typical
and conservative meteorological conditions. The IDLH could be exceeded up to
about 50 m downwind under calm/inversion conditions. On this basis, the severity
of consequence is judged to be minor to moderate depending on the meteorology at
the time of the spill.
c) Typical Spill of Formaldehyde-Containing Waste
Under typical meteorological conditions, potential exceedances of the IDLH for
formaldehyde are predicted to occur up to a distance of about 130 m from the spill.
Under conservative and calm/inversion meteorological conditions, exceedances are
predicted to occur up to distances of about 630 m, and 1,100 m respectively.
Based on the areas over which exceedance of the IDLH value are predicted, the
severity of consequence for this event is judged to be major to catastrophic,
depending on meteorological conditions.
d) Typical Spill of Acetone-Containing Waste
Exceedances of the IDLH for acetone are predicted to occur over a relatively
short distance (i.e., less than 10 m) under all meteorological conditions. Thus, the
severity of consequence for this event is judged to be minor.
5. Off-Site Fire
Two off-site fire events are evaluated:
Volume VII External Review Draft
VI-7 Do Not Cite or Quote
-------
• A fire involving a spill of 5,000 gallons of waste containing 15%
tetrachloroethene and 85% toluene, resulting in HC1 and phosgene emissions.
• A fire involving a spill of 100 gallons of waste containing 15 %
tetrachloroethene and 85% toluene, resulting in HC1 and phosgene emissions. .
The results of these events are summarized hi Table VI-9, and are discussed below.
a) Conservative Fire Scenario
In the off-site fire scenario, under typical meteorology, exceedances of the
IDLH are not predicted for either HC1 or phosgene. Under conservative
meteorology, exceedances of the IDLH are predicted to occur within distances of
275 m (for HC1) and 125 m (for phosgene). Any exceedances which occur would
be hi "pockets", with the site and location of these pockets dependent upon terrain
elevation hi the vicinity of the accident.
Based on the results of the ARCHIE model, the fatality zone radius for heat
effects would be 40 m, and the injury zone radius would be about 60 m, assuming
the fire did not occur until the spill area reached its maximum size. If the fire were
to start at the tune of the discharge, the fatality and injury zone radii would be
reduced to about 35 m and 50 m, respectively.
If a fireball were to form, the ARCHIE model predicts a fatality zone radius of
approximately 170 m, and an injury zone radius of about 340 m. As discussed hi
Chapter IV of this report, it is highly unlikely that a fireball would form given the
types of wastes transported to the WTI facility.
On the basis of potential HC1 and phosgene emissions, the large off-site
transportation spill is judged to have minor consequences under typical meteorology,
and potentially major consequences under conservative meteorology. Given the
potential heat effects of the fire, the event is assigned a severity of consequence
ranking of moderate, while the severity is ranked as major if it is assumed a fireball
can form.
b) Typical Fire Scenario
In the typical off-site fire scenario, exceedances of the IDLH values for HC1
and phosgene are not expected.
In the off-site fire scenario involving a 100 gallon spill, the fatality zone radius
for heat effects is 9 m, and the injury zone radius is 13 m, assuming the fire does
not occur until the spill area reached its maximum size. If the fire is assumed to
Volume VII External Review Draft
VI-8 Do Not Cite or Quote
-------
start during the discharge, the fatality and injury zone radii decrease to 5 m and 7
m, respectively.
If a fireball formation is assumed, the ARCHIE model predicts a fatality zone
radius of 20 m, and an injury zone radius of 45 m. However, a fireball is not likely
to form in a typical off-site fire scenario due to the small size of the spill leading to
the fire.
Given that no exceedances of IDLH values are expected, and the small area for
potential heat effects, the typical off-site fire event is categorized as moderate. The
event is classified as having moderate severity if a fireball is assumed to form.
B. Probability of Occurrence
1. On-Site Events
As discussed hi Chapter I, the probability of occurrence in an Accident Analysis can
be assessed qualitatively, semiquantitatively or quantitatively. In this Accident Analysis,
the probability has been assessed qualitatively, or semiquantitatively, depending on the
data available for the specific accident scenario. Furthermore, the probability rankings
that are assigned correspond to accident classes, rather than specific accident events.
This approach was adopted given die limited information available on the likelihood of
specific events, as discussed below.
As discussed in Chapter I, the U.S. EPA Summary of Incidents at Incinerators and
Commercial TSDFs Report on Emergency Incidents at Hazardous Waste Incinerators and
Commercial Treatment, Storage, and Disposal Facilities (TSDFs) (U.S. EPA 1995b)
provides information regarding incidents reported at hazardous waste facilities. A total
of 50 emergency incidents, as defined by U.S. EPA, were reported at the hazardous
waste incinerators identified in the study. For commercial hazardous waste incinerators
only, 24 emergency incidents at 11 facilities were reported, with 10 involving a release
of hazardous waste. No emergency incidents have been reported at 15 commercial
incineration facilities, so these facilities were not discussed hi U.S. EPA (1995b). In all,
26 commercial hazardous waste incineration facilities were identified to have operated in
the U.S. sometime during the period from 1981 through 1994.
The total operating tune for the 26 commercial incinerators during the tune period
considered by the study is approximately 250-300 years. This operating tune total is
conservative, since no information was available for operations before 1981, and no
operating dates were available for two facilities. Thus, approximately one emergency
incident involving a hazardous waste release has been reported for every 25 to 30 years
of operation for the commercial incinerators. None of the 10 incidents reported at .
Volume VII External Review Draft
Vl-9 Do Not Cite or Quote
-------
commercial combustion facilities involving releases of hazardous waste has resulted in a
fatality or serious injury hi off-site communities, although on-site worker injuries and
fatalities have been reported (U.S. EPA 1995b).
According to the U.S. EPA Chemical Emergency Preparedness and Prevention
Office (CEPPO), the Emergency Response Notification System (ERNS) database
includes first-hand reports of incidents. Further detailed information on selected
incidents from ERNS .is maintained hi the Accidental Release Inventory Program (ARIP)
database. However, neither the ERNS nor ARIP databases provide comprehensive
information on incidents at specific incinerators or other TSDFs (Chung 1995). Finally,
the RCRA Corrective Action database and the Bureau of Labor Statistics database do not
provide relevant information specific to incidents at hazardous waste TSDFs. In
summary, a rigorous quantitative analysis for hazardous waste-related accidents can not
be performed based solely on data from the operating history of commercial hazardous
waste incinerators or TSDFs.
The estimated probability of occurrence rankings for the various on-site accident
events are discussed separately below. These rankings do not explicitly take into
account WTI procedures and design features for preventing spills, leaks, fires, and
mixing of incompatible wastes, as discussed hi Chapter II and are thus considered
conservative. Furthermore, the probability of occurence rankings correspond to accident
classes rather than specific accident events. For example, the probability ranking for a
"typical" size spill of "typical" waste represents the ranking for spills on the order of
100 gallons involving wastes received by the WTI facility hi relatively high volumes.
a) On-Site Spill
As indicated by the summary of incidents reported at the WTI facility (hi
Table 3 of Appendix VII-1), it is reasonable to assume that small spills (i.e., less
than 20 gallons) are expected to be relatively common, using the definition of
FEMA (1993). According to FEMA (1993), accidents can be classified as common
if they are expected to occur one or more tunes per year on average; there have
been 5 spills of 20 gallons or less hi about 2 years of operation at the WTI facility.
There have been no spills greater than 20 gallons reported at WTI hi the past
two years. However, as documented hi Table 1 of Appendix VII-1, several spills of
100 gallons or more have been reported at TSDFs hi the U.S. since 1981. While
data for quantifying the frequency of larger (i.e., greater than 100 gallon) spills at
hazardous waste incinerators are not available, the available information summarized
hi Table 2 of Appendix VII-1 would suggest that spills of approximately 100 gallons
might be considered at most reasonably likely (i.e., expected to occur at least once
Volume VII External Review Draft
VI-10 Do Not Cite or Quote
-------
every 10 years on average), while spills of 5,000 gallons might be considered at
most reasonably likely (i.e., expected to occur between once every 10 years and
once every 100 years on average). These relative rankings are generally consistent
with available data on the distribution of spill sizes from full-size tankers during
highway transit between 1971 and 1986, which indicate that 70% of all spills were
20 gallons or more; 40% were 100 gallons or more, but only 5% were 5,000
gallons of more.(U.S. DOT 1986). Thus on-site spills of about 5,000 gallons are
estimated to be about 10-fold less likely to occur than on-site spills of about 100
gallons.
The likelihood of spills involving a "worst-case" chemical, such as
formaldehyde, is believed to be significantly lower than the likelihood of a spill
involving a "typical" chemical, such as acetone. For example, acetone represents
approximately 3 % of the total pumpable feeds based on waste profiles for the first
nine months of operation, while formaldehyde represents only about 0.5%. Thus,
the probability of occurrence for spills of "worst-case" chemicals are ranked lower
than for spills of "typical" chemicals.
Finally, it is less likely that spills will occur during conservative or
calm/inversion meteorological conditions than during typical meteorological
conditions. Conservative conditions, which reflect a stable atmosphere along with
low wind speeds (< 1 m/sec), would be expected to occur less than 10% of the
hours hi a year, according to the meteorological data discussed hi Chapter V. The
calm/inversion scenarios evaluated hi this analysis (a period of windspeed less than
1.0 m/sec, followed immediately by a period of stable atmosphere), would be
expected to occur less than 5 % of the hours hi a year. For example, based on the
one-year hourly surface meteorological data (April 1992 - March 1993) recorded at
the WTI site, a stable atmosphere (F-stability) with low wind speed (windspeeds
between 1.0 and 1.5 m/sec) would occur immediately after a calm hour only about
1.7% of the tune.
On the basis of the information provided above, the on-site spill scenarios have
been assigned the rankings for probability of occurrence shown hi Table VI-10.
b) On-site Fire
Data on the frequency of fires at hazardous waste incineration facilities and
other TSDFs are very limited. Relatively few fires have been reported since 1981,
when reporting under RCRA began. Thus, there is considerable uncertainty hi
estimating the likelihood of occurrence for an on-site fire.
Volume VII External Review Draft
VI-11 Do Not Cite or Quote
-------
The frequency of ignition hi the event of a spill depends on a number of factors,
including the flammability of the waste, the proximity of an ignition source, and the
atmospheric conditions. However, based on data from oil refinery operations,
Battelle (1987) estimated an ignition frequency of one in every 25 spills. On this
basis and the likelihood rankings assigned to the on-site spills, the probability of
occurrence rankings assigned for the on-site fire scenarios are listed in Table VI-10.
The rankings do not take into account the probability of chlorinated wastes being
involved hi the fire, and thus may overstimate the likelihood of adverse
consequences.
c) On-Site Mixing of Incompatible Wastes
Data on the frequency of incidents involving the mixing of incompatible wastes
at hazardous waste incineration facilities and other TSDFs are very limited. As
shown hi Table 2 of Appendix VII-1, very few such incidents have been reported at
other TSDFs since 1981. However, based on the Report on Emergency Incidents at
Hazardous Waste Incinerators and Commercial Treatment, Storage, and Disposal
Facilities (TSDFs) (U.S. EPA 1995b), it does not appear that incidents involving
mixing of incompatible wastes are any more likely than fires. Thus, the rankings
assumed for on-site fires are also assigned for mixing of incompatible wastes, as
shown on Table VI-7. Given the lack of frequency data for events involving mixing
of incompatible wastes, there is considerable uncertainty associated with these
rankings.
2. Off-Site Events
a) Off-She Spill Events
Site-specific calculations used to calculate the off-site accident and spill
frequency of trucks carrying waste to WTI are described hi Appendix VII-5. Spills
may occur during waste transport as a result of both major accidents and minor
valve and fitting leaks. Based on an evaluation of site-specific traffic accident data,
a collision-related spill involving trucks bringing waste to the WTI facility is
estimated to have about a 1 hi 60 chance of occurring each year on State Route 39
(SR 39) hi East Liverpool, Ohio. Non-collision related spills are estimated to have
about a 1 hi 40 chance of occuring each year on the same route. Considering both
collision and non-collision related releases and based on data regarding spill size, a
spill of greater than 100 gallons is estimated to have a 1 hi 60 chance of occurring
Volume VII External Review Draft
VI-12 Do Not Cite or Quote
-------
^ each year. A spill of greater than 5,000 gallons is estimated to have a 1 in 295
{ chance of occurring each year.
\_^ _.-
An estimate of the likelihood of a spill occurring during transport of waste to
the WTI facility can also be roughly approximated using national data for 1991, the
most recent year for which data on the total quantity of hazardous waste shipped in
the U.S. are available (U.S. EPA 1994b). Based on U.S. EPA (1994b), there were
approximately 15 million tons of hazardous waste transported within the United
States in 1991. During that same year, there were 175 highway-related incidents
involving hazardous waste, with an average spill size of 92 gallons (U.S. DOT
1995). Thus, there was approximately one incident per every 75,000 tons of
hazardous waste transported on the highway.
According to the RCRA permit for the WTI incinerator (U.S. EPA 1983), up to
approximately 75,000 tons of waste is allowed to be incinerated at the WTI facility
each year. Thus, one transportation-related incident might be expected during each
year of operation at the WTI facility over the entire transportation network for the
facility. However, only 25 injuries were reported to result from the 175 highway-
related incidents in 1991, or about one injury for every 7 incidents (U.S. DOT
^ ^ 1995). All injuries and fatalities listed in U.S. DOT (1995) were the result of
chemical exposure (Duyzh 1995). Thus, there is approximately a 1 in 7 chance that
v exposure-related injury might occur each year over the generator to WTI
transportation route (the likelihood of an injury along the local access route in East
Liverpool only would be considerably lower).
Finally, during the 10 years between 1984 and 1993, there were one fatality and
143 injuries reported involving highway transport of hazardous waste (U.S. DOT
1995). For highway transport of hazardous materials, there were 115 fatalities and
2,781 injuries. Thus, it can be estimated that there are between 1 fatality for every
25 injuries (using the hazardous materials data) and 1 fatality for every 140 injuries
(using the hazardous waste data). Based on the 1 hi 7 probability for an injury each
year along the WTI transportation route, there would be between 1 chance in 175
and 1 chance in 980 each year of an exposure-related fatality along the overall
generator to WTI transportation route. Again, the likelihood of a fatality along the
local access route in East Liverpool only would be lower.
Considering the U.S. DOT and U.S. EPA data summarized above, the
likelihood of occurrence rankings are assigned to the off-site spill events, based on
the general guidance provided in U.S. EPA (1987) and FEMA (1993). These
_••-•" —-x
rankings are shown in Table VI-11, and correspond to the liklihood of a spill along
the local access route hi East Liverpool.
Volume VII External Review Draft
VI-13 Do Not Cite or Quote
-------
b) Off-Site Fire Events
As previously discussed, there is considerable uncertainty in estimating the
probability of a fire resulting from a spill. The likelihood of a fire depends on the
nature of the waste spilled, and the proximity of an ignition source, among other
factors. Based on data from oil refinery operations, Battelle (1987) estimated a fire
frequency of one in every 25 spills. According to data cited in FEMA (1993), about
1 % of most types of truck accidents result hi a fire; this corresponds to-a fire
frequency of about one in every 20 to 50 spills.
Considering the estimated likelihood of an off-site spill, and the reduced
likelihood of a spill leading to a fire, the likelihood of occurrence rankings are
assigned to the off-site fire events and listed in Table VI-11.
C. Summary of Results and Key Assumptions
The severity of consequence and probability of occurrence results for on-site accident
scenarios are summarized hi Table VI-12. As shown hi Table VI-12, only on-site events
with "minor" off-site consequences are judged "likely" to occur at the WTI facility, and only
on-site events with "minor" or "moderate" off-site consequences are judged to be "reasonably
likely" to occur. All on-site accident scenarios with "major" off-site consequences are
judged "unlikely" to occur. All on-site accident scenarios with "catastrophic" off-site
consequences are judged "very unlikely" to occur.
The results of the Accident Analysis described hi this report are consistent with the
results of the Credible Event Analysis performed by S.E. Technologies (1992) for WTI. The
results of the Credible Event Analysis (SE Technologies 1992) are not directly comparable to
the results of this Accident Analysis, because the Credible Event Analysis compared
downwind distances to U.S. EPA Level of Concern (LOG) values, rather than IDLH values.
However, the results of one type of accident, mixing of incompatible wastes, can be
compared. In both the Credible Event Analysis and the current Accident Analysis, the
mixing of incompatible waste scenario resulted in the potential for significant off-site
exposures. In the Credible Event Analysis, a "hazard distance" (i.e., distance over which an
LOG would be exceeded) was calculated to be approximately 7,000 m for the mixing of
incompatible waste scenario. As shown on Table VI-7 hi this Accident Analysis, the
downwind distance over which an IDLH is predicted to be exceeded for a comparable mixing
of incompatible waste scenario ranges from 680 m to 4,620 m, depending on meteorology.
(As discussed hi Chapter VII, the downwind distance over which an LOG is predicted to be
exceeded for this scenario ranges form 1,280 m to 12,200 m, depending on meteorology).
Consistent with this Accident Analysis, the Credible Event Analysis determined that the
probability of occurrence for this type of accident is low. The results of the Credible Event
Volume VII External Review Draft
VI-14 Do Not Cite or Quote
-------
Analysis and this Accident Analysis for the other types of on-site events (i.e., spills and fires)
are also comparable, with "hazard distances" potentially extending several hundred meters
downwind due to spills, and potential heat effects off-site due to major fires. However, this
Accident Analysis examined several scenarios involving large spills of very toxic, volatile
waste not considered in the Credible Event Analysis, and thus has projected greater possible
consequences associated with spill events.
The severity of consequence and probability of occurrence results for off-site accident
scenarios are summarized in Table VI-13. For the off-site accident scenarios, events with
minor consequences were determined to be at most, reasonably likely to occur. Off-site
accidents with moderate or major consequences are judged to be unlikely or very unlikely to
occur. Events classified as having potentially catastrophic consequences were determined to
be very unlikely to occur. The Credible Event Analysis performed by S.E. Technologies
(1992) for WTI did not assess off-site accidents.
Major assumptions made in ranking the accident events according to severity of
consequence and likelihood of occurrence are listed in Table VI-14.
Volume VII . External Review Draft
VI-15 Do Not Cite or Quote
-------
TABLE VI-1
Criteria Used in Ranking the Severity of Consequence
Severity of
Consequence Ranking
General Criteria
Minor
No exceedance of an IDLH value in inhabited off-site areas; and
negligible potential for off-site fatalities or serious injuries due to
heat effects from a fire.
Moderate
Exceedance of IDLH values hi inhabited off-site areas over
distances of 100 m or less; injuries due to heat effects limited to a
distance of 100 m into inhabited areas.
Major
Exceedance of IDLH values hi inhabited off-site areas over
distances between 100 m to 1000 m; injuries due to heat effects
limited to a distance of 1000 m into inhabited areas.
Catastrophic
Exceedance of IDLH values hi inhabited off-site areas over
distances greater than 1000 m; injuries due to heat effects extend
to distances greater than 1000 m into inhabited areas.
Volume VII
VI-16
External Review Draft
Do Not Cite or Quote
-------
TABLE VI-2
Criteria Used in Ranking Probability of Occurrence
Probability of Occurrence
Ranking
Common
Likely
Reasonably Likely
Unlikely
Very Unlikely
General Criteria
Expected to occur one or more times each year on average.
Expected to occur at least once every 10 years on average
according to available statistics.
Predicted to occur between once every 10 years and once
every 100 years on average.
Predicted to occur between once every 100 years and once
every 1,000 years on average in a specific locale.
Predicted to occur less than once in 1,000 years.
Volume VII
VI-17
External Review Draft
Do Not Cite or Quote
-------
TABLE VI-3
Severity of Consequence for On-Site Scenarios
Meteorological Conditions
Typical
Conservative
On-Site Spills
5,000 gallon spill
Formaldehyde
Acetone
100 gallon spill
Formaldehyde
Acetone
Major
Minor
Moderate
Minor
Catastrophic
Minor
Major
Minor
On-Site Fires
20,000 gallons of waste
200 gallons of waste
Minor1
Minor2
Minor1
Minor2
Calm/Inversion
Catastrophic
Minor
Major
Minor
NE3
NE3
Mixing of Incompatible Wastes
10,000 gallons of waste
200 gallons of waste
Major
Minor
Catastrophic
Major
Catastrophic
Major
Notes:
1 On the bases of potential HC1 and phosgene emissions and heat effects, the
conservative fire is judged to have minor consequences. If a fireball were to form, the
consequences would be classified as major, but the probability of occurrence is very
unlikely.
2 On the bases of potential HC1 and phosgene emissions, heat effects and assumed
fireball formation, the typical fire is judged to have minor consequences.
3 NE: Not evaluated. Calm/inversion conditions not evaluated for the fire scenarios.
Volume VII
VI-18
External Review Draft
Do Not Cite or Quote
-------
TABLE VI-4
Severity of Consequence for Off-Site Scenarios
Meteorological Conditions
Typical
Conservative
Off-Site Spills
5,000 gallon spill
- Formaldehyde
- Acetone
100 gallon spill
- Formaldehyde
- Acetone
Major
Minor
Major
Minor
Catastrophic
Moderate
Catastrophic
Minor
Calm/Inversion
Catastrophic
Moderate
Catastrophic
Minor
Off-Site Fires
5,000 gallons of waste
100 gallons of waste
Moderate1
Moderate2
Major1
Moderate2
NE3
NE3
Notes:
1 On the bases of potential HCI and phosgene emissions, the conservative fire is judged
to have minor consequences under typical meteorology, and potentially major
consequences under conservative meteorology. Given the potential heat effects of the
fire, the event would be judged to have moderate consequences. If a fireball were to
form, the consequences would be classified as major, but the probability of
occurrence is very unlikely.
2 On the bases of potential HCI and phosgene emissionsand heat effects the typical fire
is judged to have moderate consequences.
3 NE: Not evaluated. Calm/inversion conditions not evaluated for the fire scenarios.
Volume VII
VI-19
External Review Draft
Do Not Cite or Quote
-------
TABLE VI-5
Consequence Assessment, On-Site Spill
Spill Size
(gallons)
5,000
5,000
5,000
5,000
5,000
5,000
100
100
100
100
100
100
Meteorology
Typical
Conservative
Calm/Inversion
Typical
Conservative
Calm/Inversion
Typical
Conservative
Calm/Inversion
Typical
Conservative
Calm/Inversion
Contaminant
Formaldehyde
Formaldehyde
Formaldehyde
Acetone
Acetone
Acetone
Formaldehyde
Formaldehyde
Formaldehyde
Acetone
Acetone
Acetone
Max. Downwind Dist. to IDLH,
no active mitigation1-1 (m)
640
4800
8450
—
—
—
40
550
1000
..
—
-
Notes:
1 Maximum Downwind Distance calculated from the property line to the east or west, or the existing railroad to the north, whichever is closer to the
location of the release. For the on-site spill, maximum downwind distance was calculated from the railroad line to the north, approximately 75 m from
the edge of the spill.
2 — : IDLH not exceeded in potential off-site receptor areas.
Volume VII
External Review Draft
Do Not Cite o \
-------
TABLE VI-6
Consequence Assessment, On-Site Fire
Waste Volume
Ignited (gallons)
20,000
20,000
200
200
Meteorology
Typical
Conservative
Typical
Conservative
Contaminant
HC1
Phosgene
HC1
Phosgene
HC1
Phosgene
HC1
Phosgene
Downwind Dist. to IDLH,
no active mitigation1 (m)
—
—
-
-
..
—
—
--
Max. Downwind
Dist. Affected by
Heat Effect (m)1
Fatality
--
Injury
-
~
~
Max. Downwind Dist. Affected
by Fireball(m)1
Fatality
300
300
-
-
Injury
625
625
--
--
Note:
1 --: not exceeded in potential off-site receptor areas.
Volume VII
VI-21
External Review Draft
Do Not Cite or Quote
-------
TABLE VI-7
Consequence Assessment, On-Site Mixing of Incompatible Wastes
Waste Volume
(gallons)
10,000
10,000
10,000
200
200
200
Meteorology
Typical
Conservative
Calm/Inversion
Typical
Conservative
Calm/Inversion
Contaminant
HC1
HC1
HC1
HC1
HC1
HC1
Max. Downwind Dist. to IDLH,
no active mitigation1'2 (m)
680
3190
4620
—
270
520
Notes:
1 Maximum Downwind Distance calculated from the property line to the east or west, or the existing railroad to the north, whichever is closer to the
release. For the on-site mixing of incompatible wastes, the maximum downwind distance was calculated from the railroad line to the north, or
approximately 75 m from the edge of the release.
2 -: IDLH not exceeded in potential off-site receptor areas.
Vo'-^e VII
External Review Draft
Do Not Cite \te
J
-------
TABLE VI-8
Consequence Assessment, Off-Site Spill
SpiU Size
(gallons)
5,000
5,000
5,000
5,000
5,000
5,000
100
100
100
100
100
100
Meteorology
Typical
Conservative
Calm/Inversion
Typical
Conservative
Calm/Inversion
Typical
Conservative
Calm/Inversion
Typical
Conservative
Calm/Inversion
Contaminant
Formaldehyde
Formaldehyde
Formaldehyde
Acetone
Acetone
Acetone
Formaldehyde
Formaldehyde
Formaldehyde
Acetone
Acetone
Acetone
Max. Downwind Dist. to IDLH,
no active mitigation1'1 (m)
. 980
5120
8550
< 10
< 10
50
130
630
1080
< 10
< 10
< 10
Notes:
1 Maximum Downwind Distance calculated from edge of spill.
2 — : IDLH not exceeded in off-site potential receptor areas.
Volume VII
VI-23
External Review Draft
Do Not Cite or Quote
-------
TABLE VI-9
Consequence Assessment, Off-Site Fire
Waste Volume Ignited
(gallons)
5,000
5,000
100
100
Meteorology
Typical
Conservative
Typical
Conservative
Contaminant
HCI
Phosgene
HCI
Phosgene
HG1
Phosgene
HCI
Phosgene
Downwind Dist. to IDLH1 2
no active mitigation
—
-
2753
1253
—
-
--
-
Max. Downwind Dist.
Affected by Heat Effect
(m)1
Fatality
35
40
5
9
Injury
50
60
7
13
Max. Downwind Dist.
Affected by
Fireball(m)1
Fatality
170
170
20
20
Injury
340
340
45
45
Notes:
1 For the off-site fire scenarios, IDLH values for HCI and phosgene are predicted to occur in areas within approximately 275 m and 125 m, respectively,
downwind from the center of the fire under conservative meteorological conditions. The areas of exceedance within this zone are expected to be
"pockets" corresponding to locations of elevated terrain.
2 -: Not exceeded in potential receptors areas.
Volume VII
External Review Draft
Do Not Cite te
-------
TABLE VI-10
Probability of Occurrence for On-Site Scenarios
Meteorological Conditions
Typical
On-Site Spills
5,000 gallon spill
Formaldehyde
Acetone
100 gallon spill
Formaldehyde
Acetone
Unlikely
Reasonably Likely
Reasonably Likely
Likely
Conservative
Calm/Inversion
Very Unlikely
Unlikely
Unlikely
Reasonably Likely
Very Unlikely
Unlikely
Unlikely
Reasonably Likely
On-Site Fires
20,000 gallons of waste
200 gallons of waste
Unlikely
Reasonably Likely
Very Unlikely
Unlikely
Very Unlikely
Unlikely
Mixing of Incompatible Wastes
10,000 gallons of waste
200 gallons of waste
Unlikely
Reasonably Likely
Very Unlikely
Unlikely
Very Unlikely
Unlikely
Volume VII
VI-25
External Review Draft
Do Not Cite or Quote
-------
TABLE VI-11
Probability of Occurrence for Off-Site Scenarios
Meteorological Conditions
Typical
Off-Site Spills
5,000 gallon spill
Formaldehyde
Acetone
100 gallon spill
Formaldehyde
Acetone
Very Unlikely
Unlikely
Unlikely
Reasonably Likely
Conservative
Calm/Inversion
Very Unlikely
Very Unlikely
Very Unlikely
Unlikely
Very Unlikely
Very Unlikely
Very Unlikely
Likely
Off-Site Fires
5,000 gallons of waste
100 gallons of waste
Very Unlikely
Unlikely
Very Unlikely
Very Unlikely
Very Unlikely
Very Unlikely
Volume VII
Vl-26
External Review Draft
Do Not Cite or Quote
-------
TABLE VI-12
Severity of Consequence and Probability of Occurrence Results for On-Site Scenarios
Scenario
On-Site Spill
• 5,000 gallon spill
Formaldehyde Waste
Acetone Waste
• 100 gallon spill
Formaldehyde Waste
Acetone Waste
On-Site Fire
• 20,000 gallon waste
• 200 gallon waste
Mixing of Incompatible Wastes
• 10,000 gallon
• 200 gallon
Meteorological Conditions
Typical
Severity of
Consequence
Major
Minor
Moderate
Minor
Minor'
Minor2
Major
Minor
Probability of
Occurrence
Unlikely
Reasonably Likely
Reasonably Likely
Likely
Unlikely
Reasonably Likely
Unlikely
Reasonably Likely
Conservative
Severity of
Consequence
Catastrophic
Minor
Major
Minor
Minor1
Minor2
Catastrophic
Major
Probability of
Occurrence
Very Unlikely
Unlikely
Unlikely
Reasonably Likely
Very Unlikely
Unlikely
Very Unlikely
Unlikely
Calm/Inversion
Severity of
Consequence
Catastrophic
Minor
Major
Minor
NEJ
NEJ
Catastrophic
Major
Probability of
Occurrence
Very Unlikely
Unlikely
Unlikely
Reasonably Likely
Very Unlikely
Unlikely
Very Unlikely
Unlikely
Notes: .
1 On the bases of potential HCI and phosgene emissions and heat effects, the conservative fire is judged to have minor coasequences. If a fireball were to form, the
consequences would be classified as major, but the probability of occurrence is very unlikely.
2 On the bases of potential HCI and phosgene emissions, heat effects and assumed fireball formation, the typical fire is judged to have minor consequences.
3 NE: Not Evaluated.
Volume VII
VI-27
External Review Draft
Do Not Cite or Quote
-------
TABLE VI-13
Severity of Consequence and Probability of Occurrence Results for Off-Site Scenarios
Scenario
Off-Site Spill
• 5,000 gallon spill
Formaldehyde
Acetone
• 100 gallon spill
Formaldehyde
Acetone
Off-Site Fire
• 5,000 gallon waste
• 100 gallon waste
Meteorological Conditions
Typical
Severity of
Consequence
Major
Minor
Major
Minor
Moderate1
Moderate2
Probability of
Occurrence
Very Unlikely
Unlikely
Unlikely
Reasonably Likely
Very Unlikely
Unlikely
Conservative
Severity of
Consequence
Catastrophic
Moderate
Catastrophic
Minor
Major1
Moderate2
Probability of
Occurrence
Very Unlikely
Very Unlikely
Very Unlikely
Unlikely
Very Unlikely
Very Unlikely
Calm/Inversion
Severity of
Consequence
Catastrophic
Moderate
Catastrophic
Minor
NE3
NE3
Probability of
Occurrence
Very Unlikely
Very Unlikely
Very Unlikely
Unlikely
Very Unlikely
Very Unlikely
Notes:
1 On the bases of potential HCI and phosgene emissions, the conservative fire is judged to have minor consequences under typical meteorology and potentially major
consequences under conservative meteorology. Given the potential heat effects of the fire, the event would be judged to have moderate consequences. If a fireball were to
form, the consequences would be classified as major, but the probability of occurrence is very unlikely.
2 On the bases of potential HCI and phosgene emissions and heat effects, the typical fire is judged to have moderate consequences.
3 NE: Not Evaluated.
Volume VII
External Review Draft
Do F \e or Quote
-------
TABLE VI-14
Key Assumptions Made in
Ranking of Accident Events
Assumption
1 . Concentrations predicted by modeling
averaged over a 30-minute duration for
comparison to IDLH values.
2. IDLH values can be used as a
benchmark to evaluate extent of possible
off-site health effects.
3. Wind is continuously blowing toward the
nearest off-site inhabited area during the
entire duration of emissions.
4. A fireball forms in the event of a fire.
5. Likelihood of occurrence can be
estimated based on historical data from
TSDFs, and from USDOT and ODPS
highway accident data.
6. The largest volume of a storage
tank/container is used in the fireball
scenario.
7. Population data from 1990 census and
estimated plume width used to develop
consequence criteria relating IDLH to
potential for injuries and fatalities.
Basis
IDLH based on a 30-minute exposure.
IDLH values represent a consistent, relatively
comprehensive set of acute toxicity criteria.
Simplifying assumption.
Simplifying assumption.
Historical data believed to be relevant to the
WTI facility.
Simplifying assumption.
Number of people potentially impacted is based
on population density, size of plume, and
chemical concentration in plume relative to
lexicological criteria.
Magnitude of Effect
Medium
High
High
Medium
Low
Medium
Medium
Direction of Effect
May underestimate.
Individuals may be exposed
to higher peak concentrations
over short periods of time.
Unknown. May over or
underestimate size of area
over which effects may be
observed, depending on
derivation of IDLH value.
Overestimates
Overestimates hazard; a
fireball may form only under
specific circumstances.
Variable. May over or
underestimate actual accident
frequencies, especially for
low probability events.
Overestimates the quantity
available for forming a
fireball.
Approach used is likely to
overestimate severity of
consequence, using FEMA
(1993) guidance.
Volume VII
VI-29
External Review Draft
Do Not Cite or Quote
-------
VII. UNCERTAINTIES
As emphasized in the U.S. EPA's exposure assessment guidelines (U.S. EPA 1992c),
identification and quantification of uncertainties is an important element of the risk
assessment process. The primary sources of uncertainty in a risk assessment are associated
with both the toxicity evaluation of chemicals of concern and die exposure assessment.
These two sources of uncertainty are discussed separately below.
A. Toxicity Evaluation
It is widely recognized that there is significant uncertainty associated with current
assessments of die toxicity of various chemicals. Sources of uncertainty hi current toxicity
assessments for various chemicals may include inadequate toxicological data, extrapolation
from animals to humans, and a lack of knowledge regarding potential interactions among
various chemicals. The regulatory approach to dealing with these sources of uncertainty is to
use conservative techniques in deriving dose-response parameters. Because U.S. EPA relies
primarily upon the same data base (IRIS) for all its risk assessments, uncertainty in the dose-
response assessment is common to any risk assessment that uses toxicity data. More
sophisticated analyses of these uncertainties have not been included in the Accident Analysis
and the comparative rankings.
In the Accident Analysis, NIOSH IDLH values are used to evaluate the downwind
distance over which adverse human health effects might be anticipated hi die event of an
accident. IDLH values were originally developed by NIOSH to be protective of healthy
adult male workers. To determine die effect of using a more stringent measure of potential
healdi effects, a quantitative sensitivity analysis is conducted widi U.S. EPA LOG values.
This sensitivity analysis is described hi Section C of this chapter.
B. Exposure Assessment
The sources and magnitude of die uncertainties associated with exposure assessment may
vary greatly from one risk assessment to another. These uncertainties are largely determined
by die media, chemicals, populations, padiways, data, and models involved hi die
assessment. The U.S. EPA Exposure Assessment Guidelines (U.S. EPA 1992c) identify
diree types of uncertainty typically associated widi an exposure assessment: (1) scenario
Volume VII External Review Draft
VII-1 Do Not Cite or Quote
-------
uncertainty, (2) parameter uncertainty, and (3) model uncertainty. These types of uncertainty
are discussed in the context of the Accident Analysis hi the following sections.
1. Scenario Uncertainty
Scenario uncertainty is the term used for uncertainty arising from the absence of
information needed to fully define the exposure and dose. Sources of scenario
uncertainty include errors hi descriptive information; inaccurate professional judgment;
and incomplete analysis (e.g., failure to consider all exposed sub-groups and significant
routes of exposure).
Scenarios hi the Accident Analysis are selected for quantitative evaluation to provide
a range of credible accident events. More extreme events, with potentially greater off-
site consequences, but significantly lower probabilities of occurrence, are also
theoretically possible. Such extreme events might include an on-site spill of 10,000
gallons of volatile waste hi an unbermed area, resulting from a collision of two full
tankers, leading to high volatile emissions. If these tank trucks hi the scenario above
carried incompatible wastes, or the wastes were highly flammable, potential adverse
consequences could be further exacerbated. Under such scenarios, IDLH values could
be exceeded over very large off-site distances (e.g., > 10,000 m). However, die
likelihood of occurrence is judged to be extremely small, given the very low probability
of two trucks colliding on-site, the low probability of the entire contents of both trucks
being released, and the presence of berms and drams hi most paved areas where a large
pool could otherwise form.
Another major source of uncertainty is the incomplete information on waste
composition. Assumptions regarding the waste composition are critical in defining both
the nature and magnitude of accidental emissions. While die availability of data on
waste composition during the first year of operations at the WTI facility reduces this
uncertainty, some amount of scenario uncertainty is unavoidable because waste
composition may change over tune.
A third major source of scenario uncertainty is die limited information available for
predicting emissions resulting from fires or the mixing of incompatible wastes. Under
these scenarios, substances are created as a result of chemical reactions involving
constituents hi waste. The type and extent of these reactions is difficult to predict, and
there are also little relevant empirical data. For example, literally dozens of chemical
reactions could hypothetically occur during an open fire involving a complex waste
mixture, and data gaps exist regarding the initial composition of the waste mixture, the
reactions which may occur between die constituents and die emission rates for toxic
substances which are produced by the combustion process. To offset such data gaps,
Volume VII External Review Draft
VII-2 Do Not Cite or Quote
-------
x x conservative assumptions are made regarding the composition of the wastes involved in
( the accidents, and the rate of generation of toxic by-products. For example, a mass
balance approach is used to predict HC1 emissions due to mixing of incompatible wastes.
2. Parameter Uncertainty
The U.S. EPA Exposure Assessment Guidelines (U.S. EPA 1992c) indicate that
parameter uncertainty may arise from measurement errors, sampling errors, variability,
and the use of generic or surrogate data. Parameters that are subject to uncertainty
include those used to estimate emission rates (e.g., spill pool size and temperature) and
chemical concentrations hi the media and locations of interest (e.g., wind speed and
other meteorological conditions).
Unlike uncertainty associated with scenario development, there are methods
available to quantify the magnitude and effect of uncertainty in a parameter value, such
as spill size. Sensitivity analysis is included in the Accident Analysis to examine the
effects of certain types of parameter uncertainty by developing both conservative and
typical accident scenarios, and evaluating the effect of a variety of meteorological
conditions. For example, in the on-site spill scenario, two different spill volumes are
evaluated. For each spill volume, two different chemicals (one higher hazard, one lower
( hazard), are assessed, each under three different sets of meteorological conditions
(typical, conservative and calm/inversion). Finally, each combination of spill volume,
chemical composition and meteorological condition is evaluated with and without
mitigation, resulting hi a total of 24 conditions being quantitatively analyzed for the on-
site spill scenario.
Meteorological uncertainty is partially offset by examining typical, conservative,
and calm/inversion weather conditions, and assuming that the wind is blowing
continuously in the direction of the nearest inhabited off-site area. The actual downwind
distance impacted by the potential release could be significantly less than that predicted
for the calm/inversion or conservative meteorological conditions, depending on the
conditions at the tune of release. Other parameters such as humidity, height of the
release, and ground terrain features introduce additional uncertainty in the results.
Another potential source of parameter uncertainty is the need for physical/chemical
data for the substances of concern. Data on vapor pressure, molecular weight, boiling
point, density, and other properties are needed to model chemical emission rates. While
the uncertainty associated with some of these parameters is negligible (e.g., molecular
weight), it can be significant for other parameters (e.g., vapor pressure) for certain
chemicals. Where such uncertainty is potentially significant, specific property values are
Volume VII External Review Draft
VII-3 Do Not Cite or Quote
-------
selected to overestimate, rather than underestimate, off-site chemical concentrations in
air.
3. Model Uncertainty
Several models are used in the Accident Analysis to predict chemical releases and
subsequent atmospheric dispersion. Models required to predict release rates include the
following:
• Approaches to predict the physical/chemical properties of a waste mixture based
on the properties of the pure components.
• Models to predict liquid release rates from trucks.
• Models to predict chemical evaporation rates from spills.
• Methods to predict the rate of generation of toxic gases as the result of mixing
two incompatible wastes.
• Methods to predict the flame temperature and vapor cloud buoyancy in the event
of a waste fire.
• Methods to predict the heat flux at various distances from a waste fire.
It is not feasible to quantify the extent of uncertainty inherent in each of these modeling
techniques. Thus, the modeling is generally implemented using assumptions expected to
result in an overestimate, rather than an underestimate, of chemical releases.
Many models have been developed to simulate the dispersion of short-term
accidental chemical releases. Each model has its own unique advantages and
disadvantages. In the Accident Analysis, two dispersion models (SLAB and ISC-
COMPDEP) are used, matching the appropriate model to the emission release condition.
However, significant uncertainties exist in the application of these models, particularly
given the complex topography in the immediate vicinity of the facility. Conservative
assumptions are generally made in applying these models to avoid underestimating
potential off-site consequences.
Volume VII External Review Draft
VTI-4 Do Not Cite or Quote
-------
C. Sensitivity Analyses
In order to evaluate the sensitivity of the results described in Chapter VI, a further
assessment is performed to examine the following specific issues:
• The effect of active mitigation measures on severity of consequence. The effects of
terminating releases through active mitigation are assessed. Two active mitigation
tune frames, 10 minutes and 60 minutes, are evaluated for the on-site accident
scenarios. In addition, the effect of an unconfined (i.e., no benns) on-site spill is
evaluated to assess the highly unlikely failure of passive mitigation measures. Off-
site scenarios are not included in the sensitivity analysis because active mitigation
would likely take longer to occur.
• The effect of averaging tune hi comparing downwind concentrations to IDLH
values. In the Accident Analysis, downwind concentrations in ah" are averaged over
a 30 minute period, and then compared to IDLH values developed by NIOSH based
on a 30-minute exposure. For scenarios with maximum emission durations shorter
than 30 minutes, the maximum exposure may be considerably higher than the 30-
minute average exposure. The effect of averaging downwind concentrations over a
30-minute period is examined in the sensitivity analysis by comparing unaveraged
maximum exposure concentrations directly with the IDLH values.
• The effect of using LOCs rather than IDLHs to determine the extent of the
potentially impacted area. Modeled off-site concentrations are compared to LOG
values to evaluate the sensitivity of the conclusions with respect to the selection of
acute health effects criteria.
Each of these issues is addressed separately below.
1. Effect of Mitigation Measures
In evaluating the effect of active mitigation, two tune periods (10 minutes and
60 minutes) were assessed. Ten minutes is believed to be a conservative estimate of the
tune it might take for automatic active mitigation procedures which are already in place
to halt emissions to air (e.g., foam or water deluge for fire suppression), or for a small
spill to be remediated. The tune period for other active mitigation measures to be
effective in stopping emissions could be longer in the event of a conservative spill or fire
situation, or hi the event that automatic active mitigation devices are not readily available
Volume VII External Review Draft
VII-5 Do Not Cite or Quote
-------
or fail. In these situations, sixty minutes or more may be required to effectively stop
emissions.
In the WTI Emergency Plan Exercise (Von Roll 1993), a scenario was evaluated
involving two accidents which occur in sequence. The first accident is the shearing of
the cap and stem of a valve from the side of a tanker truck, resulting in a leak of
hazardous waste. In this exercise, it was estimated to take 10 minutes for the
appropriate personnel to reach the scene, and approximately an additional hour for the
situation to be assessed, the potential immediate off-site impact to be determined, the
leak to be stopped and the spill to be cleaned up.
The second accident involves a second truck colliding with the first truck, resulting
in the mixture of the (incompatible) contents of the two tankers. In.this hypothetical
incident, two people have been injured. Therefore, the first twenty minutes are spent
removing the individuals from the accident area and assessing the situation. The leak of
materials is stopped after an additional 40 minutes.
In each of these accident scenarios, it appears that active mitigation measures and
emergency response can limit the release of chemicals to approximately one hour.
Because of the tune required to notify the appropriate personnel and assess the situation
before proceeding, it is unlikely that a conservative release could be terminated within
10 minutes. In these two scenarios, 10 to 20 minutes have passed before any active
response designed to terminate emissions is initiated. Therefore, a mitigation time
period of 60 minutes is also considered in this sensitivity analysis.
In the Accident Analysis, it was assumed that passive mitigation (e.g., berms, drains
and dikes) would be hi place and effective for on-site scenarios. The likelihood of a
simultaneous accident and failure of the passive mitigation system is very small.
However, the impact of the failure of passive systems is illustrated through an evaluation
of the on-site spill in this sensitivity analysis.
a. On-Site Spills
Active Mitigation
As shown in Table VI-5, assuming no active mitigation of a 5,000 gallon on-site
spill of "worst-case" waste, exceedances of the IDLH for formaldehyde extend to
approximately 8,500 m, 4,800 m and 640 m, under calm/inversion, conservative and
typical meteorological conditions, respectively. If it is assumed that mitigation and
emergency response limit emissions to a duration of 10 minutes, exceedances of the
IDLH for formaldehyde are reduced to 6,700 m, 3,900 m and 640 m, respectively
(Table VII-1). Therefore, the effect of mitigation, even assuming the 10 minute
Volume VII External Review Draft
VII-6 Do Not Cite or Quote
-------
response time, reduces the predicted downwind distance to the IDLH by
approximately 20% or less, depending on the meteorological conditions. If active
mitigation takes 60 minutes, the maximum downwind distance is the same as for no
.active mitigation.
Active mitigation has no effect on the maximum distance downwind to. the
IDLH value for the 100 gallon spill of formaldehyde waste. Additionally, as was
discussed in Chapter VI, exceedances of the IDLH value for acetone are not
predicted to occur at any off-site inhabited locations, with or without active
mitigation.
Failure of Passive Mitigation
The size of the on-site spill scenario dictates the size of the off-site area that
could be impacted by the release. The larger the source area, the higher the
downwind concentration will be. To assess the increased spill size associated with a
failure of passive mitigation systems, the 5,000 gallon on-site spill of "worst-case"
waste was considered in the sensitivity analysis.
If a 5,000 gallon spill occurs on-site at a location without the berms or drains,
the source area would be approximately 4.5 tunes greater than the area confined by
the berms, based on the assumption that the spill will form a liquid pool of 1 cm in
depth. A sensitivity analysis is performed to examine the distance to the IDLH
concentration for the on-site spill scenario.
For the 5,000 gallon spill of formaldehyde/methanol waste, the distance to the
IDLH concentration increases slightly for a release with no passive mitigation.
Under the typical meteorological condition, the distance to the IDLH concentration
increases by approximately 50%, from 640 m (for the confined release) to 980 m.
Under the conservative meteorological condition, the distance to the IDLH
concentration increases from 4,800 m to 5,000 m. There would be no significant
increase hi maximum downwind distance under calm/inversion conditions. The
slight increase is primarily to the following:
• The off-site concentration increases as the source area increases.
• For the same concentration averaging tune at the receptor, the off-site.
concentration decreases as the emission duration decreases
In summary, distances to the IDLH concentration increase by as much as 50%
in comparison to the scenarios evaluated assuming passive mitigation. However., the
Volume VII External Review Draft
VII-7 Do Not Cite or Quote
-------
severity of consequence ranking would not be significantly affected for the accident
event considered. It should be emphasized that the passive mitigation measures are
already in place at the WTI facility, as shown hi Table II-1.
b. On-Site Fires
As shown hi Table VII-2 and discussed hi Chapter VI, exceedances of the IDLH
values for HC1 and phosgene are not expected off-site with any combination of waste
volume ignited and meteorology conditions. Active mitigation procedures,
therefore, would not affect the results of these scenarios.
c. On-Site Mixing of Incompatible Wastes
For the mixing of compatible waste scenario involving 10,000 gallons of waste,
the maximum downwind distance to reach exceedances of the IDLH value for HC1
without active mitigation are 4,620 m, 3,190 m and 680 m, for calm/inversion,
conservative and typical meteorological conditions, respectively (Table VI-7).
Mitigation within 10 minutes decreases the projected downwind distances under
calm/inversion and conservative conditions by approximately 30%, to 3,380 m and
2,170 m, respectively (Table VII-3). Mitigation within 10 minutes effectively
contains emissions to within the site boundaries under typical meteorological
conditions.
For the mixing of incompatible waste scenario involving 200 gallons of waste,
active mitigation within 10 minutes does not significantly reduce the maximum
downwind distance to the IDLH. Similarly, active mitigation requiring 60 minutes
to implement would not effect the results of the no-mitigation scenarios for either
the 10,000 gallon or 200 gallon events.
2. Effect of Averaging Time
In order to make a direct comparison between the modeled off-site concentrations
and the IDLH value, which is based on a 30-minute exposure period, the modeled off-
site concentrations are also averaged over a 30-minute period. For events where
exposures are shorter than 30 minutes, this averaging serves to effectively decrease the
modeled concentration, therefore decreasing the downwind distance over which the
IDLH is exceeded.
For a continuous plume, which applies to the on-site and off-site fire scenarios, the
concentrations downwind of a source generally decrease with increasing averaging tune
due to the increased meandering of wind direction (Turner 1967):
Volume VII External Review Draft
VII-8 Do Not Cite or Quote
-------
= C,.hr (60/f/ (5)
where, Cs = Concentration averaged over tg, (ppm);
tj = the averaging time (minutes);
Cj.hr = the 1-hr average concentration (ppm); and
p = 0.2 (U.S. EPA 1988).
The decrease in concentration follows a one-fifth power law with the averaging time for
averaging periods from about 3 minutes to about 30 minutes (Steward et al, as cited by
Turner 1967). Studies also indicate the power law exponent could vary between 0.17
and 0.2 and the power law relationship could be applied to averaging times up to 24
hours (Turner 1967). Based on the one-fifth power law relationship, a 15-minute
average concentration will be approximately 15% greater than a 30-minute average.
For a continuous finite duration release, which applies to the spill events and the
mixing of incompatible waste scenarios, the average concentration will be reduced from
the peak concentration if the averaging tune is greater than the source release time,
because the release is relatively short and the receptor is exposed to the material for only
a fraction of the concentration averaging time. For receptors located within a short
distance downwind of the source (e.g. with 1 km downwind of the source), the exposure
time is approximately the same as the source release tune. Therefore, a 10-minute
average concentration would be 3 times higher than a 30-minute average concentration if
the release duration is only 10 minutes. Accordingly, the distance to the IDLH
concentration, based on the 10-minute average concentration, will be greater than that
defined based on the 30-minute average concentration.
To quantitatively evaluate the effect of averaging time on the downwind distance
exceeding the IDLH, two scenarios are examined in the sensitivity analysis:
• On-site spill of 100 gallons of formaldehyde waste
• On-site mixing of 10,000 gallons of incompatible wastes
The results of this analysis are shown hi Table VII-4. For the on-site spill of
formaldehyde waste, the predicted emission duration is approximately 11 minutes. In
the Accident Analysis, the downwind concentrations from this 11 minute release are
averaged over 30 minutes and then compared to the IDLH. In this sensitivity analysis,
Volume VII External Review Draft
VII-9 Do Not Cite or Quote
-------
the downwind concentrations averaged over the 11-minute time span are compared
directly to the IDLH.
As shown in Table ¥11-4, there is an increase in the maximum distance to the
IDLH, if the IDLH is compared directly to the downwind concentration averaged over
the 11-minute time span. The greatest relative increase is under typical meteorological
conditions, where the downwind distance to the IDLH increases from 40 m to 140 m.
This would result in the event being reclassified as having major rather than moderate
consequences. The downwind distance increases from 550 m to 850 m under
conservative meteorological conditions, and from 1,000 m to 1,300 m under
calm/inversion meteorological conditions. Thus, the event would remain classified as
having major consequences under conservative meteorological conditions, but reclassified
as having catastrophic consequences under calm/inversion conditions. The probability of
occurrence ranking would not change for any meterological condition.
The relative increases in maximum distance to IDLH are less significant for the on-
site mixing of incompatible waste scenario. The maximum distance to the IDLH
increases by about 30% for typical meteorological (680 m to 870 m), by about 10% for
conservative meteorology (3,190 m to 3,480 m), and by about 5% for calm/inversion
meteorology (4,620 m to 4,800 m). The severity of consequence classifications and the
probability of occurrence ranking would not change for any meteorological condition.
3. Effect of Using LOCs to Estimate Downwind Distance
To evaluate the sensitivity of the conclusions with respect to the selection of acute
toxicity criteria, the effect of using U.S. EPA LOG values, rather than NIOSH IDLH
values, was assessed. As discussed in Chapter I, U.S. EPA LOG values are generally
lower (i.e., more stringent) than corresponding NIOSH IDLH values. The IDLH and
LOG values for die chemicals quantitatively evaluated hi the Accident Analysis are
summarized on Table VII-5. As shown, the LOG value can be up to 10-fold lower than
the corresponding IDLH, as in the case of phosgene.
The results of the Accident Analysis using the LOG values are shown for the on-site
spill, on-site fire, on-site mixing of incompatible wastes, off-site spill, and off-site fire
scenarios in Tables VII-6 through VII-10. Key results of the sensitivity analysis are the
following:
• For on-site spills involving formaldehyde, exceedances of the LOG value extend
approximately 35% to 100% further than exceedance of the IDLH value,
depending on the meteorological conditions.
Volume VII External Review Draft
VII-10 Do Not Cite or Quote
-------
• No off-site exceedances of the IDLH or the LOG for acetone are predicted for
the on-site spill scenarios.
• For the on-site fire scenarios, IDLH values are not expected to be exceeded for
either HC1 or phosgene. LOG values for both HC1 and phosgene could be
exceeded, however, hi the event of a large (20,000) gallon spill, under
conservative meteorology.
• In the on-site mixing of incompatible waste scenarios, exceedances of LOG
values are predicted to extend about 3-fold to 4-fold further off-site than are
exceedances of IDLH values.
• For on-site spills, exceedances of the LOG value for formaldehyde are predicted
to extend between 35% and 100% further than exceedances of IDLH values for
off-site spills. In addition, the LOG value for acetone is predicted to be
exceeded up to a distance of approximately 120 m hi the event of a 5,000 gallon
spill.
• For on-site fire scenarios, exceedances of the LOG values for HC1 and phosgene
are predicted under conservative meteorological conditions. For off-site fire
scenarios, exceedances of the IDLH values are not predicted.
Thus, as expected, use of LOG values instead of IDLH values as a benchmark for
acute toxicity results hi a larger potential impact area hi terms of the maximum
downwind distance from the accident location. The criteria developed to rank severity
of consequence for the Accident Analysis (shown hi Table VI-1), should not be used hi
evaluating LOG values, because they were developed specifically for comparison to
IDLH values.
01-3999C:PCCOOAC3.W51
Volume VII External Review Draft
VII-11 Do Not Cite or Quote
-------
Spill Size
(gallons)
5,000
5,000
5,000
5,000
5,000
5,000
100
100
100
100
100
100
TABLE VIM
Consequence Assessment, On-Site Spill with Mitigation1'2
Meteorology
Typical
Conservative
Calm/Inversion
Typical
Conservative
Calm/Inversion
Typical
Conservative
Calm/Inversion
Typical
Conservative
Calm/Inversion
Contaminant
Formaldehyde
Formaldehyde
Formaldehyde
Acetone
Acetone
Acetone
Formaldehyde
Formaldehyde
Formaldehyde
Acetone
Acetone
Acetone
Max. Downwind Dist. to
IDLH, 60 min mitigation
time3 (m)
640
4800
8450
-
-
--
40
550
1000
—
—
Max. Downwind Dist. to
IDLH, 10 min mitigation
time4 (m)
640
3920
6720
-
—
-
40
550
1000
..
—
'
Notes:
1 Maximum Downwind Distance from the property line to the east or west, or the existing railroad to the north, whichever is closer to the location of the
release. For the on-site spill, maximum downwind distance was calculated from the railroad line to the north, approximately 75 m from the edge of the
spill.
2 — : IDLH not exceeded in potential off-site receptor areas.
3 Active mitigation assumed to stop emissions within 60 minutes. The maximum downwind distance to IDLH using a 60-minute mitigation time is the
same as the maximum distance to IDLH with no active mitigation.
4 Active or automatic mitigation assumed to stop emissions within 10 minutes.
Volume VII
vr
External Review Draft
Do Not Cite o- xte
-------
TABLE VII-2
Consequence Assessment, On-Site Fire with Mitigation1
Waste Volume
Ignited (gallons)
20,000
20,000
200
200
Meteorology
Typical
Conservative
Typical
Conservative
Contaminant
HC1
Phosgene
HC1
Phosgene
HC1
Phosgene
HC1
Phosgene
Downwind Dist. to IDLH, 60 min
mitigation time1 (m)
—
-
—
-
—
—
-
-
• Downwind Dist. to
IDLH, 10 min mitigation time3 (m)
—
-
—
-
—
—
—
—
Notes:
1 — : IDLH not exceeded in potential off-site receptor areas.
2 Active mitigation assumed to stop emissions within 60 minutes. The maximum downwind distance to IDLH using a 60-minute mitigation time is the
same as the maximum distance to IDLH with no active mitigation.
3 Active or automatic mitigation assumed to stop emissions within 10 minutes.
Volume VII
VII-13
External Review Draft
Do Not Cite or Quote
-------
Waste Volume
(gallons)
10,000
10,000
10,000
200
200
200
TABLE VII-3
Consequence Assessment, On-Site Mixing of Incompatible Wastes with Mitigation1'2
Meteorology
Typical
Conservative
Calm/Inversion
Typical
Conservative
Calm/Inversion
Contaminant
HC1
HC1
HC1
HC1
HC1
HC1
Max. Downwind Dist. to IDLH, 60 min
mitigation time3 (m)
680
3190
4620
—
270
520
Max. Downwind Dist. to
IDLH, 10 min mitigation
time4 (m)
_
2170
3380
—
270
520
Notes:
' Maximum Downwind Distance from the property line to the east or west, or the existing railroad to the north, whichever is closer to the release. For
the on-site mixing of incompatible wastes, the maximum downwind distance was calculated from the railroad line to the north, or approximately 75 m
from the edge of the release.
2 --: IDLH not exceeded in potential off-site receptor areas.
3 Active mitigation assumed to stop emissions within 60 minutes. The maximum downwind distance to IDLH using a 60-minute mitigation time is the
same as the maximum distance to IDLH with no active mitigation.
4 Active or automatic mitigation assumed to stop emission within 10 minutes.
Volume VII
\
V
External Review Draft
Do Not Cite { \fe
J
-------
TABLE VH-4
Results of Averaging Time Sensitivity Analysis
Scenario
On-site spill of 100 gallons
of formaldehyde waste
On-site mixing of 10,000
gallons of incompatible
wastes
Chemical of
Concern
Formaldehyde
HC1
Emission Scenario
Typical
Conservative
Meteorology
Typical
Conservative
Inversion/Calm
Typical
Conservative
Inversion/Calm
Concentration
Averaging Time
(sec)
680
1800
680
1800
305
1800
1200
1800
1200
1800
759
1800
ID.LH
(ppm)
19.6
19.6
19.6
19.6
19.6
19.6
49.1
49.1
49.1
49.1
49.1
49.1
Max. Dist. to
1DLH (m)1
140
40
850
550
1300
1000
870
680
3480
3190
4800
4620
Notes:
1 Maximum Downwind Distance calculated from the property line to the east or west, or the existing railroad to the north, whichever is closer to the
location of the release. For the on-site spill, maximum downwind distance was calculated from the railroad line to the north, approximately 75 m from
the edge of the spill.
Volume VII
VII-15
External Review Draft
Do Not Cite or Quote
-------
TABLE VH-5
IDLH and LOG Values Used for Chemicals Evaluated hi the Accident Analysis
Substance
Acetone
Formaldehyde
Hydrogen Chloride (HC1)
Phosgene
IDLH (g/m3)
(U.S. EPA 1995c)
5.9
0.025
0.075
0.0081
LOC (g/m3)
(U.S. EPA 1995c)
4.7
0.012
6.015
0.0008
Volume VII
VTI-16
External Review Draft
Do Not Cite or Quote
-------
v y
TABLE VII-6
Summary of Downwind Distance to LOG, On-Site Spill
SpiU Size
(gallons)
5,000
5,000
5,000
5,000
5,000
5,000
100
100
100
100
100
100
Meteorology
Typical
Conservative
Calm/Inversion
Typical
Conservative
Calm/Inversion
Typical
Conservative
Calm/Inversion
Typical
Conservative
Calm/Inversion
Contaminant
Formaldehyde
Formaldehyde
Formaldehyde
Acetone
Acetone
Acetone
Formaldehyde
Formaldehyde
Formaldehyde
Acetone
Acetone
Acetone
Max. Downwind Dist. to LOC, no
active mitigation1-1 (m)
1000
8190
11400
--
--
-
100
900
1600
-
-
-
Notes:
1 Maximum Downwind Distance calculated from the property line to the east or west, or the existing railroad to the north, whichever is closer to the
location of the release. For the on-site spill, maximum downwind distance was calculated from the railroad line to the north, approximately 75 m
from the edge of the spill. •
2 — : LOC not exceeded in potential off-site receptor areas.
Volume VII
VII-17
External Review Draft
Do Not Cite or Quote
-------
TABLE VII-7
Summary of Downwind Distance to LOC, On-Site Fire
Waste Volume Ignited (gallons)
20,000
20,000
200
200
Meteorology
Typical
Conservative
Typical
Conservative
Contaminant
HC1
Phosgene
HC1
Phosgene
HC1
Phosgene
HC1
Phosgene
Downwind Dist. to LOC, no active
mitigation1'1 (m)
—
.
675-1125
~
-
-
-
-
Notes:
1 For the on-site fire scenarios, LOC values are predicted to be exceeded in areas in a zone approximately 675 m to 1 125 m downwind from the center of
the on-site fire source, under conservative meteorological conditions. The areas of exceedance within this zone are expected to be "pockets" with radii
of approximately 25 m.
2 -: LOC not exceeded in potential off-site receptor areas.
Vo' -e VII
j
\
External Review Draft
Do Not Cite \e
-------
TABLE VII-8
Summary of Downwind Distance to LOC, On-Site Mixing of Incompatible Wastes
Waste Volume
(gallons)
10,000
10,000
10,000
200
200
200
Meteorology
Typical
Conservative
Calm/Inversion
Typical
Conservative
Calm/Inversion
Contaminant
HC1
HC1
HC1
HC1
HC1
HC1
Max. Downwind Dist. to LOC, no active
mitigation1-2 (m)
1780
8790
12200
130
980
1700
Notes:
1 Maximum Downwind Distance calculated from the property line to the east or west, or the existing railroad to the north, whichever is closer to the
release. For the on-site mixing of incompatible wastes, the maximum downwind distance was calculated from the railroad line to the north, or
approximately 75 m from the edge of the release.
2 — : LOC not exceeded in potential off-site receptor areas.
Volume VII
VII-19
External Review Draft
Do Not Cite or Quote
-------
TABLE VII-9
Summary of Downwind Distance to LOG, Off-Site Spill
Spill Size
(gallons)
5,000
5,000
5,000
5,000
5,000
5,000
100
100
100
100
100
100
Meteorology
Typical
Conservative
Calm/Inversion
Typical
Conservative
Calm/ Inversion
Typical
Conservative
Calm/Inversion
Typical
Conservative
Calm/Inversion
Contaminant
Formaldehyde
Formaldehyde
Formaldehyde
Acetone
Acetone
Acetone
Formaldehyde
Formaldehyde
Formaldehyde
Acetone
Acetone
Acetone
Max. Downwind Dist. to LOG, no active
mitigation1'1 (m)
1490
8490
11540
<10
<10
57
190
980
1670
<10
<10
<10
Notes:
1 Maximum Downwind Distance calculated from edge of spill.
2 — : LOG not exceeded in off-site potential receptor areas.
VII
External Review Draft
Do Not Cite / te
-------
TABLE VII-10
Summary of Downwind Distance to LOC, Off-Site Fire
Waste Volume Ignited (gallons)
5,000
5,000
100
100
Meteorology
Typical
Conservative
Typical
Conservative
Contaminant
HCI
Phosgene
HCI
Phosgene
HCI
Phosgene
HCI
Phosgene
Downwind Dist. to LOC, no active
mitigation1 (m)
.
—
2100'
1100'
—
~
—
-
Notes:
1 For the off-site fire scenarios, LOC values for HCI and phosgene are predicted to occur in areas within approximately 2100 m and 1100 m,
respectively, downwind from the center of the fire under conservative meteorological conditions. The areas of exceedance within this zone are expected
to be "pockets" in locations of elevated terrain.
2 --: LOC not exceeded in potential receptors areas.
Volume VII
VII-21
External Review Draft
Do Not Cite or Quote
-------
VIII. SUMMARY AND CONCLUSIONS
The results of the Accident Analysis are summarized hi Table VIII-1 (typical
meteorology), Table VIII-2 (conservative meteorology) and Table VII-3 (calm/inversion), in
terms of severity of consequences and probability of occurrence. The rankings in Tables
VIII-1, VIII-2, and VIII-3 were developed according to the guidelines established by U.S.
EPA (1987) and FEMA (1993). As shown in the summary tables, the probability of an
accident with major or catastrophic consequences is classified as unlikely or very unlikely.
With one exception (on-site spill of 100-gallons of formaldehyde waste) the probability of an
accident with moderate consequences is also classified as unlikely or very unlikely. The on-
site typical-sized spill of a worst-case chemical (e.g. 100 gallons of formaldehyde waste)
during typical meterology was classified as reasonably likely. It should be recognized that
this event represents the general class of small on-site spills of highly volatile, highly toxic
chemicals rather than a 100 gallon spill of formaldehyde waste only. Events with minor
consequences are classified as likely to occur; no accidents evaluated in this assessment are
classified as common.
There is no standard approach for interpreting the results of an Accident Analysis. As
stated in FEMA (1993), "Special circumstances may require special consideration on a case
by case basis. Specific guidelines should be worked out by each locale to represent the
resources and relationships between organizations applicable to that community" (p. 13-5).
According to U.S. EPA (1987) and FEMA (1993), however, an accident frequency/severity
screening matrix approach can be useful in considering the results of an Accident Analysis.
An illustrative matrix suggested by FEMA (1993) is presented hi Figure VIII-1. In this
matrix, the need for comprehensive planning and preparedness is linked to the probability of
occurrence and severity of consequence of an event. Based on Figure VIII-1, and Tables
VIII-1 to VIII-3, the results of the WTI Accident Analysis can be presented as follows:
"Events for which comprehensive planning and preparedness are essentially mandatory at
the appropriate levels of government or industry" (FEMA 1993)
• On-site spills of 100 gallons acetone waste
Volume VII External Review Draft
VIII-1 Do Not Cite or Quote
-------
"Events for which comprehensive planning is optional and does not necessarily warrant
anv maior efforts or costs" (FEMA 1993)
. • On-site spills of 100 gallons of formaldehyde waste
• On-site spill of 5,000 gallons of formaldehyde waste
• On-site mixing of 200 gallons of incompatible wastes
• On-site mixing of 10,000 gallons of incompatible wastes
• Off-site spill of 100 gallons of formaldehyde waste
• Off-site spill of 5,000 gallons of formaldehyde waste
• Off-site fire involving 100 gallons of chlorinated waste
"Events for which comprehensive planing may be unwarranted and unnecessary" (FEMA
1993)
• On-site spill of 5,000 gallons of acetone waste
• On-site fire involving 200 gallons of chlorinated waste
• On-site fire involving 20,000 gallons of chlorinated waste
• Off-site spill of 100 gallons of acetone waste
• Off-site spill of 5,000 gallons of acetone waste
• Off-site fire involving 5,000 gallons of chlorinated waste
In general, the consequence-probability rankings summarized in Tables VIII-1 to VIII-3
are consistent with the information presented in the Report on Emergency Incidents at
Hazardous Waste Incinerators and Commercial Treatment, Storage and Disposal Facilities
(TSDFs) (U.S. EPA 1995b). Using the data from U.S. EPA (1995b), and the rankings based
on FEMA (1993), the probability of an event having moderate, major, or catastrophic
consequences would be classified as unlikely or very unlikely over a facility lifetime. The
probability of an event having minor consequences would be classified as likely or reasonably
likely. This generally agrees with the consequence-probability rankings used in this Accident
Analysis.
Volume VII External Review Draft
VIII-2 Do Not Cite or Quote
-------
TABLE Vra-1
Probability/Severity Matrix
Typical Meteorological Conditions
Possibility of
Occurrence
Severity of Consequence
Minor
Moderate
Major
Catastrophic
Common
Likely
Scenario 1A
Reasonably Likely
Scenario 1C
Scenario 2A
Scenario 3A
Scenario 4A
Scenario IB
Unlikely
Scenario 2B
(no fire ball)
Scenario 4C
Scenario 5A
Scenario ID
Scenario 3B
Scenario 4B
Very Unlikely
Scenario 5B
(no fireball)
Scenario 4D
Scenario 5B
(with fireball)
Scenario 2B
(with fireball)
Scenario 1A: On-site spill, 100 gallons, acetone waste
Scenario IB: On-site spill, 100 gallons, formaldehyde waste
Scenario 1C: On-site spill, 5,000 gallons, acetone waste
Scenario ID: On-site spill, 5,000 gallons formaldehyde waste
Scenario 2A: On-site fire, 200 gallons, chlorinated waste
Scenario 2B: On-site fire, 20,000 gallons, chlorinated waste
Scenario 3A: On-site mixing of incompatible wastes, 200 gallons
Scenario 3B: On-site mixing of incompatible wastes, 10,000 gallons
Scenario 4A: Off-site spill, 100 gallons, acetone waste
Scenario 4B: Off-site spill, 100 gallons, formaldehyde waste
Scenario 4C: Off-site spill, 5,000 gallons, acetone waste
Scenario 4D: Off-site spill, 5,000 gallons, formaldehyde waste
Scenario 5A: Off-site fire, 100 gallons, chlorinated waste
Scenario 5B: Off-site fire, 5,000 gallons, chlorinated waste
Volume VII
vm-3
External Review Draft
Do Not Cite or Quote
-------
TABLE Vffl-2
Probability/Severity Matrix
Conservative Meteorological Conditions
Possibility of
Occurrence
Severity of Consequence
Minor
Moderate
Major
Catastrophic
Common
Likely
Reasonably Likely
Scenario 1A
Unlikely
Scenario 1C
Scenario 2A
Scenario 4A
Scenario IB
Scenario 3A
Very Unlikely
Scenario 2B
(no fireball)
Scenario 5A
Scenario 4C
Scenario 2B
(with fireball)
Scenario 5B
(with or
without
fireball)
Scenario ID
Scenario 3B
Scenario 4B
Scenario 4D
Scenario 1A: On-site spill, 100 gallons, acetone waste
Scenario IB: On-site spill, 100 gallons, formaldehyde waste
Scenario 1C: On-site spill, 5,000 gallons, acetone waste
Scenario ID: On-site spill, 5,000 gallons formaldehyde waste
Scenario 2A: On-site fire, 200 gallons, chlorinated waste
Scenario 2B: On-site fire, 20,000 gallons, chlorinated waste
Scenario 3A: On-site mixing of incompatible wastes, 200 gallons
Scenario 3B: On-site mixing of incompatible wastes, 10,000 gallons
Scenario 4A: Off-site spill, 100 gallons, acetone waste
Scenario 4B: Off-site spill, 100 gallons, formaldehyde waste
Scenario 4C: Off-site spill, 5,000 gallons, acetone waste
Scenario 4D: Off-site spill, 5,000 gallons, formaldehyde waste
Scenario 5A: Off-site fire, 100 gallons, chlorinated waste
Scenario 5B: Off-site fire, 5,000 gallons, chlorinated waste
Volume VII
VHI-4
External Review Draft
Do Not Cite or Quote
-------
TABLE Vm-3
Probability/Severity Matrix
Calm/Inversion Meteorological Conditions
Possibility of
Occurrence
Common
Likely
Reasonably Likely
Unlikely
Very Unlikely
Severity of Consequence
Minor
Scenario 1A
Scenario 1C
Scenario 4A
Moderate
Scenario 4C
Major
Scenario IB
Scenario 3A
Catastrophic
Scenario ID
Scenario 3B
Scenario 4B
Scenario 4D
Scenario 1A: On-site spill, 100 gallons, acetone waste
Scenario IB: On-site spill, 100 gallons, formaldehyde waste
Scenario 1C: On-site spill, 5,000 gallons, acetone waste
Scenario ID: On-site spill, 5,000 gallons formaldehyde waste
Scenario 3A: On-site mixing of incompatible wastes, 200 gallons
Scenario 3B: On-site mixing of incompatible wastes, 10,000 gallons
Scenario 4A: Off-site spill, 100 gallons, acetone waste
""i
Scenario 4B: Off-site spill, 100 gallons, formaldehyde waste
Scenario 4C: Off-site spill, 5,000 gallons, acetone waste
Scenario 4D: Off-site spill, 5,000 gallons, formaldehyde waste
01-3999C:PCCOOAC3.W51
Volume VII
Vffl-5
External Review Draft
Do Not Cite or Quote
-------
SEVERITY OF CONSEQUENCE
REASONABLY
LIKELY
COMPREHENSIVE PLANNING AND PREPAREDNESS ARE ESSENTIALLY
MANDATORY AT THE APPROPRIATE LEVELS OF GOVERNMENT OR INDUSTRY.
COMPREHENSIVE PLANNING IS OPTIONAL AND DOES NOT NECESSARILY
WARRANT ANY MAJOR EFFORTS OR COSTS. GIVE CONSIDERATION TO
SHARING ANY NECESSARY SPECIAL RESPONSE RESOURCES ON A
REGIONAL BASIS.
COMPREHENSIVE PLANNING MAY BE UNWARRANTED AND UNNECESSARY.
TAKEN FROM FEMA (1993)
External Review D
Do Not Cite or Qu
DRAFTED BY: JT DATE: 8/28/95
ILLUSTRATIVE ACCIDENT
FREQUENCY/SEVERITY
Cr'DCTC'MIKI^ MATDIY
bLKLLNHNU MAIKIA
Figure
VIII-1
01— 3999CP01
Volume VII " VTII-6
-------
IX. REFERENCES
American Society for Testing and Materials (ASTM). 1986. Proposed guide for estimating
the incompatibility of selected hazardous wastes based on binary chemical reactions. D-
34 Proposal P 168. March.
Battelle. 1987. Hazard Analysis of Ontario Waste Management Industrial Waste Treatment
and Disposal Facility. Phase II Probability of Tank Farm Fire Involving Vaporization of
Halogen-Organic Waste. Prepared for the Ontario Waste Management Corporation.
March.
Bretherick, L. 1985. Handbook of reactive chemical hazards. Third edition. Butterworths.
Boston.
Burgess, D. S., A. Strasser, and J. Grumer. 1961. Diffusive burning of liquid fuel in open
trays. The Fire Research Abs. & Review 3:177.
Chung, D. (U.S. EPA Emergency Preparedness Office). 1995. Personal Communication,
June 7.
Duyzh, R., U.S. Department of Transportation. 1995. Telephone conversation with D.
Arsnow of ENVIRON. May 23.
Ermak, D.L. 1990. User's manual for the SLAB model, an atmospheric dispersion model
for denser-than-air releases, Lawrence Livermore National Laboratory UCRL-MA-
105607.
Federal Emergency Management Agency (FEMA). 1993. Handbook of chemical hazard
analysis procedures. NTIS PB93-158756.
Howard, P.M. 1989. Handbook of environmental fate and transport data (Vol. I. Large
Production and Priority Pollutants). Chelsea, MI.
Howard, P.H. 1990. Handbook of environmental fate and transport data (Vol. II. Solvents).
Chelsea, MI.
Gallant, R.W. 1968. Physical properties of hydrocarbons: Hydrocarbon Processing. Vol.
47, No. 5. May.
Volume VII External Review Draft
IX-1 Do Not Cite or Quote
-------
Moorhouse J. and R. J. Carpenter. 1986. Factors affecting vapor evolution rate from
liquified gas spills. In Refining of estimates of fee consequences of heavy toxic vapor
releases. Institution of Chemical Engineers. North Western Branch.
January 8.
Montgomery, J.H., and L.M. Welkom. 1990. Groundwater chemical desk reference.
Chelsea, MI.
National Library of Medicine. 1991. Hazardous Substances Data Bank (HSDB).
Nazario, F.A. 1988. Preventing or surviving explosions. Chemical Engineering August 15,
1988. p. 102-109.
Ohio Department of Public Safety (ODPS). 1995. Letter to USEPA Region V summarizing
truck crashes in East Liverpool and Ohio State. September 1.
O'Mara, M. M., L. B. Crider, and R. L. Daniel. 1971. Combustion products from vinyl
chloride monomer. Amer. Industrial Hygiene Assoc. Journal 32:153-156.
Perry, R.H. and D. Green. 1984. Perry's chemical engineers' handbook, sixth edition.
McGraw-Hill Book Company, New York.
Randerson, D. 1984. Atmospheric boundary layer, in Atmospheric science and power
production, ed. by D. Randerson. United States Department of Energy. DOE/TIC-
27601. Washington, D.C.
Randolph, K. (U.S. EPA). Personal Communication. May.
Sax, N. L and R. J. Lewis, Sr. 1989. Dangerous properties of industrial materials.
Seventh edition. Van Nostrand Reinhold. New York.
SE Technologies, Inc. 1992. Waste Technologies Industries: Credible event analysis for
emergency planning. March.
Sjoberg, B. 1952. Thermal decomposition of chlorinated hydrocarbons. Svensk Kemistk
Tidsskrift 64:63-79.
Turner, D.B. 1967. Workbook of Atmospheric Dispersion Estimates. U.S. Department of
Health, Education, and Welfare. Publication No. 999-A1-26. Cincinnati, Ohio.
United States Department of Commerce (USDOC). 1993. Statistical Abstract of the United
States: 1993 (I13th Ed.). U.S. Bureau of the Census. Washington, DC.
United Stated Department of Transportation (U.S. DOT). 1986. Hazardous Materials
Information System.
Volume VII External Review Draft
IX-2 Do Not Cite or Quote
-------
United States Department of Transportation (U.S. DOT). 1995. Hazardous Materials
Information System.
United States Environmental Protection Agency (U.S. EPA). 1983. Hazardous Waste
Management Permit, Waste Technologies Industries. EPA Identification
#OHD980613541. U.S. Environmental Protection Agency, Region V.
United States Environmental Protection Agency (U.S. EPA), Federal Emergency
Management Agency (FEMA), and United States Department of transportation (U.S.
DOT). 1987. Technical guidance for hazards analysis: Emergency planning for
extremely hazardous substances. OSWER-88-0001 (NTIS PB93-206910). December.
United States Environmental Protection Agency (U.S. EPA). Office of Air Quality Planning
and Standards. 1988. A workbook of screening techniques of assessing impacts of toxic
air pollutants. U.S. EPA-450/4-88-009. Research Triangle Park, N.C. September.
United States Environmental Protection Agency (U.S. EPA). 1992a. Framework for
Ecological Risk Assessment. EPA/630/R-92/001.
United States Environmental Protection Agency (U.S. EPA). 1992b. Office of Air Quality
Planning and Standards. Workbook of screening techniques for assessing impacts of toxic
air pollutants (Revised). U.S. EPA 454/R-92-024. May.
United States Environmental Protection Agency (U.S. EPA). 1992c. Guidelines for
Exposure Assessment. Federal Register 57: 22888-22938. May 29.
U.S. Environmental Protection Agency (U.S. EPA). 1993a. WUphase II risk assessment
project plan, EPA ID number OHD98061354L Region V, Chicago, Illinois. EPA
Contract No. 68-W9-0040, Work Assignment No. R05-06-15. November.
United States Environmental Protection Agency (U.S. EPA). 1993. Office of Air Quality
Planning and Standards. Guidance on the application of refined dispersion models for
hazardous/toxic air releases. U.S. EPA-454/R-93-002. Research Triangle Park, NC.
May.
United States Environmental Protection Agency (U.S. EPA). 1994a. Risk Assessment
Forum. Report on the technical workshop on WTI incinerator risk issues and Fact Sheet.
U.S. EPA/630/R-94/001. Washington, D.C.
United States Environmental Protection Agency (U.S. EPA). 1994b. National analysis:
The biennial RCRA hazardous waste report (Based on 1991 data). U.S. EPA 530-R-94-
039c. Washington, D.C.
United States Environmental Protection Agency (U.S. EPA). 1995a. Accidental release
prevention requirements: Risk management programs under Clean Air Act Section
112(r)(7); Proposed rule. Federal Register 60:13526-13545. March 13.
Volume VII External Review Draft
IX-3 Do Not Cite or Quote
-------
United States Environmental Protection Agency (U.S. EPA). 1995b. Report on emergency
incidents at hazardous waste incinerators and commercial treatment, storage, and
disposal facilities (TSDFs). Draft. May.
United States Environmental Protection Agency (U.S. EPA). 1995c. Most current IDLHs
for the WTI Accident Analysis. Memorandum from C. Bogard, Region 5 RCRA
Permitting Branch, to C. Matthiessen, CEPPO.
United States Environmental Protection Agency (U.S. EPA). 1995d. Toxic Release
Inventory, Public Data Release. Washington, D.C. EPA 745-R-95-010.
Victorine, G. U.S. EPA Region 5. 1995a. Personal Communication. February.
Victorine, G. U.S. EPA Region 5. 1995b. Personal Communication. May.
Victorine, G. U.S. EPA Region 5. 1995c. Personal Communication. September.
Victorine, G. U.S. EPA Region 5. 1995d. Personal Communication. September.
Von Roll Corporation (Von Roll). 1993. Waste Technologies Industries: Emergency plan
exercise. September 23.
Von Roll Corporation (Von Roll). 1994. Von Roll Fire Protection Systems.
Waste Technologies Industries (WTI). 1982. Application to the U.S. Environmental
Protection Agency. September 4, as revised November 11.
Waste Technologies Industries (WTI). 1992. Contingency plan and spill prevention, control
and countermeasures plan. April 24.
01-3999C:PCCOOAC3.WS1
Volume VII External Review Draft
IX.-4 Do Not Cite or Quote
-------
APPENDIX VH-1
Incidents Reported at the WTI Facility
and Comparable Facilities
-------
TABLE 1
Hazardous Waste Combustor Facilities1
Facility
3-M
Cottage Grove, MN
Allied Chemical
(aka "Allied Signal, Inc.-
Environmental Systems and
Services" in HWC [1995])
Birmingham, AL
Aptus
Coffeyville, KS
Aptus
Aragonite, UT
Commercial
Incinerator?/
Capacity (tpy)1
No
Yes
PAIC & RC(1): 2,200
Yes
PAIC: 60,850
RC(1): 219,000
(Per Victorine 1995b,
facility says permit limit
is same, as PAIC, not
higher RCRIS value.)
Yes
RC(3): 86,000
Years of
Operation3
15+ (since
at least
early 80s,
per U.S.
EPA 1995a)
15 +
(pre-81)
10
(since 86)
4
(Since late
91)
Reported Incidents4
(1) incinerator
operations; explosion
(2) incinerator
operations; explosion
NR
incinerator operations;
explosion
NR
Incident Date and Description
(1) Date: Early 1980s
Description: hot slae contacted low
temperature ash quench water, resulting in a
thermal explosion.
(2) Date: 9/18/92
Description: molten metal in slae dropped
into ash quench, trapping some water and
creating a steam explosion.
i
Date: Fall 1990
Description: waste with high BTU level
introduced to incinerator; gas accumulated in
scrubber and was set off by spark, causing an
explosion in the scrubber.
Reported
Impact
(1) no injuries; no releases
to the environment
(2) no injuries; brief release
of smoke from burning fuel
oil; no other releases of
hazardous waste
no injuries; no natural
resource damages; no
hazardous waste released;
possible exceedances of
hydrochloric acid and
particulate in air emissions
Volume VII
Appendix VIM
1-1
External Review Draft
Do Not Cite or Quote
-------
TABLE 1
Hazardous Waste Combustor Facilities1
Facility
Atochem
Carrollton, KY
Bridgeport Rental and Oil
Services (BROS), NJ
Chemical Waste Management
(CWM)
Chicago, IL
Commercial
Incinerator?/
Capacity (tpy)1
Yes
RC(3): 11,000
(Per Victorine 1995b,
EPA Reg.4 calls this a
"limited commercial in-
cinerator," allowed to
receive only 3,800 tpy
off-site haz. waste; feed
limits total 13,700 tpy.)
No
Yes
Years of
Operation3
15 +
(pre-81)
10+
(pre-81 to
2/91)
Reported Incidents4
NR
(1) incinerator
operations; explosion
(2) incinerator
operations; release
incinerator operations;
explosion
Incident Date and Description
(1> Date: 9/20/92
Description: explosion caused by rapid steam
generation that resulted when a slag ring that
formed in the kiln fell into the water in the
ash quench; fugitive emissions resulted.
Total hydrocarbon (THC) monitor readings
unusual prior to explosion.
(2) Date: 9/21/92
Description: release of large amount of ash;
particulate matter released for 8 minutes.
Date: 2/13/91
Description: drum with a packet containing
tetrazole fed into rotary kiln, causing an
explosion.
Reported
Impact
(1) fugitive emissions; no
injuries or natural resource
damage reported.
(2) particulate matter
traveled off-site; no impacts
reported
no injuries or releases to
environment
Volume
Appendix
Exf
Di
'Review Draft
hte or Quote
-------
TABLE 1
Hazardous Waste Combustor Facilities1
Facility
Chemical Waste Management
(CWM)
Port Arthur, TX
Chemron6
Palmer, AK
Diversified Scientific Services,
Inc. (DSSI) .
Kingston, TN
Dow Chemical
Midland, MI
Commercial
Incinerator?/
Capacity (tpy)1
Yes
Yes
RC(2) & RC(3)
combined: 13,000
No
No
Years of
Operation9
6
(since -90)
Reported Incidents4
(1) incinerator
equipment failure; fire
(2) equipment failure;
spill
NR
operations; fire
(1) incinerator
operations; explosion
(2) incinerator
operations; explosion
Incident Date and Description
(1) Date: 6/92
Description: kiln fire that resulted from
overheating during normal operation.
(2) Date: 12/24/92
Description: one gallon of air pollution
control train waste leaked; workers assumed
it contained PCBs; immediate cleanup,
including removal of asphalt and soil, until no
visible waste (tests showed waste did not
contain PCBs).
Date: 7/31/92
Description: electrical outage allowed some
unburned propane to go through boiler;
charcoal filters in secondary air pollution
control (APC) system caught fire and burned
for 4 minutes.
(I) Date: 1/25/92
Description: feed line to incinerator blocked;
nozzle removed improperly and natural gas
leaked out, causing an explosion.
(2) Date: 2/4/93
Description: explosion in incinerator; solid,
non-regulated rubbish released, visible flames
and hot gases emitted.
Reported
Impact
(1) no information provided
(2) no injuries or
environmental impacts
no injuries; no hazardous
waste releases
(1) one worker injury; no
hazardous waste released;
no natural resource damage
(2) no injuries or exposures
to hazardous waste
Volume VII
AnnpnHiy VII-1
External Review Draft
Do Not Cite or Quote
-------
TABLE 1
Hazardous Waste Combustor Facilities1
Facility
E.I. DuPont de Nemours7
Axis, AL
Eastman Kodak Company
Kodak Park, NY
ECOVA (formerly Waste-Tech)
Kimball, NE
ENSCO
El Dorado, AR
General Electric
Pittsfield, MA
Commercial
Incinerator?/
Capacity (tpy)1
No
No
Yes
PAIC: 45,000
Yes
Yes
Years of
Operation3
New
15+
(pre-81)
15 +
(pre-81)
Reported Incidents4
(1) equipment failure;
spill
(2) operations;
explosion
incinerator eqpt failure
NR
(1) incinerator eqpt
failure; explosion
(2) operations; fire
NR
Incident Date and Description
(1) Date: 6/9/94
Description: approx. 3.800 gallons sulfuric
acid released from leaking transfer pipe;
2,500 gallons recovered.
(2) Date: 6/10/94
Description: One drum containing hydrogen
peroxide and ground corncobs burst.
Date: 7/12/90
Description: Recycle cooling water svstem
ruptured, spilling 75^31 water (2 gal onto
ground, 73 gal into industrial sewer). Loss of
pressure in system following rupture caused
an automatic shutdown of the facility;
emergency stack opened, resulting in a visible
plume (wastes in the kiln at the time were 10-
chloro-2,4-dinitrobenzene and 2-
methylhydroquinone) from stack that lasted 7
minutes.
(1) Date: 4/20/89
Description's) : explosion in waste heat
recovery unit due to equipment failure; no
hazardous waste involved.
(2) Date: 8/10/93
Description: spontaneous combustion due to
worker leaving cap off container of bromine
and chlorine.
Reported
Impact
(1) 300 yd3 contaminated
soil removed (apparently
on-site)
(2) none reported
visible soil contamination
from spill to ground
(cleaned up immediately);
visible plume; no other
information available
(1) no injuries or significant
releases
(2) no injuries; no
information on
environmental impacts
Volume VII
Appendix V"
Extern-1 Review Draft
Do' sjte or Quote
-------
TABLE 1
Hazardous Waste Combustor Facilities1
Facility
ICI Environmental
Joplin, MO
Johnston Atoll Chemical Agents
Disposal System (J AC ADS),
Johnston Atoll
Commercial
Incinerator?/
Capacity (tpy)1
Yes
No
Years of
Operation3
New
5
(trial burn
2/90, per
app. to
U.S. EPA
1995a)
Reported Incidents4
NR
(1) incinerator eqpt
failure
(2) incinerator eqpt
failure; fire
(3) incinerator eqpt
failure
(4) incinerator eqpt
failure
(5) incinerator eqpt
failure
(6) spill
Incident Date and Description
(1) Date: 12/90
Description: short-term leakage of nerve
agent from agent feed system after feed shut
off; emissions lasted for 45 minutes.
(2) Date: 3/11/91
Description: instrumentation malfunction
resulting in smoke release, no chemical agent
being processed.
(3) Date: 5/2/91
Description: small bearing cooling oil fire.
caused by an overheated bearing.
(4) Date: 6/26/91
Description: pressure transient occurred
during start-up, resulting in deformation of
furnace chamber and building.
(5) Date: 1/21/92
Description: kiln stopped rotating, svstem
shut down.
(6) Date: 12/18/92
Description: spill onto coral of 50 gal
xylene, 1.6 gal hexane, 0.6 gal isopropanol,
due to wind storm; contingency plan
implemented, soil (coral) sampling
performed.
Reported
Impact
(1) emissions below
permitted levels
(2) no information provided
(3) no harmful releases
reported
(4) no information provided
(5) no releases reported
(6) no information provided
Volume VII
Appendix VII-1
1-5
External Review Draft
Do Not Cite or Quote
-------
TABLE 1
Hazardous Waste Combustor Facilities1
Facility
Commercial
Incinerator?/
Capacity (tpy)1
Years of
Operation3
Reported Incidents4
Incident Date and Description
Reported
Impact
Johnston Atoll Chemical Agents
Disposal System (JACADS),
continued
(7) operations5
(8) leak5
(9) operations5; fire
(10) operations; release
(11) operations5 spill
(12) incinerator eqpt
malfunction;
fire
(13) incinerator eqpt
malfunction, etc.;
release
(7) Date: 12/27-28/92
Description: losses of ventilation due to
power loss in Munitions Demilitarization
Building (MDB); contingency plan
implemented.
(8) Date: 12/28/92
Description: small amount of leakage from
rocket.
(9) Date: 1/2/93
Description: fire in Explosion Containment
Room.
(10) Bate: 5/31/93
Description: potential release of 0.012 mg/m3
mustard gas outside building (allowable stack
cone., 0.03 mg/ms).
(ll)p_ate: 12/9/93
Description: spill of 500 Ibs of chemical
agent in MDB.
(12) Date: 3/14/94
Description: small fire caused by hot gases
in feed chute, due to feed gates jamming.
(13) Date: 3/24/94
Description: release of chemical agent above
allowable limit for 25 minutes, due to design
and procedural problems, equipment
malfunction, operator error.
(7) no chemical agent
migration outside building
(8) off-site: no hazards to
human health or
environment
(9) no information provided
(10) no information
provided
(11) spill contained in
building
(12) no migration of
hazardous waste inside or
outside facility
(13) maximum ground level
concentrations below
General Population Limit
Volume VII
Appendix
Exte-
D/
^Review Draft
)ite or Quote
-------
TABLE 1
Hazardous Waste Combustor Facilities1
Facility
Laidlaw Environmental
Roebuck, SC
Laidlaw Environmental Services
Clarence, NY
Lake City Army Ammunition
Plant
Independence, MO
Commercial
Incinerator?/
Capacity (tpy)2
Yes
PAIC & RC(1): 39,000
Yes
RC(1): 131
(Per Victorine 1995b,
NYDEC indicates this is
a non-RCRA incinerator
due to ICR exemption)
No
Years of
Operation3
15 +
(pre-81)
15 +
(pre-81)
Reported Incidents4
(1) transfer line failure
(2) bulk liquid storage
(3) incinerator eqpt
failure
(4) operations3
(5) operations5, fire
NR
incinerator operations
Incident Date and Description
(1) Date: 3/17/82
Description: 3,000-Eal solvents spilled from
corroded pipe that connects the blend tanks to
the incinerator.
(2) Date: 2/9/88
Description: 6.000-gal maleic anhydride
spilled from storage tank.
(3) Date: 3/22/91
Description: thermal relief vent from
incinerator vaporizer blown off the unit; fell
down to the direct burn containment pad.
(4) Date: 2/8/94
Description: vapor cloud emitted during
redrumming of orthochlorophenol.
(5) Date: 9/19/94
Description: small fiberglass fire, contained
and extinguished in 3 minutes.
Date: 3/29/91
Description: During trial burn, live rounds
put through incinerator, not completely
treated, fell off of conveyor belt and set off.
Reported
Impact
(1) on-site: soil
contamination (removed)
off-site: no impacts noted
(2) on-site: soil
contamination (removed)
off-site: no impacts noted
(3) no injuries or known
hazardous waste releases
(4) off-site: vapor cloud
drifted off-site; one person
reported sinus problem
(5) none reported
no injuries; no significant
. releases
Volume VII
Appendix VII-1
1-7
External Review Draft
Do Not Cite or Quote
-------
TABLE 1
Hazardous Waste Combustor Facilities1
Facility
LWD
Clay, KY
Monsanto Company
Muscatine, I A
Rhone-Poulenc Basic Chemical
Company-Hammond Plant*
Hammond, IN
Rhone-Poulenc Basic Chemicals
Company
Baton Rouge, LA
Rhone-Poulenc Basic Chemicals
Houston, TX
Rollins Environmental Services
Logan Township, NJ (aka
Bridgeport)
Commercial
Incinerator?/
Capacity (tpy)1
Yes
No
Yes
PAIC: 80,000
(converted from 20 mil.
gpy assuming 8 Ib/gal)
RC(3): 84,000
Yes
Yes
Yes
RC(1): 81,796
Years of
Operation3
15 +
(pre-81)
15 +
(pre-81)
15 +
(pre-81)
25 (since 70
per U.S.
EPA 1995a,
App. 1)
Reported Incidents4
transportation; fire
incinerator eqpt
failure; fire
NR
NR
NR
bulk liquid storage;
fire5
Incident Date and Description
Date: 2/2/82
Description: direct-feed tank truck containing
acetone exploded and caught on fire; three
other trucks also caught fire; no releases.
Facility now closed.
Date: 7/92
Description: loss of quench water flow that
caused temperature in scrubber to rise,
causing fire. Incinerator only burning natural
gas at the time.
Date: 12/8/77
Description: series of explosions and fires at
a tank farm.
Reported
Impact
on-site: operator had burns.
fractured leg; oil/acetone
mixture released; releases
contained in berm
off-site: fire-fighting water
reached drainage ditch, then
creek
no injuries; no release of
hazardous waste
on-site: 6 fatalities. 12
injuries, soil and ground
water contamination
off-site: no contamination
Volume VTT
Appendix
Exte-
Dc
' .Review Draft
'ite or Quote
-------
TABLE 1
Hazardous Waste Combustor Facilities1
Facility
Rollins Environmental Services
Baton Rouge, LA
Rollins Environmental Services
Deer Park, TX
Ross Incineration Services
Grafton, OH
Commercial
Incinerator?/
Capacity (tpy)1
Yes
RC(3): 59,000
or
RC(1): 289,605
(converted from 30
metric tons/hr, assuming
1 metric ton = 1.102
tons)
Yes
RC(3): 122,000
Yes
RC(1): 140,160
or
RC(2): 105,000
Years of
Operation3
15+
(pre-81)
15 +
(pre-81)
15 +
(pre-81)
Reported Incidents4
NR
operations; fire
(1) incinerator
operations; fire
(2) incinerator
operations; explosion
Incident Date and Description
••
Date: 11/91
Description: fire in furnace duct.
(1) Date: 8/12/94
Description: drum ignited due to acid residue
improperly left on skid; cyclohexane, styrene,
and mineral spirits released to air.
(2) Date: 5/1/95
Description: explosion in secondary
combustion chamber while feeding drummed
waste; chamber damaged; roof left open to
environment.
Reported
Impact
no information provided
(1) one worker injured; no
information on
environmental impacts
(2) no injuries; fugitive
emissions; no information
on environmental impacts
Volume VII
Appendix VII-1
1-9
External Review Draft
Do Not Cite or Quote
-------
TABLE 1
Hazardous Waste Combustor Facilities1
Facility
Commercial
Incinerator?/
Capacity (tpy)z
Years of
Operation3
Reported Incidents4
Incident Date and Description
Reported
Impact
ThermalKEM
Rock Hill, SC
Yes
PAIC: 25,000
15 +
(pre-81)
(1) incinerator
operations; explosion
(2) incinerator
operations;
explosion
(3) incinerator eqpt
failure; explosion
(4) fire5
(5) mixing wastes3; fire
(1) Date: 7/10/87
Description: three explosions resulted when
incorrectly identified nitroglycerine/
lactose material introduced into incinerator.
(2) Date: 12/8/88
Description: drum caused strong reaction in
incinerator, which caused release of safety
pressure relief door and fuel line rupture,
caused by nitrocellulose incorrectly identified
as non-reactive ,
(3) Date: 3/24/91
Description: low water pressure caused
boiler tube to fail, causing the package boiler
to explode. The incinerator was burning
natural gas at the time of the explosion.
(4) Date: 4/25/93
Description: hydraulic hoses and oil, part of
drum repackaging system, caught fire
(5) Date: 1/14/95
Description: fire in Drum Repackaging
Building, caused by improperly mixed wastes;
off-site response agencies notified
(1) no environmental
releases or fires
(2) no information provided
(3) no off-site impact;
diesel/water spill was
contained
(4) no releases or injuries
(5) off-site: no releases
above reportable quantity
Volume vn
Appendix'
Ext/-
D<
Review Draft
,'ite or Quote
-------
TABLE 1
Hazardous Waste Combustor Facilities1
FacUity
TWI
Sauget, 1L
USDOE
Oak Ridge, TN
United States Pollution Control
Inc. (USPCI)
Clive, UT
Waste Reclamation and
Research
Eau Claire, WI
Waste Technologies Industries
East Liverpool, OH
Commercial
Incinerator?/
Capacity (tpy)2
Yes
RC(3): 50,000
No
Yes
RC(1): 359,160
Yes
PAIC: 2,500 (converted
from 624,000 gpy to tpy
assuming 8 Ib/gal)
RC(2): 3,500
Yes
PAIC & RC(3): 60,000
Years of
Operation3
15 +
(pre-81)
1
(Since 94)
15 +
(pre-81)
2
(Since 93)
Reported Incidents4
(1) mixing of
incompatible wastes
(2) operations;
explosion
(3) incinerator
operations; explosion
incinerator eqpt failure
NR
NR
NR, No major
incidents reported in
U.S. EPA (1995b).
Incident Date and Description
(1) Date: 1/16/90
Description: blending tank released plume of
196 Ibs of hydrochloric acid, due to improper
identification of corrosivity of waste being
added to tank
(2) Date: 1/26/91
Description: sodium azide incinerated: ash
placed in a dumpster; ash exploded a few
hours later
(3) Date: 2/5/91
Description: molten slag partly blocked exit
from incinerator during operation; slag
dislodged and fell into standing water below,
causing a steam explosion.
Date: 6/15/89
Description: induced draft fan for incinerator
failed; flying debris damaged stack
Reported
Impact
(1) no information provided
(2) no injuries or
environmental impacts
reported
(3) one worker injury;
vaporized hazardous waste
released; no environmental
impacts
no injuries; no detectable
off-site releases of toxic
material
Volume VII
Appendix VII-1
1-11
External Review Draft
Do Not Cite or Quote
-------
TABLE 1
Hazardous Waste Combustor Facilities1
FacUity
Commercial
Incinerator?/
Capacity (tpy)*
Years of
Operation3
Reported Incidents4
Incident Date and Description
Reported
Impact
Notes:
Sources:
• U.S. EPA 1995a. Report on Emergency Incidents at Hazardous Waste Incinerators and Commercial Treatment, Storage, and Disposal Facilities (TSDFs).
Draft. May.
• Victorine, G. U.S. EPA Region 5. 1995a. Facsimile memo to Staff Members in OSW and EPA Regions, with List of Commercial Hazardous Waste
Incinerators, Providing Years of Operation under RCRA Regulations.
• Victorine, G. U.S. EPA Region 5. 1995b. Facsimile memo to M. Mangino Providing Capacity Information on Selected Commercial Incinerators. July 27.
• The Hazardous Waste Consultant (HWC). 1995. Commercial Hazardous Waste Management Facilities: 1995 Survey of North America. Vol. 13, Issue 2,
March/April.
"Yes" signifies facility was identified as a commercial incinerator in Victorine (1995a).
Capacity Information (all capacities listed in tons per year (tpy)):
PAIC = permitted annual incineration capacity listed in HWC (1995).
Capacities from RCRIS. obtained from Victorine (1995b):
RC(1) = capacity per RCRIS in tpy, converted from tons/hr or Ib/hr
RC(2) = capacity per RCRIS in tpy, converted from gal/day or gal/hr assuming 1 gal=8 Ibs (based on 128 ounces per gallon/16 ounces per pound)
RC(3) = capacity per RCRIS in tpy, converted from MMBTU/hour based on note in Victorine (1995b) indicating that at one incinerator, 98 MMBTU/hr is
approximately equal to 60,000 tpy
Values of RC(2) and RC(3), converted from liquid or thermal capacities, are rounded to two significant figures to reflect uncertainty in conversion factors.
All calculations assume 24 hour/day operation.
Years of operation are from Victorine (1995a) unless otherwise noted.
NR - No incidents reported in U.S. EPA (1995a).
Incident related to waste handling or storage, not incineration.
Facility identified in HWC (1995); not listed in Victorine (1905a). Victorine (1995b) provides capacity information for rotary calciner and boiler.
This facility is identified as a "permitted DuPont commercial combustion facility" in U.S. EPA (1995a), but not listed as such elsewhere. According to Chip Crockett of
the Alabama Environmental Management Agency (telephone call, 7/13/95), this facility burns only hazardous waste generated on-site, and is not a commercial combustion
facility.
01-3999C:PCCOOAC3.W51
Volume vn
Appendix'
Extf
Di
Review Draft
lite or Quote
-------
TABLE 2
Summary of Incidents Reported at Treatment, Storage and Disposal Facilities1
Facility
Reported Incidents
Incident Date and Description
Reported
Impact
Albright and Wilson
Charleston, SC
(1) explosion and fire
(2) equipment failure
(1) Date: 6/17/91
Description: explosion and fire in Special Products Unit
(2) Date: 1/14/93
Description: rupture in steam jacket and piping released steam and by-
products
Note: Neither incident involved hazardous waste.
(1) nine deaths (apparently on-site),
fire .fighting water flowed to
containment pond
(2) no information
Carolina Solite, Norwood, NC
(1) equipment failure;
spill
(2) equipment failure;
spill
(1) Date: 11/4/93
Description: waste blend tank burst pipe, spilled 2,500 gal of waste;
most of spill contained; 50 to 100 gal escaped to soil; cleaned up
(2) Date: 1/94
Description: similar to 11/93
(1) soil contamination (remediated);
no human or environmental impacts
reported
Chemical Waste Management
(Commercial TSD)
Emelle, AL
(1) mixing waste; fire
(2) operations
(3) mixing waste; fire
(4) "ball of fire"
(5) flash fire
(1) Date: 11/10/92
Description: while oil was being added to drum of epichlorohydrin,
mixture ignited.
(2) Date: 12/5/92
Description: 170,000 gal water pumped from fire water tank to crusher
dispersion unit, found to be contaminated with D039 waste; ditch through
which water flowed had contaminated soil.
(3) Date: 12/8/92
Description: fire in vat of D004/D018 hazardous waste after addition of
Portland cement.
(4) Date: 1/9/93
Description: employee observed ball of fire rising above active trench,
followed by puff of smoke and another ball of fire.
(5) Date: 2/26/93
Description: flash-ignition of the reagent sulfur as it was mixed with
waste; lasted 1-2 seconds.
(1) no injuries
(2) soil contamination (remediated)
(3) no injuries, no releases
(4) no information
(5) no visible releases of hazardous
substances
Volume VII
Annendix VO-1
1-13
External Review Draft
Do Not Cite or Quote
-------
TABLE 2
Summary of Incidents Reported at Treatment, Storage and Disposal Facilities'
Facility
Chemical Waste Management
Arlington, OR
ChemPro
Tacoma, WA
Chem-Tech Systems
Los Angeles, CA
CP Chemicals
Sumter, SC
Delaware Container Company
Coatesville, PA
Fisher Industrial Services, Inc.
(Commercial TSD)
Glencoe, AL
Holnam/Safety-Kleen
Holly Hill, SC
International Paper
Joplin, MO
Reported Incidents
fire
operations; spill
bulk liquid handling
bulk liquid storage
mixing of incompatible
wastes
fire
(1) bulk liquid storage;
explosion
(2) transportation
transfer line failure
Incident Date and Description
Date: 5/5/94
Description: fire in landfill, believed to be due to disposing wood debris
near stabilized, heat-generating waste streams.
Date: ~ 87
Description: 10.000-eal spill of chromic acid through loose valve.
Date: 8/29/94
Description: release of nitrous oxide—acute emissions lasting 20 minutes
to 1 hour, during transfer of water with chrome into tank with mixed
acids.
Date: 11/29/85
Description: spill of 2,200-gal ammonia and 2.000-pal hydrochloric acid
from two storage tanks (tank valves left open by employees
[intentionally]).
Date: 10/14/85
Description: waste containing aluminum-based paint (not on manifest)
released "some gas"; residents detected odor; emergency personnel
called.
Date: 8/13/93
Description: small fire in roll-off, including various D- and F- listed
wastes; fire restricted to container.
(1) Date: 10/23/87
Description: 100,000-eal fuel tank exploded.
(2) Date: 8/13/92
Description: 638-gal spill during railcar transfer.
Date: 10/1/92
Description: water contaminated with wood-treating wastes released
during transfer from one closed surface impoundment to another; 30,000
gal released to the environment
Reported
Impact
no injuries; fire contained in landfill
soil contamination
two on-site employees complained of
dizziness and nausea; air emissions
dispersed by wind
no information provided
32 residents (or 100, per community)
treated for nose and throat irritations;
no hospitalizations or deaths
no information (fire restricted to
container)
(1) no information provided (not a
regulated unit)
(2) site remediated
no information on waste concentration
in water or result of release
Volume VII
Appendix /* \
Exter—i Review Draft
D<
ite or Quote
-------
TABLE 2
Summary of Incidents Reported at Treatment, Storage and Disposal Facilities1
Facility
Reported Incidents
Incident Date and Description
Reported
Impact
Laidlaw Environmental Services
(GSX Laidlaw Landfill)
Pinewood, SC
(1) operations; fire
(2) operations
(3) operations; fire
(4) fire
(5) waste mixing; fire
(1) Date: 1991
Description: fire at drum shredder unit.
(2) Date: 2/92
Description: spill at waste solidification unit.
(3) Date: 9/9/93
Description: fire at drum shredder unit, involving two drums of lithium
manganese batteries.
(4) Date: 4/12/94
Description: fire involving alkaline batteries.
(5) Date: unknown
Description: smoke and small pockets of flame from oil and grease
treatment tanks; later discovered load also contained caustic manure and
aluminum.
(1) no major release
(2) .soil contaminated (remediated)
(3) no injuries reported
(4) no injuries reported
(5) no information provided
Mill Service
Yukon, PA .
(1) operations
(2) bulk liquid
unloading
(1) Date: 11/12/91
Description: partially treated waste sludges accidentally placed in a
surface impoundment.
(2) Date: six times in last 10 years, none since '92
Description: nitric acid puffs occur from waste pickle liquor. This
occurs when the dome of a tank truck that was not cleaned out properly
is removed.
no information provided
Volume VII
AnnonHiv VII-1
External Review Draft
Do Not Cite or Quote
-------
TABLE 2
Summary of Incidents Reported at Treatment, Storage and Disposal Facilities1
Facility
Northwest Enviro Service
Seattle, WA
Oil and Solvent Process Company
Azusa, CA
Phillips Environmental (formerly
ChemPro)
Pier 91
Port of Seattle, WA
Rhone Poulenc Basic Chemical
Company
Martinez, CA
Safety-Kleen Lexington Recycling
Center
Lexington, SC
Reported Incidents
(1) operations; fire
(2) operations
(3) mixing waste
(4) spill
bulk liquid handling
operations
industrial operations;
fire; release
bulk liquid handling
Incident Date and Description
(1) Date: 1988
Description: welding sparks ignited fumes from below-grade pit, causing
fire.
(2) Date: 10/89
Description: during processine of oil wastes, workers from neighboring
building hospitalized, complaining about fugitive emissions.
(3) Date: 3/28/92
Description: heat, flames and toxic fumes generated due to mixing
incompatible wastes.
(4) Date: 2/14-15/94 '
Description: spill into storm drain of 5.500 eal of hazardous waste and
oil; migrated to river and wetland (company claimed sabotage).
Date: 4/21/89
Description: 9,6 11 -eal spill of wastewater containing 1.3% solvents
(mostly acetone) due to transfer line failure.
Date: 1990
Description: welders ignited fumes in an empty tank at tank farm/waste
oil facility.
Date: 7/23/92
Description: release of corrosive sulfonation acid sludge caused fire and
explosion; U.S. EPA criticized response actions and capabilities.
NOTE: This facility has never operated as a commercial TSDP under
RCRA. RCRA incinerator permit had been submitted at time of release,
but was withdrawn.
Date: 4/8/92. 6/19/92
Description: two spills (300 gal and 40 gal) while filling tanks.
substances unknown.
Reported
Impact
(1) no injuries or natural resource
damage
(2) hospitalized off-site workers
(3) no information
(4) contamination of site, wetlands,
and river
5 gallons onto public road; soil
contamination cleaned up; no threat
human health or environment
one worker killed; fugitive emissions
released
one Pacific Gas & Electric worker
seriously injured (apparently on-site)
due to contact with sludge; elevated
air concentrations of hydrogen sulfide
and sulfur dioxide in damaged area
no information provided
Volume VII
Appendix J
Exte-
DC
' Review Draft
iite or Quote
-------
TABLE 2
Summary of Incidents Reported at Treatment, Storage and Disposal Facilities1
Facility
Sol-Pro
Tacoma, WA
Southeastern Chemicals
Sumter, SC
Statewide Environmental Services
Los Angeles, CA
United States Pollution Control,
Inc. (USPCI)
Grassy Mountain Landfill, Tooele
County, UT
Washington Chemical
Reported Incidents
(1) operations;
explosion
(2) operations
fires
operations
spill
mixing of incompatible
wastes; explosion
Incident Date and Description
(1) Date: -1991
Description: welders working on a feed tank ignited fumes inside the
tank, resulting in explosion.
(2) Date: unknown
Description: fugitive emissions from solvent recyclers, evaporators, and
process vents containing acetone, toluene, and lacquer thinner, and from
a hopper for empty chemical drums; leaks from vats and containers.
Date: 4/12/92. 4/14/92. 4/20/92, 6/6/92
Description: four fires in 1992.
Date: 3/21/91
Description: solidified organic peroxides transferred into polyethylene
drum for incineration, resulting in unexpected reaction.
Date: 9/16/88
Description: 50 eal of unknown liquid hazardous waste spilled onto
ground from truck.
Date: 3/90 or 4/90
Description: incompatible wastes mixed together and sealed in a 55-gal
drum, causing explosion. Drum propelled through air, spraying waste in
all directions.
Reported
Impact
(1) no injuries; small fugitive
emission releases
(2) hazardous emissioas; releases to
surface water; no physical or health
problems
no major releases
release of water vapor and carbon
dioxide; on-site workers visited
hospital, released same day
no damage to liners, no ground water
contamination
no injuries; minor property damage
Notes:
1 Sources:
• U.S. EPA 1995a. Report on Emergency Incidents at Hazardous Waste Incinerators and Commercial Treatment, Storage, and Disposal Facilities (TSDFs).
Draft. May.
• Victorine, G. U.S. EPA Region 5. 1995. Facsimile memo to Staff Members in OSW and U.S. EPA Regions, with List of Commercial Hazardous Waste
Incinerators, Providing Years of Operation under RCRA Regulations.
Volume VII
Appendix VII-1
1-17
External Review Draft
Do Not Cite or Quote
-------
TABLES
Reported Equipment/Procedural Failures at the WTI Facility (Victorine 1995d)
Date
'05/27/93
09/15/93
11/02/93
12/10/93
12/14/93
12/15/93
12/15/93
12/16/93
12/22/93
12/23/93
12/27/93
Reported Equipment/Procedural Failures
Kiln brought down due to brick failure. Rebrick kiln.
More brick failure. Rebrick back half of kiln.
Spill of 10 gallons of high-BTU waste onto soil. All potentially
contaminated soil was removed.
Quench pump system failure results in ID fan trip while drums of
waste were still in the kiln; kiln reportedly released smoke for 3
minutes. (Apparently violation of RCRA permit condition requiring
negative pressure at all times.)
Tertiary ah- fan bearing failure: trial burn condition 2 rerun delayed
for repairs.
Scrubber pump cavitation reportedly causes unacceptable flow
variation; attributed to check valve failure: trial burn delayed while
adjustments made.
Tank lining failure due to poor adhesion. Unacceptably high flow
swings in the organic feed lance system result as the pieces of lining
flow through the pipes and out the lance. Also, minor problems
associated with spurious readings from a failed redundant
thermocouple (measuring kiln temperature).
Ball of slagged clay falls out of kiln and ruptures pressure relief
panels hi slag quench tank. Trial burn delayed for repairs. Failed
tank linings which caused problem on previous day are confirmed.
Trial burn stopped due to delays.
Automatic Waste Feed Cutoff (AWFCO) due to low voltage hi third
field of the Electrostatic Precipitator (ESP). Problem was due to "ash
bridge" hi the hopper. In cleaning out ash bridge, Permittee spilled
10 Ibs of ash (HW) onto concrete containment. Ash is cleaned up.
Malfunction of flyash handling system baghouse, 0.1 Ib of dust (HW)
is released.
Feed of drum into kiln with higher than expected BTU release rate
causes process oscillation and AWFCO for LOW TEMP. Also
results in process steam venting for several minutes.
Volume VII
Appendix VTI-1
1-18
External Review Draft
Do Not Cite or Quote
-------
TABLES
Reported Equipment/Procedural Failures at the WTI Facility (Victorine 1995d)
Date
12/28/93
12/29/93
01/09/94
01/10/94
01/11/94
01/14/94
01/14/94
01/17/94
01/17/94
01/18/94
01/19/94
Reported Equipment/Procedural Failures
Exceed Ohio Environmental Protection Agency (EPA) temporary
solids feed limit of 8000 Ib/hr for one hour by 98 Ibs. (Permittee
subsequently reported that drum weighing sequence was changed to
prevent this problem from occurring again.)
Chain conveyor which drags quenched slag out of the slag quench
tank breaks and falls into slag quench tank at 2:00 am. Facility burns
out waste for four hours, drams tank, shuts down kiln and makes
repairs.
C-water tank W5 overflows into containment while transferring C-
water from recycle tank W4 (which was temporarily being used for
C-water). No wastewater is released from containment.
Replace 5 rings of bricks on the discharge end of kiln.
More C-water overflows tank W5 into containment reportedly due to
a valve being partially stuck open. No wastewater is released from
containment.
AWFCO due to high flow after Hi-BTU lance pump failed; response
measures (viz., increasing feed through the organic liquids lance)
evidently were too aggressive. Exceeded 65,000 standard cubic feet
per minute (scfm) permit limit. Not burning any solids at the time.
One of three drums of the same waste was opened for sampling and
began smoking. Fumes were caught by the vapor recovery system,
while fire extinguisher was directed on drum and the drum resealed.
No significant releases.
Neutralization pump to spray dryer head tank leaks and spills spray
dryer feed water onto concrete containment. No releases to
environment.
Steam (not HW) release due to frozen pressure transmitters in steam
loop.
Spilled 3-5 pounds of lime (not HW) onto concrete area after the lime
screw unit which feeds tank Nl is repaired and returned to service.
Initial report was that a gasket was evidently not correctly tightened
after the lime screw unit was repaired.
Leak in condenser due to cold weather necessitates more than normal
venting of steam (not HW).
Volume VII
Appendix VII-1
1-19
External Review Draft
Do Not Cite or Quote
-------
TABLE 3
Reported Equipment/Procedural Failures at the WTI Facility (Victorine 1995d)
Date
Reported Equipment/Procedural Failures
01/22/94
Damage caused by cold weather reportedly caused some of the steam
coils in the flue gas reheat system to rupture, causing high opacity
readings. Facility brought off waste and down onto natural gas (for 2
days) while repairs were made. Welding on heat exchanger results in
observations of smoke for several hours near the stack..
01/24/94'
Failed check valve causes "C" water to backflow into a sump below
the process water storage tanks. Valve is isolated and replaced; no
release to the environment.
01/28/94
3 second positive pressure excursion in secondary combustion
chamber (SCC) results in AWFCO. The pressure excursion is
reportedly due to slag falling of the wall of the SCC and into the slag
quench tank, resulting hi a large amount of steam being generated
and released into the SCC.
01/31/94
Corrosion of an "air bell" inside the ESP causes air bell to fall and
short out the first field of the ESP. This shuts down the first ESP
field and triggers an AWFCO. Since.fields 2 and 3 remained
operative as the facility came off waste, it is believed that only a
minor increase hi emissions would have been experienced for a very
short time, with emissions remaining within allowable limits.
Quarterly ECIS performance test scheduled to start on 2/1 has to be
postponed until 2/15.
2/14/94
One atomizer hi the spray dryer plugs up or malfunctions, so service
water is fed to spray dryer to maintain proper attemperation.
However, since there was insufficient blowdown from the scrubber
(the scrubber is normally blown down to the spray dryer through the
atomizers, and blowdown evidently had to be reduced since the spray
dryer couldn't handle it all), SO2 removal in the scrubber evidently
decreased and resulted in an SO2 exceedance. Between 2013 and
2119 hours, the facility emitted up to 15.9 pounds per hour of SO2;
OEPA air permit limit is 11.3 pounds per hour.
02/15/94
ID fan trips due to mistake made while electrical work is being done
on control system. No drums/bulk waste hi the kiln.
02/16/94
AWFCO due to high carbon monoxide caused by plugging in high-
BTU lance. Evidently, plugging caused "spurting" flow which led to
less complete combustion than does smooth flow.
Volume VII
Appendix VII-1
1-20
External Review Draft
Do Not Cite or Quote
-------
TABLE 3
Reported Equipment/Procedural Failures at the WTI Facility (Victorine 1995d)
Date
02/23/94
. 02/25/94
03/03/94
03/08/94
03/12/94
03/26/94
04/06/94
04/16/94
04/26/94
05/10/94
Reported Equipment/Procedural Failures
Same as 02/16; delays start of trial burn test. No drums or bulk
waste in the kiln. Attributed to specific conditions of the trial burn.
Same as 02/16; trips incinerator 10 minutes before the 4-hour test run
is complete per the trial burn plan. No drums or bulk waste in the
kiln. Attributed to specific conditions of the trial burn.
Spill of 5-8 gallons of acidic/solvent sludge when rupture disk blows
hi tank PT-3, due to level alarm failure and related overfilling.
Waste is contained in secondary containment, but apparently gets
pumped from sump into C-water system, contaminating C-water.
Power fluctuations caused problems for variable drives on spray dryer
atomizers, atomizers trip off, system has AWFCO at 6:00 am due to
high temperature at the outlet of the spray dryer. System is checked
out and returned to service, but has a similar AWFCO around 8:00
am due to failure of spray dryer atomizer vacuum pump which, under
present logic, automatically tips off the atomizer.
Rebrick kiln.
Spill of 15-18 gallons of HW into secondary containment in the drum
pumpout tank area. Due to apparent failure of maintenance personnel
to reconnect a vent line on a sludge pump after a service operation.
HW cleaned up and put in drums.
Spill of < 5 gallons of waste into and just outside of secondary
containment for the pumpout tanks. Workers were disconnecting
hoses used for temporary waste routing, hoses were evidently under
more pressure than anticipated. All spillage was onto pavement, and
was cleaned up.
Problems with slag conveyor, plant is brought down for three days
for repairs.
While repackaging reactive wastes from drums into 5-gallon pails,
three pails start liberating strong tar-like odor. Pails were
immediately sent to the kiln and were destroyed, all within 20
minutes. Waste was cumene hydroperoxide.
Large piece of slag rolled out of the kiln and into the slag quench
tank, causing pressure relief panels hi the quench tank to release.
Plant brought down for repairs, plans are made to modify the design
of the slag quench tank and conveyor system.
Volume VII
Appendix VII-1
1-21
External Review Draft
Do Not Cite or Quote
-------
TABLES
Reported Equipment/Procedural Failures at the WTI Facility (Victorine 1995d)
Date
05/14/94
06/08/94
06/15/94
07/12/94
07/28/94
08/19/94
08/25/94
09/01/94
09/29/94
10/23/94
10/31/94
11/04/94
12/08/94
Reported Equipment/Procedural Failures
Slag conveyor jammed, came off track, and fell into the slag quench
tank. Plant brought down for repairs. Upon re-start on Sunday
morning, ESP field #3 was found to be shorting out. Plant brought
back down so that ceramic insulators on ESP field #3 could be
changed. Plan to be back on waste 5/17.
Problems with slag quench tank and conveyor.
Shut down to inspect brickwork in kiln, need to replace several rows
of bricks.
Unit down for repairs to slag conveyor.
Unit down for rebricking of kiln and repairs to slag conveyor.
Unit down for repairs to slag conveyor.
Problem with large piece of slag falling into quench tank causes SCC
overpressure and visible puff for 3-5 seconds.
During monitor recertification, CO monitors are found to be reading
high and hence out of certification. Even though this could be
considered to be "overprotective, " facility is instructed not to burn
waste until at least one monitor can be certified. WTI goes down for
about two weeks to install new slag quench tank, and also decides to
lease a new CO monitor, while also ordering two brand-new CO
units. Temporary CO monitor is successfully certified, and facility
operates on this monitor until new units arrive.
Unit down until 10/24/94 due to problems with spray dryer pump(s)
and sensor(s).
Unit down (reason not recorded) until 10/25/94
Electrical technician causes fuse to blow while changing an indicator
lamp for the water level in the waste heat boiler. The process
computer interprets this as meaning that the boiler has gone dry, and
responds by tripping the plant off. Hot gases remaining in the kiln
evidently flow backward through the vapor recovery system piping
and out the three carbon absorber boxes associated with the vapor
recovery system. Event lasts approximately 10 minutes, with some
visible emissions reportedly seen at ground level.
Plant down for minor brick repairs.
Leaking piping at scrubber water pump inside scrubber building.
Volume VII
Appendix VII-1
1-22
External Review Draft
Do Not Cite or Quote
-------
TABLES
Reported Equipment/Procedural Failures at the WTI Facility (Victorine 1995d)
Date
Reported Equipment/Procedural Failures
12/29/94
Rolled up cloth-like item in bulk waste feed got caught in hot-side
doors of bulk feed chute, and began smoldering. Technicians
reportedly used a hose to extinguish the item and knock it free.
01/04/95
Steam release due to frozen condensate line at heat exchanger.
Corrective action included revision to control system to send
information concerning temperature and valve position up to the
control room.
01/08/95
Unit down for partial rebricking.
02/14/95
Small electrical fire in a control cabinet within the spray dryer
penthouse, immediately extinguished by plant personnel with fire
extinguisher. The spray dryer is controlled both electrically and
hydraulically, and some of the hydraulic piping which runs through
the cabinet ruptured and spilled into penthouse, onto floor grating,
and through grating onto insulation. Oil is steam-cleaned off the
following evening.
02/15/95
When upper doors were opened to drop a load of bulk solids into the
kiln, the bulk waste which was in the clamshell caught fire.
Sprinkler system activated, extinguishing fire reportedly within 1
minute. This event was reportedly caused by a "flashback" of
powdery material falling out of clamshell bucket. Damage was
reportedly limited to the crane bucket wires, cables, and insulation in
the immediate area.
3/15/95
Release of a repulsive odor, affecting much of East Liverpool, due to
the receipt and unloading of a tanker of waste which contained the
mercaptan thiophenol. No exact release point was ever identified
with certainty, but reportedly only a few drops of this waste (which
reportedly has an odor threshold of 0.3 ppb) could result in this kind
of problem. The possibility exists mat this odor was at least in part
due to releases from the truck after it left the plant site. WTI stopped
receiving shipments of this waste until it completed enclosure of the
tanker truck unloading pad and venting of this enclosure to the vapor
recovery system.
Volume VII
Appendix VTI-1
1-23
External Review Draft
Do Not Cite or Quote
-------
TABLES
Reported Equipment/Procedural FaUures at the WTI Facility (Victorine 1995d)
Date
Reported Equipment/Procedural Failures
7/03/95
The waste in one of the two enclosed bulk solid waste pits caught
fire. Fire was quickly extinguished by the automatic water deluge
system. No injuries; minor damage to the door into the pit. Since
this enclosure is vented to the vapor recovery system, no significant
releases were suspected, but some smoke was reported as leaking out
from under and around the door. Ignition source is attributed to a
burning piece of waste, either travelling through the ah" from the
incinerator feed chute doors to the pit, or being carried from the
chute doors to the pit via the clamshell bucket.
7/18/95
An incoming truck load of caustic waste was mistaken for an
expected shipment of virgin caustic from the same trucking company,
and therefore the truck driver was mistakenly directed by facility
personnel to off-load the material into the caustic tank (this caustic
tank is used for neutralization of the scrubber liquor). The mistake
was immediately caught, and all the material (mixture of waste and
virgin caustic) in the caustic tank was subsequently treated as a
hazardous waste. WTI cleaned out the tank and instituted additional
verification procedures for bill-of-lading.
Volume VII
Appendix VII-1
1-24
External Review Draft
Do Not Cite or Quote
-------
APPENDIX VH-2
Ranking of Chemicals of
Potential Concern
-------
TABLE 1
Chemicals Eliminated from the Preliminary List*
CAS Number
591-08-2
98-86-2
53-96-3
591-08-2
111-65-9
131-74-8
7803-55-6
7778-39-4
692-42-2
696-28-6
151-56-4
75-55-8
542-62-1
100-01-6
10647-8
100-21-0
51-43-4
122-09-8
92-87-5
50-32-8
81-81-2
50-32-8
7440-41-7
598-31-2
357-57-3
39196-18-4
111-76-2
123-86-4
592-01-8
Substance
Acetamide, N-(aminothioxomethyl)-
Acetophenone
Acetylaminofluorene, 2-
1 -Acetyl-2-thiourea
Aliphatic hydrocarbons (assumed octane)
Ammonium picrate
Ammonium vanadate
Arsenic acid H3AsO4
Arsine, diethyl-
Arsonous dichloride, phenyl-
Aziridine
Aziridine, 2-methyl-
Barium cyanide
Benzenamine, 4-nitro-
Benzenamine, 4-chloro-
Benzenedicarboxylic acid, 1,2-
1 ,2-Benzenediol, 4-[l-hydroxy-2-(methylamino)ethyl]-
Benzeneethanamine, a,a-dimethyl-
Benzidine
Benzo(a)pyrene
2H-l-Benzopyran-2-one, 4-hydroxy-3-(3-oxo-l-phenylbutyl)-, & salts, when present at concentrations
greater than 0.3%
Benzoquinone, p-
Beryllium
Bromoacetone
Brucine
2-Butanone, 3,3-dimethyl-l-(methylthio)-,O-[methylaminocarbonyl] oxime
Butoxyethanol, 2- (Butyl cellosolve)
Butyl acetate
Calcium cyanide
Volume VII
Appendix VII-2
1-1
External Review Dra:
Do Not Cite or Quot
-------
CAS Number
75-44-5
107-20-0
106-47-8
108-90-7
218-01-9
544-92-3
106-44-5
108-39-4
460-19-5
131-89-5
53-70-3
106-93-4
1649-08-7
75-71-8
75-34-3
540-59-0
75-35-4
542-88-1
60-57-1
56-53-1
311-45-5
692-42-2
309-00-2
465-73-6
60-57-1
72-20-8
124-40-3
Substance "~
Carbonic dichloride
Chloroacetaldehyde
p-Chloroaniline
Chlorobenzene
Chrysene
Copper cyanide
Cresol, 4-
Cresol, 3-
Cyanides (soluble cyanide salts), not otherwise specified
Cyanogen
2-Cyclohexyl-4, 6-dinitrophenol
Dibenz(a,h)anthracene
Dibromoethane
Dichlorodifluoroethane ^
Dichlorodifluoromethane x-
Dichloroethane, 1,1- (ethylidene dichloride)
Dichloroethene
Dichloroethene, 1,1-
Dichloromethyl
Dieldrin
Diethyl stilbestrol
Diethyl-p-nitrophenyl phosphate
Diethylarsine
1,4,5, 8-Dimethanonaphthalene, 1,2,3,4, 10, 10-hexa- chloro-l,4,4a,5,8,8a,-hexahydro-,
(la,4a,4a/3,5o:,8a,8a/3)-
1,4,5, 8-Dimethanonaphthalene, 1, 2,3,4, 10, 10-hexa- chloro-l,4,4a,5,8,8a,-hexahydro-,
(la,4a,4aj8,5/3,8/3,8a/3)-
2,7:3,6-Dimethanonaphth [2,3-b]oxirene, 3,4,5,6,9,9-hexachloro-la,2,2a,3,6,6a,7,7a-octahydro-,
(laa,2j8,2aa,3|8,6/8, 6aa,7/3,7aa)-
2,7:3,6-Dimethanonaphth [2,3-b]oxirene, 3,4,5,6,9,9-hexachloro-la,2,2a,3,6,6a,7,7a-octahydro-,
(lao:,2/3,2a/3,3a,6a:, 6a/3,7/3,7aa)-, & metabolites ,/—
Dimethylamine
Volume VII
Appendix VII-2
1-2
External Review Draft
Do Not Cite or Quote
-------
TABLE 1
Chemicals Eliminated from the Preliminary List'
CAS Number
119r93-7
105-67-9
131-11-3
122-09-8
51-28-5
121-14-2
606-20-2
145-73-3
51-43-4
460-19-5
107-12-0
141-78-6
51-79-6
105-39-5
52-85-7
206-44-0
62-74-8
64-18-6
28-86-4
98-01-1
76-44-8
110-43-0
57-58-4
110-54-3
142-92-7
60-34-4
7803-51-2
193-39-5
78-59-1
67-63-0
Substance
Dimethylbenzidine, 3,3'-
Dimethylphenol (assumed 2,4-)
Dimethylphthalate
a,a-Dimethyphenethylamine
2 ,4-Dinitrophenol
Dinitrotoluene, 2,4-
Dinitrotoluene, 2,6-
Endothall
Epinephrine
Ethanedinitrile
Ethyl cyanide
Ethyl acetate
Ethyl carbamate
Ethylchloroacetate
Famphur
Fluoranthene
Fluoroacetic acid, sodium salt
Formic acid
Fulminic acid, mercury (2+) salt
Furfural
Heptachlor
Heptanone, 2-
Hexaediyl tetraphosphate
Hexane
Hexyl acetate
Hydrazine, methyl-
Hydrogen phosphide
Indeno(l,2,3-cd)pyrene
Isophorone
Isopropanol
Volume VII
Appendix VII-2
1-3
External Review Draft
Do Not Cite or Quote
-------
CAS Number
108-21-4
120-58-1
2763-96-4
108-31-6
628-86-4
509-14-8
542-88-1
75-70-7
76-44-8
115-29-7
16752-77-5
80-62-6
504-60-9
36-49-5
75-09-2
1116-54-7
55-18-5
924-16-3
930-55-2
4549-40-0
134-32-7
91-59-8
557-19-7
100-01-6
55-63-0
100-02-7
152-16-9
145-73-3
109-66-0
131-74-8
TABLE 1 / -J
Chemicals Eliminated from the Preluninary List"
Substance
Isopropyl acetate
Isosafrole
3(2H)-Isoxazolone, 5-(aminomethyl>
Maleic anhydride
Mercury fulminate
Methane, tetranitro-
Methane, oxybis[chloro-
Metiianethiol, trichloro-
4,7-Methano-lH-indene, 1,4,5,6,7, 8,8-heptachloro-3a,4,7,7a-tetrahydro-
6,9-Methano-2,4,3-benzodioxathiepin, 6,7,8,9,10,10-hexachloro-l,5,5a,6,9,9a-hexahydro-, 3-oxide
Methomyl
Methyl methacrylate
Methylbutadiene, 1-
Methylcholanthrene, 3- ^
Methylene chloride
N-nitrosodiethanolamine
N-nitrosodiethylamine
N-nitrosodi-n-butylamhie
N-nitrosopyrolidine
N-nitrosomethylvinylamine
Naphthylamine, 1-
Naphthylamine, 2-
Nickel cyanide
p-Nitroaniline
Nitroglycerine
Nitrophenol (para)
Octamethylpyrophosphoramide
7-Oxabicyclo[2.2. l]heptane-2,3-dicarboxylic acid
Pentane
/
Phenol, 2,4,6-trinitro-, ammonium salt
Volume VII
Appendix VH-2
1-4
External Review Draft
Do Not Cite or Quote
-------
TABLE 1
Chemicals Eliminated from the Preliminary List*
CAS Number
131-89-5
534-52-1
51-28-5
88-85-7
311-45-5
298-02-2
298-04-4
60-51-5
55-91-4
297-97-2
298-00-0
52-85-7
56-38-2
85-44-9
109-06-8
116-06-3
542-76-7
75-86-5
55-63-0
71-23-8
598-31-2
107-19-7
107-18-6
107-02-8
107-19-7
504-24-5
154-11-5
108-46-3
12039-52-0
630-10-4
Substance
Phenol, 2-cyclohexyl-4,6-dinitro-
Phenol, 2-methyl-4,6-dinitro-, & salts
Phenol, 2,4-dinitro-
Phenol , 2-( 1 -methylpropyl)-4 , 6-dinitro-
Phosphoric acid, diethyl 4-nitrophenyl ester
Phosphorodithioic acid, O, O-diethyl S-[(ethylthio)methyl] ester
Phosphorodithioic acid, O, O-diethyl S-[2-(ethylthio)ethyl] ester
Phosphorodithioic acid, O, O-dimethyl S-[2-(methylamino)-2-oxoethyl] ester
Phosphorofluoridic acid, bis(l-methylethyl) ester
Phosphorothioic acid, O,O-diethyl O-pyrazinyl ester
Phosphorothioic acid, O,O,-dimethyl O-(4-nitrophenyl) ester
Phosphorothioic acid, O-[4-[(dimethylamino)sulfonyl]phenyl] O,O-dimethyl ester
Phosphorothioic acid, O,O-diethyl O-(4-nitrophenyl) ester
Phthalic anhydride
Picoline, 2-
Propanal, 2-methyl-2-(methylthio)-, O-[(methylamino)carbonyl]oxime
Propanenitrile, 3-chloro-
Propanenitrile, 2-hydroxy-2-methyl-
1,2,3-Propanetriol, trinitrate
Propanol, n-
2-Propanone, 1-bromo-
Propargyl alcohol
2-Propen-l-ol
2-Propenal
2-Propyn-l-ol
4-Pyridhiamine
Pyridhie, 3-(l-methyl-2-pyrrolidhiyl)-, (S)-, & salts
Resorcinol
Selenious acid, dithallium(l+) salt
Selenourea
Volume VH
Appendix VII-2
1-5
External Review Oral
Do Not Cite or Quot
-------
TABLE 1 ^ 4
Chemicals Eliminated from the Preliminary List"
CAS Number
506-64-9
357-57-3
630-20-6
79-34-5
107-49-3
757-58-4
12039-52-0
7446-18-6
541-53-7
103-85-5
86-88-4
823-40-5
95-80-7
76-13-1
120-82-1
79-00-5
75-69-4
87-90-1
75-70-7
121-44-8
7803-55-6
4549-40-0
557-21-1
Substance
Silver cyanide
Strychnidin- 10-one, 2,3-dimethoxy-
Tetrachloroethane, 1,1,1,2-
Tetrachloroethahe, 1,1,2,2-
Tetraethyl pyrophosphate
Tetraphosphoric acid, hexaethyl ester
Thallium(l) selenite
Thallium(l) sulfate
Thioimidodicarbonic diamide [(H2N)C(S)]2NH
Thiourea, phenyl-
Thiourea, 1-naphthalenyl-
Toluenediamine, 2,6-
Toluenediamine, 2,4-
Trichloro-l,2,2,-trifluoroethane, 1,1,2- /"" *
Trichlorobenzene (assumed 1,2,4-)
Trichloroethane, 1,1,2-
Trichlorofluoromethane
Trichloroisocyanuric acid (Symclosene)
Trichloromethanethiol
Triethylamhie
Vanadic acid, ammonium salt
Vinylamine, N-methyl-N-nitroso-
Zinc cyanide
Note:
a 170 chemicals were eliminated from the preliminary list of 309 chemicals.
Volume VII
Appendix VII-2
1-6
External Review Draft
Do Not Cite or Quote
-------
TABLE 2
Ranking of Chemicals of Potential Concern for Short-Term Exposures*
CAS
Number1
107-20-0
640-19-7
62-74-8
67-64-1
107-2-8
107-13-1
116-6-3
309-0-2
107-18-6
20859-73-8
2763-96-4
504-24-5
7664^1-7
62-53-3
506-61-6
1327-53-3
1303-28-2
7784-34-1
7784-42-1
7M3-2
108-98-5
100-44-7
71-36-3
75-15-0
56-23-5
57-74-9
7782-50-5
Substance
Acetaldehyde, chloro-
Acetamide, 2-fluoro-
Acetic acid, fluoro-, sodium salt
Acetone
Acrolein
Acrylonitrile
Aldicarb
Aldrin
Ally! alcohol
Aluminum phosphide
Aminomethyl-3-isoxazolol, 5-
Aminopyridine, 4-
Ammonia
Aniline
Argentate(l), bis(cyano-C)-, potassium
Arsenic oxide
Arsenic pentoxide
Arsenous trichloride
Arsine
Benzene
Benzenethiol
Benzyl chloride
Butanol
Carbon disulfide
Carbon tetrachloride
Chlordane
Chlorine
Basis2
B
B
B
A
B, C, D
A, C, D
B, D
B, D
B,C, D
B, D
B
B
C
A, D
B
B
B, D
C
C
A
B
B, D
A
A, B, C, D
A
D
C
R, Rank3
(IDLH)
80
61
4
130
10
83
6
37
57
86
81
87
92
99
88
27
66
24
20
112
28
59
124
111
109
101
40
R, Rank3
(IDLH,
VP)
29
NS
NS
47
13
31
93
97
32
NS
NS
100
15
77
NS
NS
NS
28
3
44
39
35
79
36
41
108
6
R3 Rank3
(IDLH,
VP, C)
NS
NS
NS
9
NS
6
NS
NS
NS
NS
NS
NS
NS
37
NS
NS
NS
NS
NS
15
NS
NS
34
5
7
47
NS
Volume VII
Appendix VII-2
2-1
External Review Draft
Do Not Cite or Quote
-------
TABLE 2
Ranking of Chemicals of Potential Concern for Short-Term Exposures*
CAS
Number1
10049-4-4
67-66-3
542-88-1
5344-82-1
542-76-7
8001-58-9
95-48-7
4170-30-3
98-82-8
506-77-4
110-82-7
108-94-1
19287-45-7
95-50-1
541-73-1
106-46-7
696-28-6
84-66-2
297-97-2
55-91-4
60-51-5
540-73-8
77-78-1
534-52-1
88-85-7
123-91-1
152-16-9
Substance
Chlorine dioxide
Chloroform
bis-Chloromethyl ether
1 -(o-Chlorophenyl)thiourea
Chloropropionitrile, 3-
Creosote (coal tar) .
Cresol, 2-
Crotonaldehyde
Cumene
Cyanogen chloride
Cyclohexane
Cyclohexanone
Diborane
Dichlorobenzene, 1,2-
Dichlorobenzene, 1,3-
Dichlorobenzene, 1,4-
Dichlorophenylarsine
Diethylphthalate
Diethyl O-pyrazinyl phosphorothioate, O,O-
Diisopropylfluorophosphate (DFP)
Dimethoate
Dimethylhydrazine
Dimethyl sulfate
Dinitro-o-cresol, 4,6- & salts (2)
Dinoseb
Dioxane, 1,4-
Diphosphoramide, octamethyl-
Basis2
c
A, C, D
C
B
B
A
A, D
A, C, D
A
B,C
A
A
C
A
A
A
B
A
B
B
B, D
A, C, D
A, D
B, D
B, D
A
B, D
R, Rank3
(IDLH)
25
117
5
55
68
NS
106
79
125
122
126
118
30
107
NS
102
100
NS
44
46
97
48
47
11
54
113
15
R2Rank3
(IDLH,
VP)
11
42
18
NS
43
NS
85
40
74
33
51
75
2
81
NS
78
87
NS
89
53
107
24
57
90
76
52
88
R, Rank3
(IDLH,
VP, C)
NS
10
NS
NS
NS
NS
41
13
36
NS
20
33
NS
35
NS
40
NS
NS
NS
NS
NS
4
29
NS
NS
22
NS
y
A
\vu
jvn-2
External Rr
Do Not C,
"Iraft
,iote
-------
TABLE 2
Ranking of Chemicals of Potential Concern for Short-Term Exposures"
CAS
Number1
107-49-3
298-4-4
541-53-7
115-29-7
72-20-8
106-89-8
16752-77-5
64-17-5
110-80-5
140-88-5
100-41-4
151-56-4
82-41-4
640-19-7
50-0-0
142-82-5
302-1-2
79-19-6
74-90-8
7647-1-0
7664-39-3
7783-7-5
7783-6-4
13463-40-6
78-83-1
465-73-6
62-38-4
Substance
Diphosphoric acid, tetraethyl ester
Disulfoton
Dithiobiuiet
Endosulfan
Endrin, & metabolites
Epichlorohydrin
Ethanimidothioic acid, N-[[(raethylamino)carbonyl]oxy]-, methyl ester (Methomyl)
Ethanol
Ethoxyethanol, 2-
Ethyl acrylate
Ethylbenzene
Ethyleneimine
Fluorine
Fluoroacetamide
Fonnaldehyde
Heptane
Hydrazine
Hydrazinecarbothioamide
Hydrocyanic acid
Hydrogen chloride
Hydrogen fluoride
Hydrogen selenide
Hydrogen sulfide
Iron, pentacarbonyl-
Isobutanol
Isodrin
Mercury, (acetato-O)phenyl-
Basis2
B
B, D
B,D
B, D
B, D
A, C, D
B
A
A
A
A
B, C, D
B, C,D
B, D
A, C, D
A
A, C, D
B
B, C,D
C
C
C
C
C
A
B, D
B
R, Rank3
(IDLH)
12
32
58
16
3
96
72
131
114
108
121
82
52
NS
35
119
62
69
60
65
36
8
78
17
127
64
93
R2Rank3
(IDLH,
VP)
92
95
NS
102
101
45
104
65
70
49
71
27
23
NS
7
59
37
NS
20
4
14
1
9
22
73
105
103 .
R3 Rank3
(IDLH,
VP, C)
NS
NS
NS
NS
46
17
NS
25
30
28
31
NS
NS
NS
2
21
11
NS
NS
1
3
NS
NS
NS
32
NS
NS
Volume VII
External Review Draft
Do Not Cite or Quote
-------
TABLE 2
Ranking of Chemicals of Potential Concern for Short-Term Exposures"
CAS
Number1
62-75-9
67-56-1
78-93-3
60-34-4
108-10-1
624-83-9
75-86-5
298-0-0
91-20-3
86-88-4
13463-39-3
54-11-5
98-95-3
10102-44-0
10102-43-9
79-46-9
62-75-9
20816-12-0
56-38-2
108-95-2
62-38-4
103-85-5
298-2-2
75-44-5
7806-51-2
151-50-8
506-61-6
Substance
Methanamine, N-methyl-N-nitroso-
Methanol
Methyl ethyl ketone (2-Butanone)
Methyl hydrazine
Methyl isobutyl ketone (2-Methyl-4-pentanone)
Methyl isocyanate
Methylactronitrile, 2-
Methyl parathion
Naphthalene
Naphthylthiourea, alpha-
Nickel carbonyl
Nicotine, & salts (2)
Nitrobenzene
Nitrogen dioxide
Nitrogen oxide NO
Nitropropane, 2-
N-nitrosodimethylamine
Osmium oxide OsO4, (T-4)-
Parathion
Phenol
Phenylmercury acetate
Phenylthiourea
Phorate
Phosgene
Phosphine
Potassium cyanide
Potassium silver cyanide
Basis2
B
A
A
B, C, D
A
B, C, D
B
B
A
B
B,C, D
B, D
A, D
B, D
B, C, D
A
B, D
B
B, D
A, D
B, D
B,D
B,D
B, C,D
B, C, D
B, D
B, D
RtRank3
(IDLH)
84
132
133
50
116
14
75
9
110
73
26
13
104
51
77
98
85
1
21
103
94
41
2
18
63
38
89
RjRank3
(IDLH,
VP)
55
60
63
25
64
12
66
98
91
NS
16
54
86
17
5
46
56
21
96
84
106
NS
82
8
NS
NS
NS
R3 Rank3
(IDLH,
VP,C)
NS
19
16
NS
26
NS
NS
NS
45
NS
NS
NS
39
NS
NS
8
NS
NS
NS
42
NS
NS
NS
NS
NS
NS
NS
J
VII
jvn-2
External Re-
Do Not Ci
e
-------
TABLE 2
Ranking of Chemicals of Potential Concern for Short-Term Exposures9
CAS
Number1
107-12-0
75-55-8
110-86-1
26628-22-8
143-33-9
57-24-9
7783-60-0
7446-11-9
7446-18-6
95-94-3
127-18-4
3689-24-5
78-0-2
109-99-9
509-14-8
1314-32-5
39196-18-4
108-98-5
79-19-6
5344-82-1
7550-45-0
108-88-3
584-84-9
91-8-7
8001-35-2
71-55-6
79-1-6
Substance
Propanenitrile
Propylenimine, 1,2-
Pyridine
Sodium azide
Sodium cyanide
Strychnidin- 10-one, & salts (2)
Sulfur tetrafluoride
Sulfur trioxide
Sulfuric acid, dithallium (1+) salt
Tetrachlorobenzene (assumed 1,2,4,5-)
Tetrachloroethylene
Tetraethyldithiopyrophosphate
Tetraethyl lead
Tetrahydrofuran
Tetranitromethane
Thallic oxide
Thiofanox
Thiophenol
Thiosemicarbazide
Thiourea, (2-chlorophenyl)-
Titanium tetrachlofide
Toluene
Toluene-2,4-diisocyanate
Toluene-2,6-diisocyanate
Toxaphene
Trichloroethane, 1,1,1-
Trichloroethylene
Basis2
B, C
B, C, D
A '
B, D
B; D
B, D
C
C
B
A
A
B
B, D
A
B, C, D
B
B, D
B, D
B, D
B,D
C
A
A, C, D
A, C, D
B
A
A
R! Rank3
(IDLH)
49
95
120
90
39
7
70
42
33
NS
105
22
53
129
43
34
67
29
71
56
23
115
31
19
91
123
128
R2Rank3
(IDLH,
VP)
26
30
68
NS
NS
NS
10
19
NS
NS
58
94
67
50
34
NS
99
38
NS
NS
NS
61
83
69
72
48
62
R3 Rank3
(IDLH,
VP,C)
NS
NS
27
NS
NS
NS
NS
NS
NS
NS
24
NS
NS
14
NS
NS
NS
NS
NS
NS
NS
18
43
38
44
12
23
Volume VII
Appendix VII-2
2-5
External Review Draft
Do Not Cite or Quote
-------
TABLE 2
Ranking of Chemicals of Potential Concern for Short-Term Exposures"
CAS
Number1
1314-62-1
1330-20-7
81-81-2
1314-84-7
Substance
Vanadium oxide
Xylene
Warfarin, & salts, when > 0.3% (2)
Zinc phosphide, when > 10%
Basis2
B, D
A
B, D
B, D
R, Rank3
(IDLH)
45
NS
74
76
RjRank3
(IDLH,
VP)
NS
NS
80
NS
R3 Rank3
(IDLH,
VP, C)
NS
NS
NS
NS
Notes:
* 139 chemicals were selected for further analysis.
1 CAS Number given for parent compound only.
1 A — Wastes received by WTI during first year of operation
B — Constituents listed as "P" wastes (acutely hazardous according to RCRA)
C — Acutely toxic chemicals identified in CAA 112(r)
D — Extremely hazardous substances from EPCRA
3 NS — IDLH, vapor pressure, or concentration data not available for this compound. Therefore, no score calculated.
01-3999C:PCCOOAC3.W51
Vo1 -^ VII
A 1VH-2
j
External Rev'
Do Not Ci
•Sraft
,ote
-------
APPENDIX VH-3
Accidental Release Modeling
-------
CONTENTS
I. RELEASE CHARACTERIZATION
A. Methodology
B. Chemical-Specific Release Rate Calculations
1. On-Site Spill
2. On-Site Fire
3. On-Site Mixing of Incompatible Wastes
4. Off-Site Tanker Truck Spill
5. Off-Site Tanker Truck Spill with Fire
C. Results of the Release Modeling
1. On-Site Spill
2. On-Site Fire
3. On-Site Mixing of Incompatible Wastes
4. Off-Site Tanker Truck Spill
5. Off-Site Tanker Truck Spill with Fire
H. REFERENCES
Page
1
1
4
4
10
14
15
16
16
17
22
24
25
26
42
TABLES
TABLE 1: Accident Analysis Calculations -
Scenario 1: On-Site Spill (conservative)
TABLE 2: Accident Analysis Calculations -
Scenario 1: On-Site Spill (typical)
TABLE 3: Accident Analysis Calculations -
Scenario 2: On-Site Fire (conservative)
TABLE 4: Accident Analysis Calculations -
Scenario 2: On-Site Fire (typical)
TABLE 5: Accident Analysis Calculations -
Scenario 3: On-Site Mixing of Incompatible Wastes (conservative)
TABLE 6: Accident Analysis Calculations -
Scenario 3: On-Site Mixing of Incompatible Wastes (typical)
TABLE 7: Accident Analysis Calculations -
Scenario 4: Off-Site Spill (conservative)
TABLE 8: Accident Analysis Calculations -
Scenario 4: Off-Site Spill (typical)
TABLE 9: Accident Analysis Calculations -
Scenario 5: Off-Site Spill with Fire (conservative)
TABLE 10: Accident Analysis Calculations -
Scenario 5: On-Site Spill with Fire (typical)
27
29
31
32
33
34
36
38
40
41
ATTACHMENT
Attachment 1: ARCHIE Output for On-Site and Off-Site Fire Scenarios
Volume VH
Appendix VH-3
External Review Draft
Do not cite or quote
-------
I. RELEASE CHARACTERIZATION
A. Methodology
Atmospheric release rates for the chemicals of primary concern are estimated for each
accident scenario selected for quantitative evaluation. The area and extent of on-site
spills/releases are based on facility-specific parameters (e.g., tank volumes, dike sizes).
Emission rates and durations are developed for specific constituents in the emissions based
primarily on short-term modeling techniques. These models can take into account the
physical/chemical properties of the chemicals (e.g., volatility, density, liquid or gas phase),
the presence of passive mitigation devices (e.g., concrete dikes and berms), and active and
redundant mitigation devices (e.g., nitrogen blankets and sprinkler systems).
Wastes consisting of a mixture of chemicals are modeled for all of the events in this
Accident Analysis. Physical and chemical properties for these mixtures are estimated from
the properties of the pure chemicals, weighted by the mass fraction of each chemical
constituent. For example, the molecular weight of a mixture, MW^, containing AT
components is:
-i
where:
MW(
E —
M If,
mass fraction of the ith component;
molecular weight of the zth component.
(1)
The heat of vaporization of a mixture, X^, is:
E »A
(2)
i-l
where:
= heat of vaporization of the ith component.
Volume VH
Appendix VH-3
External Review Draft
Do not cite or quote
-1-
-------
Except for vapor pressure and boiling point, all mixture parameters with units proportional to
the mass (e.g., density) are calculated in a manner similar to Equation (1), whereas
parameters with units proportional to the inverse mass (e.g., heat capacity), are calculated in
a manner similar to Equation (2). The vapor pressure of a mixture is the sum of the vapor
pressures (in equilibrium with the liquid mixture) of the individual components. For a binary
mixture, the liquid can be assumed to act as an ideal solution. Using Raoult's law, the vapor
pressure of the mixture is:
Pv - *AP« +*„?* (3)
where:
pY — vapor pressure of the mixture (Pa);
XA = liquid mole fraction of component A (unitless);
pv* = vapor pressure of pure component A (Pa);
XB = liquid mole fraction of component B (unitless);
pvB' = vapor pressure of pure component B (Pa).
The mass fraction, wit and mole fraction, xit are related by:
and the vapor phase concentrations, yi} are related to the liquid phase concentrations, *„ by
Raoult's law:
y. = (5)
Pv
where:
v, = vapor mole fraction of the ith component at equilibrium with liquid
(unitless).
The vapor pressure of a pure component in a mixture- depends on the boiling temperature
of the mixture which, in turn, is determined by the bubble point of the mixture. The bubble
point is the temperature at which the first bubble of vapor forms when a liquid is heated at
constant pressure. The bubble point of a mixture is approximately its boiling point when the
pressure is equal to atmospheric pressure (1 atm). For an ideal solution, Raoult's law is
Volume VII External Review Draft
Appendix VH-3 Do not cite or quote
-2-
-------
used to determine the bubble point as follows. At the bubble point, and atmospheric
pressure, Equation (3) becomes:
1 atm
where:
Tb = boiling point temperature of the mixture;
~ vapor pressure of pure component A at Tb (Pa);
— vapor pressure of pure component B at Tb (Pa).
The bubble point was calculated by solving Equation (6) iteratively. Antoine's equation
was used to determine the vapor pressure of the pure component as a function of
temperature:
(7)
where A, B and C are chemical-specific Antoine's constants, Tis the boiling point in °C, and
the vapor pressure />*„ is expressed in units of mm Hg. The Antoine equation's constants are
obtained from a standard chemical engineering handbook (Dean 1973). If the constants were
not readily available, they were estimated from vapor pressure-temperature data (Perry and
Green 1984).
The estimates of the chemical emission rates for the accident scenarios discussed in this
report are based on the following assumptions:
• Worst-case mixtures are represented as binary mixtures containing one chemical of
potential concern;
• These binary mixtures behave as ideal solutions (i.e., Raoult's Law applies);
• All liquids are stored at ambient temperature (20°C) and atmospheric pressure;
• Worst-case releases are represented as the release of the largest stored quantity of a
chemical of potential concern over a 10-minute period, under worst case
meteorological conditions (F stability and 1.5 m/s wind speed), considering passive
mitigation measures (U.S. EPA 1995);
Volume VH External Review Draft
Appendix VU-3 Do not cite or quote
-3-
-------
• For spills in areas where no containment barriers are present, the liquid pool will
reach its maximum size when the depth of the pool is 1 cm (U.S. EPA 1992);
• The temperature of the liquid after release is the same as the ambient temperature.
The procedures used to estimate chemical release rates for each accident scenario are
described below.
B. Chemical-Specific Release Rate Calculations
1. On-Site Spill
The spills of two types of mixtures, formaldehyde/methanol and acetone/toluene
mixtures, are examined in the Accident Analysis. The following parameters are used for
the formaldehyde/methanol mixture:
Formaldehyde Methanol Mixture
Mass Fraction 0.1 0.9 1.0
Molecular Weight 30.0 32.1 31.9
Boiling Point (K) 252 338 309
Density (kg/m3) 815 791 794
Vapor Pressure at 20°C (Pa) 441,000 12,900 58,400
The following parameters are used for the acetone/toluene mixture:
Acetone Toluene Mixture
Mass Fraction 0.1 0.9 1.0
Molecular Weight 58.1 92.1 87.0
Boiling Point (K) 329 384 367
Density (kg/m3) 790 870 861
Vapor Pressure at 20°C (Pa) 24,500 2,930 6,170
The conservative on-site spill scenario selected for quantitative evaluation results
from a spill of the contents of a 5,000-gallon tanker truck in the Organic Waste Tank
Farm Truck Unloading Station. The tanker was assumed to be a horizontal cylindrical
tank, 9.5 m long and 1.6 m in diameter. The typical on-site spill scenario selected
results from the rupture of two drums, resulting in a 100-gallon release. The spilled
drums were assumed to be horizontal cylinders, 1 m long and 0.515 m in diameter.
To model the single-phase release of a liquid waste and the subsequent evaporation
of the resulting liquid pool, two emission rates must be determined and compared — the
Volume VII External Review Draft
Appendix VII-3 Do not cite or quote
-4-
-------
liquid release rate, E, and the rate of evaporation from a liquid pool, E^. Comparing
these two emission rates will determine the rate of release to the atmosphere.
For low volatility liquids, E will be greater than E^, and the pool's evaporation
determines the rate at which material enters the atmosphere. The size of the pool being
formed, Ap, depends on the release rate, duration, and the presence of containment
barriers (e.g., dikes, speed bumps, building walls, etc.) in the spill vicinity. For the
conservative case, the size of the pool resulting from the 5,000 gallon spill is limited by
the containment barriers of the Truck Unloading Station, i.e., approximately 418 m2
(75' x60'). This corresponds to a pool depth of approximately 4.5 cm. For the typical
case, assuming the 100 gallon spill spreads to its maximum size and has a depth of 1 cm
(U.S. EPA 1992), the area of the liquid pool would be approximately 38 m2.
In accordance with U.S. EPA guidelines (U.S. EPA 1995), a worst case release is
defined as the release over a 10-minute period of the largest quantity of a regulated
substance resulting from a vessel or process piping failure. Therefore, the liquid release
rate can be estimated by dividing the mass of the liquid in the tanker truck by ten
minutes:
E = ""**' (8)
(10min)(60sec/min)
where:
E = emission rate of liquid from hole, (kg/s);
K«t = volume of storage tank (m3);
p, = storage density (kg/m3).
The liquid release rate calculated by Equation (8) can be related to the dimensions of the
tanker and the hole in the tanker using the following (U.S. EPA 1993):
,
-------
pH = pressure at the hole (Pa):
ph = max (pa ,/?„)+£,£#,; (10)
pa = ambient pressure (Pa);
g = acceleration due to gravity = 9.806 (m/s2);
Hl = vertical distance between hole and the top of liquid level (m);
pa = vapor pressure of the chemical at storage temperature, Ts (Pa).
Assuming the area of the hole is much smaller than the cross-sectional area of the liquid
container, Equation (9) reduces to:
This assumption will be verified when the hole area is calculated. Using the liquid
release rate defined in Equation (8), the area of the hole in the tanker (A0) can be back
calculated from Equation (11).
The liquid release rate (£) is compared to the evaporation rate of a liquid pool:
£ = 6.94xlO~7(l+0.0043(Ara)2)I7r075/i (MW)—L (12)
' Pvh
where:
Epooi - P°ol emission rate (kg/s);
Ur = ambient wind speed at 10 m altitude (m/s);
Ap — pool size (m2);
Ta = ambient temperature (K);
0 if [7;-273.15] <0
[ra-273.15] if [^-273.15] SO
vapor pressure of the liquid at Ta (Pa);
vapor pressure of hydrazine at Ta (Pa):
76.858-1^1^ -8.221n(ra)+0.0061557 ra <13>
For binary mixtures, Equation (3) can be used to calculate pv.
Equation (12) is an empirical formula for estimating source emissions from spills of
toxic liquids (Clewell 1983). It was derived from limited data with specific
Volume Vn External Review Draft
Appendix VII-3 Do not cite or quote
-------
meteorological conditions. Although the ranges of meteorological conditions and
chemical properties were not specified by U.S. EPA, it is understood that this equation
should be used for estimating emission rates under typical meteorological conditions
only. Emission estimates obtained from applying the equation to spills under extreme
meteorological conditions (such as calm conditions, very low wind conditions, or
extreme high wind conditions) represent only results extrapolated beyond the available
data and should not be used without further evaluation. For example, Equation (12) will
predict no emissions for a spill during the calm hours (hours with no winds). In the
current assessment, the pool emission rates were estimated using Equation (12) and
average meteorological conditions (namely, average wind speed and normal
temperature).
If the value of EpoolE and the discharge rate from the tanker determines
the atmospheric emission rate. As the chemical is released, a pool forms that is smaller
than Ap, with an evaporation rate from the formed pool equal to E. The smaller pool
size can be back calculated from Equation (12), setting E^ equal to E.
To determine the evaporation rate of a chemical of concern, the total pool
evaporation rate, E^, is multiplied by the chemical's mole fraction in the volatilizing
mass. Because the vapor pressure of formaldehyde is much greater than that of
methanol, formaldehyde will volatilize from the liquid pool more rapidly than methanol.
Since the two chemicals are released into the atmosphere at different rates, the liquid
pool composition will vary with time. Using Equations (4) and (5) (Raoult's Law), the
vapor mass fractions of formaldehyde and methanol in equilibrium with a 10%
formaldehyde, 90% methanol solution are 0.47 and 0.12, respectively; the balance of the
vapor mass is air. Therefore, the volatilizing mass consists of 80% formaldehyde and
20% methanol.
Being much more volatile and initially present in a lower quantity, the liquid pool
will be depleted of formaldehyde before the entire pool evaporates. As the composition
of the pool changes, the vapor pressure, boiling point-and equilibrium compositions will
also change. Therefore, assuming the system remains in pseudo-steady state, the
properties of the liquid pool and the emission rate are recalculated at discrete time
intervals using Equations (3) through (10) until the pool is depleted of formaldehyde.
The calculated time required to deplete the pool of formaldehyde is used in the
dispersion modeling as the duration of release. The average emission rate for the
Volume VII External Review Draft
Appendix VII-3 Do not cite or quote
-7-
-------
mixture during the duration of release is calculated from the iterative steps discussed
above. The average mole fraction of formaldehyde in vapor is calculated by averaging
the mole fraction computed in each time step. The average mole fraction is used in the
dispersion analysis to convert the formaldehyde concentrations from the mixture
concentrations.
An algorithm is developed for estimating the average mole fraction of a chemical in
vapor during an accident release. It first estimates the quantity of chemicals emitted
from the liquid pool for a finite time increment. The vapor pressure and evaporation
rate of the liquid pool are then recalculated for the next time increment using the
remaining mass in the liquid pool. By iterating the calculations, the duration and
quantity of emissions and the average mole fraction of the chemical of concern in the
vapor phase can be estimated. The methodology is described as follows:
Step 1. Estimate the initial vapor emission rate
The initial emission rate for the mixture can be estimated using the steady-state
emission model described in Equation (12). The evaporation duration is defined for the
mixture, t^, based on the same equation and the total amount of mixture available for
volatilization (U.S. EPA 1993, FEMA 1993):
tmix = M^/E^u,,
where M,^ is the total quantity of mixture available for evaporation.
It is assumed that the emission rate E^ will remain constant during a release
duration of t^ (U.S. EPA 1993, FEMA 1993), which ignores the time-varying nature of
the emission, and therefore overestimates the emission rates and durations for chemicals
with high volatility while underestimated for the chemicals with low volatility.
Step 2. Estimate the initial chemical-specific vapor emission rate
The initial chemical-specific vapor emission rate is estimated using the following
equation (U.S. EPA 1993):
The product of M^M^. and P^P^. represents the initial mass fraction of one
chemical in the vapor immediately after the volatilization.
Volume VH External Review Draft
Appendix VII-3 Do not cite or quote
-8-
-------
As previously mentioned, chemicals with higher evaporation potential will escape
from the pool faster than other chemicals and therefore the mass fraction of a chemical
with higher volatility in the vapor phase will be greater than the chemical with low
volatility. For example, the initial emissions for a 10% formaldehyde and 90%
methanol mixture will consist of approximately 80% of formaldehyde in the vapor. As
the time increases, the percentage of formaldehyde in the vapor will decrease because of
less formaldehyde available for volatilization in the mixture.
Step 3. Estimate the amount of chemicals evaporated during the initial tune step
The amount of chemical evaporated during the initial time step, dM,^, can be
calculated by the following equation:
dMcbenl = Echem x dt,
where dt is the time increment used in defining the time step.
Step 4. Estimate the chemical properties of the liquid pool for the next tune step
By calculating the mass volatilized from the mixture (Step 3) and subtracting it from
the total mass, the mass fraction for the next time step is known. With the new mass
fractions, the chemical properties of the residual liquid mixture can be determined.
Subsequently, the vapor pressure for the new mixture can be computed for estimating the
vapor emission rates for the next time step.
Step 5. Iterate the calculations hi Steps 1 through 4 for the next tune step
Steps 1 through 4 are repeated until the total mass of the liquid pool is completely
depleted.
Step 6. Compute the average chemical-specific emission rate, emission duration,
and mole fraction La the vapor phase
The chemical-specific emission duration can be easily determined during the
iteration by identifying the time required for a chemical to be completely depleted from
the mixture. The average chemical-specific emission rate can be calculated by summing
the mass emitted for each time step and dividing by the total time. The average mole
fraction in the vapor phase is calculated by the sum of the moles of the chemical of
concern emitted divided by the total moles emitted for the duration of the release.
Volume VII External Review Draft
Appendix VII-3 Do not cite or quote
-9-
-------
2. On-Site Fire
The on-site fire scenario selected for quantitative evaluation is a storage tank rupture
in the Organic Waste Tank Farm in the presence of an ignition source, resulting in a
pool fire. The contents of the storage tanks are a mixture of 15 % tetrachloroethene
(PCE) and 85% toluene. The following parameters were used for the
tetrachloroethylene/toiuene mixture:
Tetrachloroethene Toluene Mixture
Mass Fraction 0.15 0.85 1.0
Molecular Weight 165.8 92.1 98.7
Boiling Point (K) 394 384 338.5
Density (kg/m3) 1,630 870 935
Vapor Pressure (Pa) 1,870 2,930 . 2,840
The storage tank is assumed to be a vertical cylinder, 6. 1 m high and 4 m in diameter.
The burning velocity for a liquid with a boiling point above ambient temperature is
given by (FEMA 1993; Burgess et al. 1961):
...
SpG 6
where:
BV = burning velocity (m/s);
MW = molecular weight (kg/kgmol);
SpG = liquid specific gravity (unitless);
Tb = normal boiling point, (K).
The rate of burning, mass burning rate per unit area, is defined as:
where:
dm/dt = mass burning rate per unit area (kg/m2-s);
p, = liquid density or storage density (kg/m3).
Volume Vn External Review Draft
Appendix VTI-3 Do not cite or quote
-10-
-------
By substituting Equation (14) into (15), Equation (15) can be rewritten as:
ZL = 1.54xlO-3(MW)e-ao043(lsr--4597) (16)
dt
The total burning rate is estimated from the product of Equation (16) and the size of the
burning pool. The pool size is defined by the size of the secondary containment area in
the building.
The height of the flame is given by (FEMA 1993; World Bank 1988):
H = 42dfaol
(17)
where:
H = flame height (m);
dpoot = effective diameter of pool (m) (calculated from pool size) ;
pa = density of air (kg/m3).
As mentioned earlier, combustion products that may be emitted during a fire include
NOX, SO2 or HC1. Phosgene emissions are also possible as a product of incomplete
combustion. O'Mara et al. (1971) reported that the potential for phosgene formation
during combustion of chlorinated hydrocarbons could be evaluated based on the
following parameter:
Number of Chlorine Atoms - Number of Hydrogen Atoms
Number of Carbon Atoms
Phosgene formation is likely when o>:0.4. Thus, for example, phosgene could be
formed during the combustion of carbon tetrachloride (<3=4), chloroform (fl=2),
tetrachloroethylene (a=2), and trichloroethylene (fl=l), but would not be expected
during the combustion of chlorobenzene (a=-0.7), dichlorobenzene (a=— 0.3), or
trichloroethane (a=0). The formation of HC1 and phosgene from the combustion of
several chlorinated hydrocarbons was estimated by Sjoberg (1952), as discussed in
Chapter IV. According to Sjoberg (1952), combustion of tetrachloroethene is estimated
to form 238 mg/g of HC1, and 7.0 mg/g of phosgene. These values are combined with
Equation (16) for estimating HC1 and phosgene emissions.
Volume VII External Review Draft
Appendix VII-3 Do not cite or quote
-11-
-------
The resulting plume of hot gases from the fire will have the effect of increasing the
release height as a result of buoyancy forces. To estimate the effective release height,
the buoyancy flux is needed. For a thermal plume, the buoyancy flux is calculated by
(Cooper and Alley 1990; Briggs 1975):
8
MWs
28.9
T. Vd;
+ 0.0089
(19)
where:
QH
d,
MWS
buoyancy flux (mVs3);
heat emission rate (kW);
inner diameter of a stack (m);
atmospheric pressure (Pa);
molecular weight of effluent gas (kg/kgmol);
standard sea level pressure (Pa);
gas temperature (K);
effluent velocity (m/s).
For most combustion sources, MW3 is approximately equal to 28.9, due to the
rigorous entrainment of air into the fire, then the first term of Equation (19) becomes
negligible, and FB can be easily calculated:
FB = 0.0089
(20)
The plume rise caused by a fire is analogous to that caused by heated gases released
from a stack. The buoyancy flux for a fire can thus be expressed using Equation (20).
The heat emission rate can be obtained by multiplying the effective emission power,
Ep, by the area of a heat flux (FEMA 1993). The heat emission rate can thus be
expressed as:
where:
QH = (-0.5634
= area of heat emissions (m2);
= boiling temperature (K).
(21)
Volume VH
Appendix VH-3
External Review Draft
Do not cite or quote
-12-
-------
The flame temperature is calculated based on the heat transfer by way of thermal
radiation. The Stefan-Boltzmann law states that the energy radiated by a hot body is
proportional to the difference in the fourth powers of the absolute temperatures of the
hot source and the more cool receiver of the radiation (Burgess 1978). By treating the
fire as a hot source, the flame temperature can be correlated to the heat flux of the fire
as:
QH = 5.67x10-"^ pp-r/jeF. (22)
where:
QH = heat emission rate (kW);
Tf = flame temperature (K);
e = effective absorptivity on emission factor (e* 1);
Fa = geometric configuration factor (Fa*> 1).
Heat effects for the on-site fire scenario are calculated using the liquid pool fire
option of the FEMA hazard assessment and consequence analysis model ARCHIE
(FEMA 1993). ARCHIE calculates the radius of the circular zone around a liquid pool
fire in which unprotected and/or unsheltered people may experience lethal burns due to
thermal radiation exposures. The major assumptions of the pool fire model include the
following:
• The wind velocity in the burning pool area is insufficient to tilt the flame in the
direction of the wind to a significant degree;
• Individuals in direct view of the flame and in the open have exposed skin (i.e.,
their skin is not protected completely from the effects of thermal radiation by
any clothing being worn);
• The base of the flame is fairly circular in shape;
• Neither carbon dioxide nor water vapor in the air absorbs any of the thermal
radiation impinging on exposed individuals;
• The injury zone is defined by a radiation intensity of 5 kW/m2, which has been
reported to cause second degree burn injuries on bare skin within 45 seconds
(Mudan 1984);
• The fatality zone is defined by a radiation intensity of 10 kW/m2, which has
been reported to quickly cause third degree burns leading to potential fatalities
(Mudan 1984).
Volume VII External Review Draft
Appendix VH-3 Do not cite or quote
-13-
-------
For the conservative on-site fire scenario evaluated here, the pool is assumed to ignite
immediately upon initiation of the liquid discharge. Thus, the burning pool area may be
smaller than the total spilled pool area.
In addition to the heat effects from a pool fire, ARCHIE can calculate the size of a
fireball (diameter, height and duration) and associated thermal radiation zones resulting
from the rupture of a tank engulfed in fire and the subsequent ignition of its contents.
Thus, in the on-site fire scenario, the impact of an explosion of a tank adjacent to the
ruptured tank can be evaluated. The major assumptions of the fireball thermal radiation
model include the following:
• No thermal radiation is absorbed by water vapor or carbon dioxide gas present
in the atmosphere;
• All flammable materials of interest are similar in characteristics (both physical
and chemical properties) to liquefied compressed propane;
• Both the container and exposed individuals are on or near the ground;
• The burn severity depends upon the amount of energy absorbed by the skin after
a surface temperature of 55 °C is achieved.
3. On-site Mixing of Incompatible Wastes
According to ASTM (1986), the mixing of certain classes of incompatible wastes
could result in the generation of toxic gases such as hydrogen chloride, hydrogen cyanide
and hydrogen sulfide, all of which have similar Levels of Concern (LOCs). Because of
the relatively large amounts of chlorinated compounds expected to be processed at the
WTI facility, the generation and release of HC1 was selected for quantitative evaluation
in this scenario. One of the chemicals with the highest chlorine content that is likely to
be handled on-site is tetrachlorethene. A 15% tetrachlorethene/85% methanol waste is
assumed to be accidentally added to a storage tank already containing mineral acids
(70% nitric acid solution). According to ASTM (1986), the mixture of strong mineral
acids with halogenated organic compounds may result in the generation of hydrogen
halides. Therefore, the mixture of tetrachlorethene with 70% nitric acid is likely to
result in the formation and release of gaseous hydrogen chloride.
The conservative on-site mixing of incompatible wastes scenario selected for
quantitative evaluation results from the accidental pumping of waste from a 5,000-gallon
tanker into the wrong vessel in the Organic Waste Tank Farm. Assuming the waste
from the tanker is being pumped at its maximum rate of 250 gal/min, the tanker contents
would be transferred into the storage tank over a 20 minute period. The typical case
Volume VH External Review Draft
Appendix VH-3 Do not cite or quote
-14-
-------
involves a situation similar to the typical case for the on-site spill scenario, i.e., the
rupture of four 55-gallon drums. Two of the drums in this typical scenario contain a
15% tetrachlorethene/85% methanol, and the other two drums contain a 70% nitric acid
solution.
The following parameters were used for the tetrachiorethene/methanol mixture:
Tetrachloroethene Methanol Mixture
Mass Fraction 0.15 0.85 1.0
Molecular Weight 165.8 32.1 36.5
Density (kg/m3) 1,630 791 -857
To model the release of HC1 resulting from the mixing of incompatible wastes, it is
assumed that as the two wastes mix, the reaction between the two wastes to produce HC1
is instantaneous. For the conservative case, the duration of atmospheric release is
estimated to be the 20 minute period required to pump all of the contents of the tanker
into the storage tank. For the typical case, the release duration is estimated to be the
amount of time required for the contents of the four drums to be spilled, forming a
liquid pool. The total amount of HC1 emitted in both cases is calculated from a mass
balance.
4. Off-Site Tanker Truck Spill
The size of the off-site spill depends on the release rate, duration and the presence
of containment barriers (e.g., street curbs, speed bumps, building walls, etc.) in the spill
vicinity, if any. As was the case for the on-site spill, the evaporation of the off-site
liquid pool is dominated primarily by the rate of mass transfer as air flows over the
surface of the pool. Equations (8) through (13) are used for estimating the emission rate
for this scenario.
Assuming the road on which the spill occurs has no curbs that are capable of acting
as a containment barrier, the liquid pool resulting from the conservative 5,000-gallon
spill is assumed to reach a maximum length of approximately 49 m, assuming pool depth
of 1 cm. This assumes the pool spreads in all directions at an equal rate, with liquids
reaching the edge of the road running off onto soil or into a ditch. Assuming the width
of the road is 15 m, the area of the pool is approximately 735 m2. In the typical 100-
gallon spill case, the pool size is approximately 38 m2.
Volume VTJ External Review Draft
Appendix VII-3 Do not cite or quote
-15-
-------
5. Off-Site Tanker Truck Spill with Fire
The off-site fire scenario is similar to the off-site spill scenario, with the additional
presence of an ignition source. To model the emissions from the resulting pool fire,
Equations (14) through (22) are used. The pool is assumed to ignite immediately upon
initiation of the liquid discharge. Thus, the burning pool area may be smaller than the
total spilled pool area. ARCHIE is used to calculate the heat effects associated with the
off-site fire (FEMA 1993).
C. Results of the Release Modeling
The average total emission rates calculated for each accident scenario are summarized
below.
Scenario
On-Site Spill
• Formaldehyde
• Acetone
On-Site Fire
• HC1
• Phosgene
On-Site Mixing of Incompatible
Wastes
• HC1
Off-Site Spill
• Formaldehyde
• Acetone
Off-Site Fire
• HC1
• Phosgene
Average Release Rate (g/s)
Conservative
1,040
465
360
11
1,790
1,840
820
1,470
43
Typical
94
42
150
4.5
71
94
42
76
2.2
Tables 1 through 10 show the input parameters used in deriving the above summary
table. Emission rates for both conservative and typical emission conditions for each accident
scenario were estimated. Step-by-step calculations and relevant input parameters for the
initial time step are presented below.
Volume VH
Appendix VII-3
External Review Draft
Do not cite, or quote
-16-
-------
1. On-Site Spill
a) Physical and chemical properties of 10% Formaldehyde/90% Methanol
mixture
H> = 0.1
\vM = 0.9
(1) Molecular weight
By Equation (1):
01
3L88 8/m°l
30.03 glmol 32.lg/mol
(2) Liquid mole fractions:
By Equation (4):
XM = 1-0.1062 = 0.8938
(3) Boiling point:
Antoine's constants:
Formaldehyde ,4=7.045; B=929.5; C=243.7
Methanol 4=7.879; B=1,473; C=230.0
Using these Antoine's constants, Equation (6) was solved iteratively for Tb.
By Equation (7):
Volume VII External Review Draft
Appendix VII-3 Do not cite or quote
-17-
-------
/7 0*47 - 929'47 \
(36.2°Q = 10\ "•' » «•'/ = 5,296
/7.
.S7863 -
.
/C (36.2°Q = W 36-2 * 230-°/ = 221.2
where r6 = 36.2°C satisfies Equation (6) as follows:
(0.1062)(5,296 mm Hg) + (0.8938)(221.2 mm Hg) = 760 mm Hg
(4) Density
PF = 815 kg/m3 at 20°C
PM = 791.4kg/m3at20°C
According to Equation (1):
o 0.9
793-7
SISkg/m3 79lAkg/m-
(5) Vapor pressure
By Equation (7):
/7.0447 - J»f,,)
(20°Q = 10\ WTTJO/ ,
(7.87863 - **"•"„)
(20°Q = 10l T*mml m 96 87
Volume Vn External Review Draft
Appendix VII-3 Do not cite or quote
-18-
-------
By Equation (3):
pv(20°C) = (0.1062)(3,311 mnHg) + (0.8938)(96.87 mmHg)
= 438 mmHg(l33.322PalmmHg)
(6) Vapor composition
By incorporating Equation (5):
(a) Initial vapor mole fractions
JV<2Q'C,l«m) = (
438
^(20-C.lorm) - (0'8938) (96' 87 ^^ = 0.20
438
(b) Initial vapor mass fraction per mole:
(0.20)(32.1g/mo/)
(0.80)(30.03g//no/)+(0.20)(32.1g//no/)
_ Q
(7) Heat of vaporization
XF = 8.25e+05J/kg
XM = 1.10e+06J/kg
By Equation (2):
• (0.10)(8.25e+057/*g)+(0.90)(1.10e+06J/*») = 1.07e+06//*g
Volume VH External Review Draft
Appendix VII-3 Do not cite or quote
-19-
-------
(8) Heat capacity
(a) Equilibrium vapor at 20° C, 1 atm
CpF.t = 789.3 J/kg K
CpUtt = 1,368 J/kg K
In a similar fashion as Equation (2):
Cpmix =
= 909.8 JlkgK
(b) Liquid mixture, 25 °C
CpFl = 4,295 J/kg K (estimated by Kopp's rule)
CPMJ = 2,542 J/kg K
In a similar fashion as Equation (2):
= 2Jl6J/kgK
b) Other Parameters
(1) Volume of spill
(2) Depth of pool
Containment area = 418.3 m2 = A,
depth =
18.93m3
418.3m2
. 0.045m
Volume VII
Appendix VII-3
-20-
External Review Draft
Do not cite or quote
-------
(3) Effective diameter of pool
- 2
418'3 m2 = 23.08 m
(4) Cross sectional area of liquid container
Hj = 1.6 m, vertical distance between hole and top of liquid level
[ 5000 gal }
A, (m') = I 264.17 gal/m>
f 1.6
1 —
c) Calculations
(1) Pressure at the hole
By Equation (10):
pk = max(101,325Pa,58,408 Pa)+(793.7*£/m3)(9.806m/j2)(1.6m) = 113,770 Pa
(2) Vapor pressure of hydrazine at Tt
By Equation (13):
= exp 176.858 - 7'245-2 -8.221n(293 K)+ 0.0061557 (293K)\ = 1,398 Pa
I 293 K I
Volume VOL External Review Draft
Appendix VH-3 Do not cite or quote
-21-
-------
(3) Liquid release rate from tanker
By Equation (8):
r_5,ooo^/_i 3)
I 264.11 gal/m3 |
= 25 ke/sec
(10min)(60sec/min) *
(4) Total initial evaporation rate
By Equation (12):
= 6.94xlO-7(l+0.0043(20K)2)(3.2 m/s)075(418 m2)(31.88 glmot).
= 2.51 kgls
(5) Initial evaporation rate of formaldehyde
!> = (:
(6) Evaporation time
Calculated iteratively as described in Steps 1 through 6 of Section B.I.
(7) Area of hole
Using Equation (11):
A0(m>) = £ = - 25^/sec = 0.0091m
0.62V2(794^/m3)(113,770-101,325Pa)
which confirms the assumption that A0
-------
(a) Mass burning rate
By Equation (16):
— = 1.54 x lO'3 (98.68 g/mol) tf-o.«*3(i.ie3u.4M>-4».7)
at
= 5.60E-02 kglm2-s
(b) Flame height
By Equation (17):
H = 42(15.1 m)
0.61
0.0560 kg/m2-s
1.2 kg/m3 ^(15.1 m)(9.8 mis2)
21.3 m
(c) HC1 emission rate
m(HCt) =XCF^AP 1238
kg PCE
m(HCl) = (0.15 kg PCE/kg) (0.0560 *g/m2-5) (180 m2) 238
= 0.36
(d) Phosgene emission rate
m(phos) = (0.15 kg PCE/kg) (0.0560 kg/m2-s) (180 m2)
= 1.06E-02 kgls
(e) Heat emission rate
By Equation (21):
S. = -0.5634 (384.45 K) + 260.87 = 44.3 kW/m2
Af
Volume VII External Review Draft
Appendix VII-3 Do not cite or quote
-23-
-------
(f) Buoyancy flux
By Equation (20):
FB = (0.0089)(44.3JtW/m2)(180m2) = 70.9m4/j
(g) Average fire temperature
By Equation (22):
(h) Heat effects
The input parameters used in ARCHIE to compute the liquid pool fire heat
effects and the fireball thermal radiation effects are summarized in Attachment 1.
3. On-Site Mixing of Incompatible Wastes
Calculations not included follow those in Section n.C.l for the On-Site Spill
Scenario. The values of these parameters are summarized in Tables 5 and 6.
(a) HC1 release rate
The HC1 release rate is based on a mass balance, assuming all Cl from the
tetrachloroethylene (PCE) reacts to form HC1. The number of moles of PCE
transferred from the tanker into the storage tank is:
Moles PCE transferred
165.8
f 0.15 k*PCE } f S'000^ 1 (857*^)
_ kgmixture I I **.W*> \
kgmolPCE
= 14.7 kgmolPCE
Four moles of HC1 are produced for every mole of PCE:
Volume VII External Review Draft
Appendix VH-3 Do not cite or quote
-24-
-------
Mass HCl produced = (U.lkgmoIPCE) [4 ^"TCp f365_*£ffCM
5 I ^mo/PCEJ [
The release rate is calculated by averaging the amount of HCl produced over the
transfer time:
HCl release rate = ' . = 1.79^/sec
(20min)(60sec/min) s
The exit velocity at which HCl is released from the vent (8 inch diameter) of the
Organic Waste Tank Farm is:
1.79fcg/sec (QM2Q6m3atm/kgmolK)(293K)
HCl velocity = _ lam _ = 3Mm/aec
0.0324m2
4. Off-Site Tanker Truck Spill
The majority of the emissions calculations for this off-site spill scenario follow those
of the on-site spill scenario described in Section n.C.l. The major difference in the
parameters used for the calculations is the size of the resulting pool. If the pool were
allowed to reach its maximum diameter, at a depth of 1 cm, the resulting pool diameter
would be:
5,000gq/
(0.01 m)w
The length of the pool is assumed to reach this maximum diameter. Because of the
presence of ditches or soil along the side of the road, which restrict the flow of the pool
in the direction perpendicular to the road, the width of the pool is assumed to be the
width of the road (15 m). The spill is either collected by the ditches or adsorbed by the
soil in the direction perpendicular to the road. Therefore the pool size for the off-site
spill scenario is:
Volume MI External Review Draft
Appendix VII-3 Do not cite or quote
-25-
-------
Af = (49m)(15m) = 735m2
The values of the parameters calculated for this off-site scenario are summarized in
Tables 7 and 8.
5. Off-Site Tanker Truck Spill with Fire
The majority of the emissions calculations for this off-site spill with fire scenario
follow those of the off-site spill scenario described in the previous section, and the on-
site fire scenario described in Section H.C.2. The major differences in the parameters
used for the calculations is the volume of the spilled wastes that are ignited. The volume
of spill associated with the off-site fire is one quarter of the volume of spill associated
with the on-site fire. The values of the parameters calculated for this scenario are
summarized in Tables 9 and 10.
01-3999C:PCCOOB85.W51
Volume VII External Review Draft
Appendix VH-3 Do not cite or quote
-26-
-------
TABLE 1
Accident Analysis Calculations
Scenario 1: On-Site Spill (conservative)
(a) 5,000 gallon spill of 10% formaldehyde/90% methanol mixture
Chemical/Physical
Properties:
W;
x,
MW (kg/kgmol)
T*(K)
ft (kg/m3)
P. (Pa)
Y,
X^ (J/kg-K)
C., (J/kg-K)
Cpa (J/kg-K)
Formaldehyde
l.OOe-01
1.06e-01
3.00e+01
2.52e+02
8.15e+02
4.41e+05
7.92e-01
8.25e+05
7.89e+02
4.30e+03
Methanol
9.00e-01
8.94e-01
3.21e+01
3.38e+02
7.91e-(-02
1.29e+04
2.08e-01
1.10e+06
1.37e+03
2.54e-(-03
Truck parameters:
Asdn2)
A.dn2)
H, (m)
T,(K)
9.09e-03
1.51e+01
1.60e+00
2.93e+02
Mixture
l.OOe+00
l.OOe+00
3.19e+01
3.09e+02
7.94e+02
5.84e+04
l.OOe+00
1.07e+06
9.10e+02
2.72e+03
Notes
liquid mass fraction
liquid mole fraction
molecular weight
boiling temperature
liquid density at Ta
vapor pressure at Ta
vapor mass fraction at Ta
heat of vaporization at Tbp
gas heat capacity at 25C
liquid beat capacity at 25C
area of hole
cross sectional area of liquid container
vertical distance between hole and top of liquid level
storage temperature
Other parameters:
T.(K)
P. (Pa)
V^ (m3)
t»a<»)
Mm2)
«U(ni)
depth (m)
Ut (m/s)
2.93e+02
l.Ole+05
1.89e+01
6.00e+02
4.18e+02
2.31e+01
4.53e-02
3.20C-I-00
ambient temperature
ambient pressure
volume of spill (5,000 gal)
spill time
pool area (75 'X 60')
effective pool diameter
pool depth
wind speed at 10
m height
Calculations:
Pk(Pa)
Pviiffa)
E (kg/s)
E^, (kg/s)
E^oo (kg/s)
W(s)
fi
fi.600
1.14e+05
1.40e+03
2.50e+01
1.04e+00
1.99e+00
3.12e+03
4.78e-01
7.42e-01
pressure at the hole
vapor pressure of hydrazine at Ta
liquid release rate from the truck
average total evaporation rate until
average total evaporation rate over
formaldehyde depleted1
first 600 sec
time to evaporate (formaldehyde)
average formaldehyde vapor mole fraction until formaldehyde depleted1
average formaldehyde vapor mole fraction over the first 600 sec
Note:
1 Depletion defined when the liquid mass fraction of formaldehyde in the evaporating pool reaches 0.001
Volume
Appendix VII-3
External Review Draft
Do not cite or quote
-27-
-------
TABLE 1 (continued)
Accident Analysis Calculations
Scenario 1: On-Site Spill (conservative)
(b) 5,000 gallon spill of 10% acetone/90% toluene mixture
Chemical/Physical
Properties:
w,
x,
MW (kg/kgmol)
Tta(K)
ft (kg/m3)
Pv (Pa)
Y,
A™ (J/kg-K)
Cn. (J/kg-K)
CDJ (J/kg-K)
Acetone
l.OOe-01
l^Oe-01
5.81e+01
3.29e+02
7.90e+02
2.45e+04
5.96e-01
5.08e+05
1.296+03
2.236+03
Toluene
9.00e-01
8.50e-01
9.21e+01
3.846+02
8.70e+02
2.93e+03
4.04e-01
3.60e+05
1.13e+03
1.736+03
Truck parameters:
Aotm2)
A.On2)
H,(m)
Tf(K)
9.09e-03
1.51e+ 01
1.60e+00
2.93e+02
Mixture
1.00e+ 00
l.OOe+00
8.70e+01
3.67e+02
8.61e+02
6.17e+03
l.OOe+00
3.75e+05
1.20e+03
1.78e+03
Notes
liquid mass fraction
liquid mole fraction
molecular weight
boiling temperature
liquid density at Ta
vapor pressure at Ta
vapor mass fraction at Ta
heat of vaporization at Tbp
gas heat capacity at 25C
liquid heat capacity at 25C
area of hole
cross sectional area of liquid container
vertical distance
between hole and top of liquid level
storage temperature
Other parameters:
T. (K)
P. (Pa)
Vradl (m3)
t»,ll(s)
A^m2)
^.(m)
depth (m)
Ur (m/s)
2.936+02
l.Ole+05
1.89e+01
6.00e+02
4.18e+02
231e+01
4.53e-02
3.20e+00
ambient temperature
ambient pressure
total volume of spill (5,000 gal)
spill time
pool area (75' X60')
effective pool diameter
pool depth
wind speed at 10 m height
Calculations:
Ph(Pa)
Pv«,(Pa)
E (kg/3)
E.OO, (kg/8)
E^Lfioo (kg/s)
Urte)
f,
fi.MO
1.15e+05
1.40e+03
2.72e+01
4.65e-01
7.12e-01
1.826+04
2.736-01
5.85e-01
pressure at the hole
vapor pressure of hydrazine at Ta
liquid release rate from the truck
average total evaporation rate until acetone depleted1
average total evaporation rate for the first 600 sec
time to evaporate (acetone)
average acetone
average acetone
vapor mole fraction until acetone depleted1
vapor mole fraction over the first 600 sec
Note:
1 Depledon defined when the liquid mass fraction of acetone in the evaporating pool reaches 0.001.
Volume VH
Appendix VH-3
External Review Draft
Do not cite or quote
-28-
-------
TABLE 2
Accident Analysis Calculations
Scenario 1: On-Site Spill (typical)
(a) 100 gallon spill of 10% formaldehyde/90% methanol mixture
Chemical/Physical
Properties:
w,
x,
MW (kg/kgmol)
T,»(K) .
f (kg/m3)
Pv (Pa)
Y,
X™ (J/kg-K)
COJ (J/kg-K)
COJ (J/kg-K)
Formaldehyde
l.OOe-01
1.06e-01
S.OOe+01
2.52e+02
8.15e+02
4.41e+05
7.92e-01
8.25e+05
7.89e+02
4.30e+03
Methanol
9.00e-01
8.94e-01
3.21e+01
3386+02
7.91e+02
129e+04
2.08e-01
1.10e+ 06
1.37e+03
2.54e+03
Drum parameters:
Aofm2)
A.On2)
H,(m)
T.(K)
1.60e-04
2.06e+00
5.15e-01
2.93e+02
Mixture
l.OOe+00
l.OOe+00
3.19e+01
3.09e+02
7.946+02
5.84e+04
l.OOe+00
1.07e+06
9.106+02
2.726+03
Notes
liquid mass fraction
liquid mole fraction
molecular weight
boiling temperature
liquid density at Ta
vapor pressure at Ta
vapor mass fraction at Ta
heat of vaporization at Tbp
gas heat capacity at 25C
liquid heat capacity at 25C
area of hole
cross sectional area of liquid container
vertical distance
between hole and top of liquid level
storage temperature
Other parameters:
T.(K)
P. (Pa)
V«n (m3)
t-i(s)
A.fm2)
dooo, (m)
depth (m)
Ur (m/s)
2.93e+02
l.Ole+05
3.79e-01
6.00e+02
3.79e+01
6.94e+00
l.OOe-02
3.20e+00
ambient temperature
ambient pressure
total volume of
spill (100 gal)
spill time
pool area
effective pool diameter
pool depth
wind speed at 10 m height
Calculations:
P, (Pa)
Pv>(Pa)
E (kg/a)
E^Ckg/s)
EMM (kgA)
Un(s)
f,
*l.«00
1.05e+05
1.406+03
2^0e-01
9.446-02
9.996-02
6.806+02
4.826-01
5.126-01
pressure at the hole
vapor pressure of hydrazine at Ta
liquid release rate from each drum
average total evaporation rate until formaldehyde depleted1
average evaporation rate over the first 600 sec
time to evaporate (formaldehyde)
average formaldehyde vapor mole fraction until depleted1
average formaldehyde vapor mole fraction over the first 600 sec
Note:
1 Depletion defined when the liquid mass fraction in
the evaporating
pool reaches 0.001
Volume
Appendix VH-3
External Review Draft
Do not cite or quote
-29-
-------
TABLE 2 (continued)
Accident Analysis Calculations
Scenario 1: On-Site Spill (typical)
(b) 100 gallon spill of 10% acetone/90% toluene mixture
Chemical/Physical
Properties:
w,
x,
MW (kg/kgmol)
T«,(K)
P (kg/m3)
Pv (Pa)
Y,
A™ (J/kg-K)
CD., (J/kg-K)
COJ (J/kg-K)
Acetone
l.OOc-01
1.50e-01
5.81e+01
3.29e+02
7.90e+02
2.45e+04
5.96e-01
5.08e+05
1.29e+03
2.23e+03
Toluene
9.00C-01
8^0e-01
9.21e+01
3.84e+02
8.70e+02
2.93e+03
4.04C-01
3.60e+05
1.13e+03
1.73e+03
Drum parameters:
Aodn2)
A^m2)
H,(m)
T.(K)
1.60e-04
2.06e+00
5.15e-01
2.93e+02
Mixture
l.OOe-t-00
l.OOe+00
8.70e-i-01
3.676+02
8.61e+02
6.17e+03
1.00e +00
3.756+05
1.206+03
1.78e+03
Notes
liquid mass fraction
liquid mole fraction
molecular weight
boiling temperature
liquid density at Ta
vapor pressure at Ta
vapor mass fraction at Ta
heat of vaporization at Tbp
gas heat capacity at 25C
liquid heat capacity at 25C
area of hole
cross sectional area of liquid container
vertical distance
between hole and top of liquid level
storage temperature
Other parameters:
T.(K)
P. (Pa)
V^ (m3)
t»n(s)
A^m2)
«U,<»)
depth (m)
Ur (m/s)
2.93e+02
l.Ole+05
3.79e-01
6.00e+02
3.79C+01
6.94e+00
l.OOe-02
320e+00
ambient temperature
ambient pressure
total volume of spill (100 gal)
spill time
pool area
effective pool diameter
pool depth
wind speed at 10 m height
Calculations:
Ph (Pa)
P*,(Pa)
E (kg/s)
E*»i (kg/s)
E..OOU600 (kg/s)
t™,(s)
f,
liJSOO
1.06e+05
1.40e+03
2.72e-01
4.22e-02
5.99e-02
3.96e+03
2.76C-01
538e-01
pressure at the hole
vapor pressure of hydrazine at Ta
liquid release rate from each drum
average total evaporation rate until acetone depleted1
average total evaporation rate for the first 600 sec
time to evaporate (acetone)
average acetone
average acetone
Note:
1 Depletion defined when the liquid mass fraction in
vapor mole fraction until depleted1
vapor mole fraction over the first 600 sec
the evaporating pool reaches 0.001
Volume
Appendix VJJ-3
External Review Draft
Do not cite or quote
-30-
-------
TABLE 3
Accident Analysis Calculations
Scenario 2: On-Site Fire (conservative)
PCE storage tank rupture in Organic Waste Tank Farm
Chemical/Physical
Properties:
w,
x,
MW (kg/kgmol) .
Tte(K)
„ (kg/m3)
Pv(Pa)
X™ (J/kg-K)
PCE
LSOe-01
8.93e-02
1.66e+02
3.946+02
1.636+03
1.87e+03
NU1
Toluene
8.506-01
9.116-01
9.216+01
3.84e+02
8.70e+02
2.93e+03
NU
Tank parameters:
A,,(m2)
A, (m2)
H,(m)
«L*(»)
T,(K)
l.Soe-02
1.24e+01
6.10e+00
3.986+00
2.936+02
Mixture Notes
l.OOe+00 liquid mass fraction
l.OOe+00 liquid mole fraction
9.87e +01 molecular weight
3.85e+02 . boiling temperature
935e + 02 liquid density at Ta
2.84e+03 vapor pressure at Ta
NU heat of vaporization at Tto
area of hole
cross sectional area of liquid container
height of storage tank (20 ft)
tank diameter
storage temperature
Other parameters:
T.(K)
P. (Pa)
V^ (m3)
trt«(s)
A^m2)
dnodtm)
depth (m)
HC1 (g/kg)
PG (g/kg)
2.93e+02
1.01e +05
7.57e+01
6.006+02
l.SOe+02
1J516+01
4.216-01
2386+02
7.00e+00
ambient temperature
ambient pressure
total volume of
spill (20,000 gal)
spill time
size of containment area
effective pool diameter
pool depth
HC1 production
from PCE
phosgene production from PCE
Calculations:
dm/dt (kg/m*-s)
H(m)
n»Hc. (fcg/s)
n>PG (kg/s)
QH (kW/m*)
F (mVs3)
T(K)
»•».(«)
5.60e-02
2.13e+01
3.60e-01
1.06e-02
4.436+01
7.096+01
9.426+02
7.036+03
mass burning rate per unit area
flame height
emission rate of HC1
emission rate of phosgene
heat emission rate
buoyancy flux
average fire temperature
time of burning
Note:
1 NU - Not used.
Volume VH
Appendix VH-3
External Review Draft
Do not cite or quote
-31-
-------
TABLE 4
Accident Analysis Calculations
Scenario 2: On-Site Fire (typical)
Four PCE drum rupture indoors
Chemical/Physical
Properties:
w,
^
MW (kg/kgmol)
Tta(K)
ft (kg/m3)
Pv (Pa)
A™ (J/kg-K)
PCE
l.SOe-01
8.93e-02
1.666+02
3.94e+02
1.63C+03
1.87e+03
NU1
Toluene
SJOe-01
9-lle-Ol
9.216+01
3.846+02
8.706+02
2.93e+03
NU
Drum parameters (modeled as a 220-gallon_borizontal
AodnZ)
A, (m2)
H,(m)
Tf(K)
1.60e-04
2.06e+00
5.15e-01
2.93e+02
Mixture Notes
l.OOe+00 liquid mass fraction
l.OOe+00 liquid mole fraction
9.87e+01 molecular weight
3.85e+02 boiling temperature
935e+02 liquid density at Ta
2.846+03 vapor pressure at Ta
NU heat of vaporization at Tbp
cylindrical container):
area of hole
cross sectional area of liquid container
vertical distance
between hole and top of liquid level
storage temperature
Other parameters:
T,(K)
P. (Pa)
V^ (m3)
tB5fll(s)
AaOn2)
d^fm)
depth (m)
HC1 (g/kg)
PG (g/kg)
2.93e+02
l.Olc+05
7.57e-01
6.006+02
7.57C+01
9.82e+00
l.OOe-02
238e+02
7.00C+00
ambient temperature
ambient pressure
total volume of spill (200 gal)
spill time
size of containment area
effective pool diameter
pool depth
HC1 production
from PCE
phosgene production from PCE
Calculations:
dm/dt (kg/mz-s)
H(m)
n»Ha (kg/s)
n»po (kg/s)
QH (kW/m2)
F (mVs3)
T(K)
thmto
5.60e-02
1.58e+01
l^le-01
4.45e-03
4.43C+01
2.98e+01
9.42e+02
1.67e+02
mass burning rate per unit area
flame height
emission rate of HC1
emission rate of
phosgene
heat emission rate
buoyancy flux
average fire temperature
time of burn
Note:
1 NU = Not used.
Volume VH
Appendix VH-3
External Review Draft
Do not cite or quote
-32-
-------
TABLE 5 |
Accident Analysis Calculations '
Scenario 3: On-Site Mixing of Incompatible Wastes (conservative)
Pumping of tanker contents into wrong storage tank
Chemical/Physical Properties:
Truck:
w,
x,
MW (kg/kgmol)
Tb(K)
P (kg/m3)
Pv (Pa)
Storage tank:
w,
x,
MW (kg/kgmol)
Tb(K)
P (kg/m3)
P. (Pa)
PCE
1.506-01
330e-02
1.66e+02
3.94e+02
1.63e+03
1.87e+03
Nitric acid
7.006-01
2.556-01
6306+01
3.56e+02
L50e+03
6.40e+03
Methanol
8JOe-01
9.67e-01
3.21e+01
338e+02
7.91e+02
1.29e+04
Water
3.00e-01
3.82e-01
1.80e+01
3.73e+02
l.OOe+03
234e+03
Mixture
l.OOe+00
l.OOe+00
3.65e-01
339e+02
8.57e+02
1.26+04
Mixture
l.OOe+00
636e-01
2.29e+01
3.93e+02
l.lle+03
337e+03
Notes
liquid mass fraction
liquid mole fraction
molecular weight
boiling temperature
liquid density
vapor pressure at Ta
liquid mass fraction
liquid mole fraction
molecular weight
boiling temperature
liquid density
vapor pressure at Ta
Other parameters:
T.(K)
P. (Pa)
V^ (m3)
r,»«f« (m3/s)
Ur (m/s)
A^On2)
**„«„ (m)
2.93e+02
l.Ole+05
3.79e+01
1.26e-02
3.20e+00
3.24e-02
8.406+00
ambient temperature
ambient pressure
total volume transferred from truck to storage tank (5,000 gal)
maximum pumping rate from truck (250 gal/min)
wind speed at 10 m height
area of vent discharge (8 inch diameter)
height of vent discharge1
Calculations:
MHC, (kg/s)
t«,(s)
1.79e+00
120+03
release rate of HC1
duration of HC1 release
Note:
1 - Includes plume rise due to momentum.
Volume VII
Appendix V1I-3
Draft
Do not cite or quote
-33-
-------
TABLE 6
Accident Analysis Calculations
Scenario 3: On-Site Mixing of Incompatible Wastes (typical)
Four drum rupture outdoors
Chemical/Physical Properties:
Drums A:
w,
x,
MW (kg/kgmol)
Tb(K)
P (kg/m3)
Pv (Pa)
Drums B:
w,
x,
MW (kg/kgmol)
Tb(K)
P (kg/m3)
Pv (Pa)
PCE
1.50e-01
330e-02
1.66e+02
3.94e+02
1.636+03
L87e+03
Nitric acid
7.00e-01
2.55e-01
6306+01
3.56C+02
LSOe+03
6.40e+03
Methanol
8.506-01
9.67e-01
3.216+01
338e+02
7.916+02
1296+04
Water
3.006-01
3.826-01
l.SOe+01
3.736+02
1.00e+ 03
2346+03
Mixture
l.OOe+00
l.OOe+00
3.65e-01
3.39e+02
8.57e+02
1.26+04
Mixture
l.OOe+00
6.36e-01
2.29e+01
3.93e+02
l.lle+03
337e+03
Notes
liquid mass fraction
liquid mole fraction
molecular weight
boiling temperature
liquid density
vapor pressure at Ta
liquid mass fraction
liquid mole fraction
molecular weight
boiling temperature
liquid density
vapor pressure at Ta
Drum parameters:
Ao(m*)
A^m2)
A^m2)
H,(m)
T.(K)
1.60e-04
1.606-04
2.06e+00
5.15e-01
2.93e+02
area of hole for Drums A
area of hole for Drums B
cross sectional area of liquid container
vertical distance between hole and top of liquid level
storage temperature
Other parameters:
T.(K)
P, (Pa)
V«» (m3)
AD(m1)
-------
TABLE 6
Accident Analysis Calculations
Scenario 3: On-Site Mixing of Incompatible Wastes (typical)
Four drum rupture outdoors
6.00e+02
spill time from Drums A
6.00e+02
spill time from Drums B
MHC,
7.14e-02
release rate of HC1
6.00e+02
duration of HC1 release
Volume VII
Appendix VII-3
Draft
Do not cite or quote
-35-
-------
TABLE?
Accident Analysis Calculations
Scenario 4: Off-Site Spill (conservative)
(a) One truck accident, containing 5,000 gallons of 10% formaldehyde/90% methanol
mixture
Chemical/Physical
Properties:
w,
x,
MW (kg/kgmol)
Tb(K)
P fkg/m3)
Pv(Pa)
Y,
A« (J/kg-K)
CD, (J/kg-K)
Qj (J/kg-K)
Formaldehyde
l.OOe-01
1.06e-01
3.00e+01
2.52e+02
8.15e+02
4.41e-i-05
7.92e-01
8.256+05
7.89e+02
4306+03
Methanol
9-OOe-Ol
8,94e-01
321e+01
338e+02
7.916+02
1.29e+04
2.08e-01
1.10e+ 06
137e+03
2.54e+03
Truck parameters:
AoOn2)
A^m2)
H, (m)
T,(K)
9.09e-03
1.51e+01
1.606+00
2.93e+02
Mixture
l.OOe+00
l.OOe+00
3.19e+01
3.09e+02
7.946+02
5.84e+04
l.OOe+00
1.07e+06
9.10e+02
2.726+03
Notes
liquid mass fraction
liquid mole fracdon
molecular weight
boiling temperature
liquid density at Ta
vapor pressure at Ta
vapor mass fracdon at Ta
heat of vaporization at Tbp
gas heat capacity at 25C
liquid heat capacity at 25C
area of hole
cross sectional area of liquid container
vertical distance
between hole and top of liquid level
storage temperature
Other parameters:
T,(K)
P. (Pa)
Vraai (m3)
t^(s)
AD(m2)
«U,(m)
depth (m)
Ur (m/s)
2.936+02
1.01e+ 05
1.89e+01
6.006+02
735e+02
3.06e+01
l.OOe-02
3.206+00
ambient temperature
ambient pressure
total volume of spill (5,000 gal)
spill time
pool area
effective pool diameter
pool depth
wind speed at 10 m height
Calculations:
P> (Pa)
P*(Pa)
E (kg/8)
E™, (kg/s)
t^.(s)
f,
1.14e+05
1.406+03
2.50e+01
1.846+00
1.74e+03
4.84e-01
pressure at the hole
vapor pressure of hydrazine at Ta
liquid release rate from truck
average total evaporation rate until formaldehyde depleted1
time to evaporate (formaldehyde)
average formaldehyde vapor mole fracdon until depleted1
Note:
1 Depletion defined when the liquid mass fracdon of
formaldehyde in
the evaporating pool reaches 0.001
Volume VII
Appendix VII-3
Draft
Do not cite or quote
-36-
-------
TABLE?
(continued)
Accident Analysis Calculations
Scenario 4: Off-Site Spill (conservative)
(b) One truck accident, containing 5,000 gallons of 10% acetone/90% toluene mixture
Chemical/Physical
Properties:
w,
x,
MW (kg/kgmol)
Tb(K)
ft (kg/m3)
Pv (Pa)
Y,
^ (J/kg-K)
C0, (J/kg-K)
CDJ (J/kg-K)
Acetone
l.OOe-01
1.50e-01
5.81e+01
3.29e+02
7.90e+02
2.45e+04
5.96e-01
5.08e+05
1.29e+03
2.23e+03
Toluene
9.00e-01
8.50e-01
9.21e+01
3.84e+02
8.70e+02
2.93e+03
4.046-01
3.60e+05
1.13e+03
1.736+03
Truck parameters:
AoOn2)
A, (m2)
H^m)
T.(K)
9.09e-03
L51e+01
1.60e+00
2.93e+02
Mixture
l.OOe+00
l.OOe+00
8.70e+01
3.67e+02
8.61e+02
6.17e+03
l.OOe+00
3.756+05
1.206+03
1.78e+03
Notes
liquid mass fraction
h'quid mole fraction
molecular weight
boiling temperature
h'quid density at Ta
vapor pressure at Ta
vapor mass fraction at Ta
heat of vaporization at Tbp
gas heat capacity at 25C
liquid heat capacity at 25C
area of hole
cross sectional area of liquid container
vertical distance
between hole and top of liquid level
storage temperature
Other parameters:
T.(K)
P, (Pa)
V^ (m3)
t»u.(s)
AD(m2)
^.(m)
depth (m)
Ur (m/s)
2.93e+02
l.Ole+05
1.89e+01
6.00e+02
735e+02
3.06e+01
238e-02
3.20e+00
ambient temperature
ambient pressure
total volume of
spill (5,000 gal)
spill time
pool area
effective pool diameter
pool depth
wind speed at 10 m height
Calculations:
Ph (Pa)
Pvh(Pa)
E (kg/s)
E™, (kg/s)
U,(s)
f,
1.15e+ 05
1.40e+03
2.726+01
8.18e-01
1.03e+04
2.74e-01
pressure at the hole
vapor pressure of hydrazine at Ta
liquid release rate from truck
average total evaporation rate until acetone depleted1
time to evaporate (acetone) •
average acetone
vapor mole fraction until depleted1
Note:
1 Depletion defined when the h'quid mass fraction of acetone in the evaporating pool reaches 0.001.
Volume VII
Appendix VII-3
Draft
Do not cite or quote
-37-
-------
TABLES
Accident Analysis Calculations
Scenario 4: Off-Site Spill (typical)
(a) One truck accident, containing 5,000 gallons of 10% formaldehyde/
90% methanol mixture
Chemical/Physical
Properties:
w,
x,
MW (kg/kgmol)
Tb(K)
P (kg/m3)
Pv(Pa)
Y,
A™ (J/kg-K)
CDJ (J/kg-K)
Cpr, (J/kg-K)
Formaldehyde
l.OOe-01
1.06e-01
3.00e+01
2.52e+02
8.15e+02
4.41e+05
7.92e-01
8.25e+05
7.89e+02
4.30e+03
Methanol
9.00e-01
8,94e-01
321C+01
338e+02
7.916+02
1.29e+04
2.08e-01
1.10e+ 06
137e+03
2.54e+03
Mixture
l.OOe+00
l.OOe+00
3.19e+01
3.09e+02
7.94C+02
5.84e+04
l.OOe+00
1.07e+06
9.10e+02
2.726+03
Notes
liquid mass fraction
liquid mass fraction
molecular weight
boiling temperature
liquid density at Ta
vapor pressure at Ta
vapor mass fraction at Ta
heat of vaporization at Tbp
gas heat capacity at 25C
liquid heat capacity at 25C
Truck parameters:
AoCm2)
A^m2)
H,(m)
T,(K)
1.82e-04
Ule+01
1.60e+00
2.93e+02
area of hole
cross sectional area of liquid container
vertical distance
between hole and top of liquid level
storage temperature
Other parameters:
T.(K)
P. (Pa)
Vmill (m3)
t»oi(s)
A^m2)
tWm)
depth (m)
Ur(m/s)
2.93e+02
l.Ole+05
3.79e-01
6.00e+02
3.79e+01
6.94e+00
l.OOe-02
3.2e+00
ambient temperature
ambient pressure
total volume of spill (100 gal)
spill time
pool area (low volatility)
effective pool diameter
pool depth
wind speed at 10 m height
Calculations:
P>(Pa)
P^(Pa)
E (kg/s)
E™, (kg/s)
Un(s)
f,
1.14e+05
1.40e+03
2.50e-01
9.44e-02
6.80e+02
4.82C-01
pressure at the hole
vapor pressure of hydrazine at Ta
liquid release rate from each truck
average total evaporation rate until formaldehyde depleted1
time to evaporate (formaldehyde)
average formaldehyde vapor mole fraction until depleted1
Note:
1 Depletion defined when the liquid mass fraction in
the evaporating pool reaches 0.001
Volume VII
Appendix V1I-3
Draft
Do not cite or quote
-38-
-------
TABLE 8 (continued) ||
Accident Analysis Calculations ''
Scenario 4: Off-Site Spill (typical)
(b) One truck accident, containing 5,000 gallons of
10% acetone/90% toluene mixture
Chemical/Physical
Properties:
w,
x,
MW (kg/kgmol)
Tb(K)
ft (kg/m3)
Pv(Pa)
Y,
*~ (J/kg-K)
Q,, (J/kg-K)
CDJ (J/kg-K)
Acetone
l.OOe-01
1.50e-01
5.81e+01
3.29e+02
7.90e+02
2.45e+04
5.96e-01
5.086+05
1.29e+03
2.23e-i-03
Toluene
9.006-01
8.50e-01
9.216+01
3.84e+02
8.70e+02
2.93e+03
4.04e-01
3.60e+05
1.13e+03
1.73e+03
Truck parameters:
AoOn2)
A.dn2)
H,(m)
T,(K)
1.82e-04
IJSle+Ol
1.60e+00
2.93e+02
Mixture
l.OOe+00
l.OOe+00
8.70e+01
3.67e+02
8.616+02
6.17e+03
l.OOe+00
3.75e+05
1206+03
1.78e+03
Notes
liquid mass fraction
liquid mass fraction
molecular weight
boiling temperature
liquid density at Ta
vapor pressure at Ta
vapor mass fraction at Ta
heat of vaporization at Tbp
gas heat capacity at 25C
liquid heat capacity at 25C
area of hole
cross sectional area of liquid container
vertical distance
between hole and top of liquid level
storage temperature
Other parameters:
T,(K)
P, (Pa)
Vmill (m3)
t»n(«)
A. (in2)
d—(m)
depth (m)
Ur (m/s)
2.93e+02
l.Ole+05
3.79e-01
6.00e+02
3.79e+01
6.94e+00
l.OOc-02
3.20e+00
ambient temperature
ambient pressure
total volume of spill (100 gal)
spill time
pool area (low volatility)
effective pool diameter
pool depth
wind speed at 10 m height
Calculations:
P. (Pa)
P«,(Pa)
E (kg/s)
E™, (kg/s)
U=(s)
f,
1.15e+ 05
1.40e+03
5.43e-01
4.22e-02
3.96e+03
2.76e-01
pressure at the hole
vapor pressure of hydrazine at Ta
liquid release rate from the truck
average total evaporation rate until acetone depleted1
time to evaporate (acetone)
average acetone
vapor mole fraction until depleted1
Note:
1 Depletion defined when the liquid mass fraction of formaldehyde in the evaporating pool reaches 0.001
Volume VII
Appendix YII-3
Draft
Do not cite or quote
-39-
-------
TABLE 9
Accident Analysis Calculations
Scenario 5: Off-Site Spill with Fire (conservative)
One truck accident, containing 5,000 gallons of 15% PCE/85% toluene mixture
Chemical/Physical
Properties:
w,
x,
MW (kg/kgmol)
Tb(K)
P (kg/m3)
Pv(Pa)
X™ (J/kg-K)
PCE
l.SOe-01
8.93e-02
1.66e+02
3.94e+02
1.63e+03
1.87e+03
NU1
Toluene
8.50e-01
9.116-01
9.21e+01
3.84e+02
8.70e+02
2.93e+03
NU
Tank parameters:
Ao(m2)
A, (m2)
H,(m)
T,(K)
9.03e-03
L51e+01
1.60e+00
2.93e.+02
Mixture
l.OOe+00
l.QOe+00
9.87e+01
3.856+02
935e+02
2.84e+03
NU
Notes
liquid mass fraction
liquid mass fraction
molecular weight
boiling temperature
liquid density at Ta
vapor pressure at Ta
heat of vaporization at Tbp
area of hole
cross sectional area of liquid container of the truck
vertical distance
between -hole and top of liquid level
storage temperature
Other parameters:
T.(K)
P. (Pa)
V^ (m3)
t»n(s)
AaCm2)
^.(m)
depth (m)
HC1 (g/kg)
PG (g/kg)
2.93e+02
l.Ole+05
1.89e+01
6.006+02
7J5e+02
3.06e+01
l.OOe-02
238e+02
7.00e+00
ambient temperature
ambient pressure
total volume of spill (5,000 gal)
spill time
size of containment area
effective pool diameter
pool depth
HC1 production
from PCE
phosgene production from PCE
Calculations:
dm/dt (kg/m2-s)
H(m)
mHci (fcg/s)
mpG (kg/s)
QHikW/m2)^
F(mVs3)
T(K)
«*»(«)
5.60e-02
3.48e+01
1.47e+00
432e-02
4.43e+01
2.90e+02
9.42e+02
430c+02
mass burning rate per unit area
flame height
emission rate of
emission rate of
HC1
phosgene
heat emission rate
buoyancy flux
average fire temperature
time of burning
Volume VII
Appendix VI1-3
Draft
Do not cite or quote
-40-
-------
TABLE 10 I
Accident Analysis Calculations
Scenario 5: Off-Site Spill with Fire (typical)
One truck accident, containing 5,000 gallons of 15% PCE/85% toluene mixture
Chemical/Physical
Properties:
w,
x,
MW (kg/kgmol)
Th(K)
, (kg/m3)
Pv (Pa)
X™ (J/kg-K)
PCE
1.50e-01
8.936-02
1.66e+ 02
3.94e+02
1.63e+03
1.87e+03
NU1
Toluene
8.50e-01
9.116-01
9.21e+01
3.84e+02
8.706+02
2.93e+03
NU
Tank parameters:
A,,(m2)
A, (m2)
H, (m)
T.(K)
1.82e-04
L51e+01
1.606+00
2.93e+02
Mixture
l.OOe+00
l.OOe+00
9.87e+01
3.85e+02
935e+02
2.84e+03
NU
Notes
liquid mass fraction
liquid mass fraction
molecular weight
boiling temperature
liquid density at Ta
vapor pressure at Ta
heat of vaporization at Tbp
area of hole
cross sectional area of liquid container
vertical distance
between hole and top of liquid level
storage temperature
Other parameters:
T,(K)
P. (Pa)
V— (m3)
^(s)
AD(m2)
dn«,l(in)
depth (m)
HC1 (g/kg)
PG (g/kg)
2.936+02
1.01e+ 05
3.79e-01
6.00e+02
3.79e+01
6.94e+00
l.OOe-02
238e+02
7.006+00
ambient temperature
ambient pressure
total volume of spill (100 gal)
spill time
size of containment area
effective pool diameter
pool depth
HC1 production
from PCE
phosgene production from PCE
Calculations:
dm/dt (kg/m2-s)
H(m)
mHC1 (kg/s)
m^ (kg/s)
QH (kW/m2)
F (mVs3)
T(K)
^(s)
5.606-02
124e+01
7.56e-02
2.22e-03
4.43e+01
1.49e+01
9.426+02
1.67e+02
mass burning rate per unit area
flame height
emission rate of HC1
emission rate of phosgene
heat emission rate
buoyancy flux
average fire temperature
time of burning
Note:
1 Not used.
1-3999C:FCCOOB85.W51
Volume VII
Appendix VII-3
Draft
Do not cite or quote
-41-
-------
H. REFERENCES
American Society for Testing and Materials (ASTM). 1986. Proposed guide for
estimating the incompatibility of selected hazardous wastes based on binary chemical
reactions. D-34 Proposal P 168. March.
Briggs, G.A. 1975. Plume rise predictions. In Lectures on air pollution and
environmental impact analyses. American Meteorological Society.
Burgess, D.S., A. Strasser, and J. Gmmer. 1961. Diffusive burning of liquid fuel in open
trays. The Fire Research Abs. & Review 3:177.
Burgess, HJ. 1978. The thermal environment conditioning and control Harper & Row
Publisher, New York, N.Y.
Clewell, HJ. 1983. A simple formula for estimating source strengths for spills of toxic
liquids. U.S. Air Force Report ESL-TR-83-03.
Cooper, C.D. and F.C. Alley. 1990. Air pollution control: a design approach. Waveland
Press. Prospect Heights, IL.
Dean, J.A. 1973. Lange's handbook of chemistry, eleventh edition, McGraw-Hill Book
Company, New York, N.Y.
Federal Emergency Management Agency (FEMA), United States Department of
Transportation (U.S. DOT), and United States Environmental Protection Agency
(U.S. EPA). 1993. Handbook of chemical hazard analysis procedure. NTIS PB93-
158756.
Mudan, K.S. 1984. Thermal radiation hazards from hydrocarbon pool fires. Prog.
Energy Comb. ScL 10:59-80.
O'Mara, M.M., L.B. Crider, and R.L. Daniel. 1971. Combustion products from vinyl
chloride monomer. Amer. Industrial Hygiene Assoc. Journal 32:153-156.
Perry, R.H. and D.W. Green. 1984. Perry's chemical engineer's handbook, Sixth edition,
McGraw-Hill Book Company, New York, NY.
Volume VII Draft
Appendix VII-3 Do not cite or quote
-42-
-------
Sjoberg, B. 1952. Thermal decomposition of chlorinated hydrocarbons. Svensk Kemistk
Tidsskrift 64:63-79.
United States Environmental Protection Agency (U.S. EPA). 1992. Office of Air
Quality Planning and Standards. Workbook of screening techniques for assessing
impacts of toxic air pollutants (Revised). U.S. EPA-454/R-92-024. Research Triangle
Park,NC. May.
United States Environmental Protection Agency (U.S. EPA). 1993. Office of Air
Quality Planning and Standards. Guidance on the application of refined dispersion
models for hazardous/toxic air releases. U.S. EPA-454/R-93-002. Research Triangle
Park,NC. May.
United States Environmental Protection Agency (U.S. EPA). 1995. Accidental release
prevention requirements: Risk management programs under Clean Air Act Section
112(r)(7); Proposed rule. Fed. Regis. «>(48):13526-13545.
World Bank. 1988. Techniques for assessing industrial hazards. World Bank Technical
Paper Number 55. The World Bank. Washington, D.C.
01-3999C:I1CCOOB85.W31
Volume VII Draft
Appendix VII-3 Do not cite or quote
-43-
-------
ATTACHMENT 1
ARCHIE Output for On-Site and Off-site Fire Scenarios
-------
1. Fire after the spill achieves maximum size
-------
HAZARDOUS MATERIAL
ADDRESS \ LOCATION
DATE OF ASSESSMENT
NAME OF DISK FILE
= PCE/toluene
= WTI, East Liverpool, OH
= June 5, 1995
= SC2CON.ASF
***
SCENARIO DESCRIPTION
WTI Accident Analysis, Scenario 2 (conservative)
Storage tank rupture in organic waste tank farm
20,000 gallon spill and fire
DISCHARGE RATE/DURATION ESTIMATES
Liquid discharge from nonpressurized container
Average discharge rate - 15352
Duration of discharge « 10.2
Amount discharged = 156095
State of material * Liquid
******* LIQUID POOL SIZE ESTIMATES
Evaporating pool area » 1940
Burning pool area « 1940
Ibs/min
minutes
Ibs
ft2
ft2
Note: Pool is assumed to ignite after pool achieves max-
imum size.
******* POOL FIRE HAZARD ESTIMATION RESULTS
Burning pool radius » 24.9
Flame height - 70
Fatality zone radius • « 65
Injury zone radius * 93
******* FIREBALL HAZARD RESULTS
Max fireball diameter 859
Maximum fireball height 1411
Fireball duration 16.5
Fatality zone radius 1199
Injury zone radius 2274
feet
feet
feet
feet
feet
feet
seconds
feet
feet
-------
INPUT PARAMETER SUMMARY
233
96.68
.94
.409
21.13
PHYSIOCHEMICAL PROPERTIES OF MATERIAL
NORMAL BOILING POINT
MOLECULAR WEIGHT
LIQUID SPECIFIC GRAVITY
VAPOR PRES AT AMBIENT TEMP
CONTAINER CHARACTERISTICS
CONTAINER TYPE
TANK DIAMETER
TOTAL WEIGHT OF CONTENTS
LIQUID HEIGHT IN CONTAINER
DISCHARGE HOLE DIAMETER
DISCHARGE COEFFICIENT OF HOLE
TEMP OF CONTAINER CONTENTS
TANK CONTENTS DURING FIREBALL
ENVIRONMENTAL/LOCATION CHARACTERISTICS
AMBIENT TEMPERATURE - 68
WIND VELOCITY « 3.4
LIQUID CONFINEMENT AREA » NONE
dearees F
psia
"mm Kg
» Vertical cylinder
= 13.046 feet
s
=
s
c
—
156095
20
8.5
.62
68
156095
Ibs
feet
inch(es
degrees
Ibs
degrees F
tnph
KEY RESULTS PROVIDED BY USER INSTEAD OF BY EVALUATION METHODS
NONE OBSERVED
KEY RESULTS OVERRIDDEN BY USER AT SOME POINT AFTER COMPUTATION
NONE OBSERVED
-------
HAZARDOUS MATERIAL - PCE/toluene
ADDRESS \ LOCATION * WTI, East Liverpool, OH
DATE OF ASSESSMENT = June 5, 1995
NAME OF DISK FILE = SC2TYP.ASF
*** SCENARIO DESCRIPTION
WTI Accident Analysis, Scenario 2 (typical)
Four drums rupture indoors
200 gallon spill and fire
DISCHARGE RATE/DURATION ESTIMATES
Liquid discharge from nonpressurized container
Average discharge rate « 156.5 Ibs/min
Duration of discharge * 9.99 minutes
Amount discharged - 1561 Ibs
State of material * Liquid
LIQUID POOL SIZE ESTIMATES
Evaporating pool area » 812 ft2
Burning pool area » 811.2 ft2
Note: Pool is assumed to ignite immediately upon initia-
tion of discharge.1
POOL FIRE HAZARD ESTIMATION RESULTS
Burning pool radius * 16.1 . feet
Flame height * 52 feet
Fatality zone radius ' » 42 feet
Injury zone radius * 60 feet
******* FIREBALL HAZARD RESULTS
Max fireball diameter
Maximum fireball height
Fireball duration
Fatality zone radius
Injury zone radius .
186 feet
305 feet
7.7 seconds
93 feet
208 feet
Note should read "Pool is assumed to ignite after pool
achieves maximum size." This is due to a scrambled flag in
the program's reportable module. This was verifed by the
company which wrote the program, Hazmat America Inc.
-------
INPUT PARAMETER SUMMARY
PHYSIOCHEMICAL PROPERTIES OF MATERIAL
NORMAL BOILING POINT
MOLECULAR WEIGHT
.LIQUID SPECIFIC GRAVITY
VAPOR PRES AT AMBIENT TEMP
233
98.68
.94
.409
21.13
degrees F
psia
min Ho
CONTAINER CHARACTERISTICS
CONTAINER TYPE
TANK DIAMETER
TOTAL WEIGHT OF CONTENTS
LIQUID HEIGHT IN CONTAINER
DISCHARGE HOLE DIAMETER
DISCHARGE COEFFICIENT OF HOLE
TEMP OF CONTAINER CONTENTS
TANK CONTENTS DURING FIREBALL
= Vertical cylinder
3.53
1561
2.8
1.42
.62
66
1561
ENVIRONMENTAL/LOCATION CHARACTERISTICS
AMBIENT TEMPERATURE > 68
WIND VELOCITY « 3.4
LIQUID CONFINEMENT AREA - NONE
feet
Ibs
feet
inch(es)
degrees F
Ibs
degrees F
mph
KEY RESULTS PROVIDED BY USER INSTEAD OF BY EVALUATION METHODS
NONE OBSERVED
KEY RESULTS OVERRIDDEN BY USER AT SOME POINT AFTER COMPUTATION
NONE OBSERVED
-------
HAZARDOUS MATERIAL
ADDRESS \ LOCATION
DATE OF ASSESSMENT
NAME OF DISK FILE
- PCS/ toluene
- WTI , East Liverpool, OH
= June 5, 1995
=° SC5CON.ASF
SCENARIO DESCRIPTION
WTI Accident Analysis, Scenario #5 (conservative)
Off -site tanker truck accident
5,000 gallon spill and fire
DISCHARGE RATE/DURATION ESTIMATES
Liquid discharge from nonpressurized container
Average discharge rate * 3854.3
Duration of discharge = 10.2
Amount discharged * 39024
State of material * Liquid
LIQUID POOL SIZE ESTIMATES
Evaporating pool area « 7907
Burning pool area » 7907
Ibs/min
minutes
Ibs
ft2
ft2
Note: Pool is assumed to ignite after pool achieves max
imum size.
pooL FIRE HAZARD ESTIMATION RESULTS
Burning pool radius « 50.2
Flame height » 114
Fatality zone radius ' « 131
Injury zone radius * 187
******* FIREBALL HAZARD RESULTS
Max fireball diameter « 541
Maximum fireball height * 889
Fireball duration « 13.1
Fatality zone radius « 552
Injury zone radius » -1106
feet
feet
feet
feet
feet
feet
seconds
feet
feet
-------
INPUT PARAMETER SUMMARY
PHYSIOCHEMICAL PROPERTIES OF MATERIAL
NORMAL BOILING POINT = 233 degrees F
MOLECULAR WEIGHT « 98.68
LIQUID SPECIFIC GRAVITY * .94
VAPOR PRES AT AMBIENT TEMP « .409 psia
« 21.13 mm Hg
CONTAINER CHARACTERISTICS
CONTAINER TYPE
TANK DIAMETER
• TANK LENGTH
TOTAL WEIGHT OF CONTENTS
LIQUID HEIGHT IN CONTAINER
DISCHARGE HOLE DIAMETER
DISCHARGE COEFFICIENT OF HOLE
TEMP OF CONTAINER CONTENTS
TANK CONTENTS DURING FIREBALL
Horizontal .cylinder
4.2
48.3
39024
4.2
5.8
.62
68
39024
ENVIRONMENTAL/LOCATION CHARACTERISTICS
AMBIENT TEMPERATURE » 68
WIND VELOCITY « 3.4
LIQUID CONFINEMENT AREA » NONE
feet
feet
Ibs
feet
inch(es)
degrees F
Ibs
degrees F
mph
KEY RESULTS PROVIDED BY USER INSTEAD OF BY EVALUATION METHODS
NONE OBSERVED
KEY RESULTS OVERRIDDEN BY USER AT SOME POINT AFTER COMPUTATION
NONE OBSERVED
-------
HAZARDOUS MATERIAL - PCE/toluene
ADDRESS \ LOCATION - WTI, East Liverpool, OH
DATE OF ASSESSMENT = Jur.e 5, 1995
-x NAME Or DISK FILE * SC5TYP.AS?
\^ *** SCENARIO DESCRIPTION
WTI Accident Analysis, Scenario 5 (typical)
Off-site tanker truck accident
100 gallon spill and fire
******* DISCHARGE RATE/DURATION ESTIMATES
Liquid discharge from nonpressurized container
Average discharge rate » 78.4 Ibs/mir.
Duration of discharge * 10 minutes
Amount discharged * 784 Ibs
State of material = Liquid
Note: Duration of discharge was intentionally shortened
by.user to account for response to spill. Computed
duration was originally 498.1 minutes.
******* LIQUID POOL SIZE ESTIMATES
Evaporating pool area « 408 ft2
Burning pool area » 407.4 ft2
: Note: Pool is assumed to ignite immediately upon initia-
v _/•' tion of discharge. 1
-POOL FIRE HAZARD ESTIMATION RESULTS
Burning pool radius « 11.4 feet
Flame height * 41 feet
Fatality zone radius « 30 feet
Injury zone radius » 43 feet
FIREBALL HAZARD RESULTS
Max fireball diameter
Maximum fireball height
Fireball duration
Fatality zone radius
Injury zone radius
148 feet
•242 feet
6.8 seconds
74 feet
145 feet
Note should read "Pool is assumed to ignite after pool
achieves maximum size." This is due to a scrambled flag in
the program's reportable module. This was verifed by the
company which wrote the program, Hazmat America Inc.
-------
INPUT PARAMETER SUMMARY
233
98.68
.94
.409
21.13
PHYSIOCHEMICAL PROPERTIES OF MATERIAL
NORMAL BOILING POINT
MOLECULAR WEIGHT
LIQUID SPECIFIC GRAVITY
VAPOR PRES AT AMBIENT TEMP
CONTAINER CHARACTERISTICS
CONTAINER TYPE
TANK DIAMETER
TANK LENGTH
TOTAL WEIGHT OF CONTENTS
LIQUID HEIGHT IN CONTAINER
DISCHARGE HOLE DIAMETER
DISCHARGE COEFFICIENT OF HOLE
TEMP OF CONTAINER CONTENTS
TANK CONTENTS DURING FIREBALL
ENVIRONMENTAL/LOCATION CHARACTERISTICS
AMBIENT TEMPERATURE » 68
WIND VELOCITY - 3.4
LIQUID CONFINEMENT AREA - NONE
degrees F
•psia
mm Hg
*
c
«
m
*
m
«
Horizontal
4.2
48.3
39024
4.2
.827
.62
68
784
cylinder
feet
feet
Ibs
feet
inch(es
degrees
Ibs
degrees F
mph
KEY RESULTS PROVIDED BY USER INSTEAD OF BY EVALUATION METHODS
NONE OBSERVED
KEY RESULTS OVERRIDDEN BY USER AT SOME POINT AFTER COMPUTATION
NONE OBSERVED
-------
2. Fire immediately upon the spill
-------
HAZARDOUS MATERIAL = PCE/toluene
ADDRESS \ LOCATION = WTI, East Liverpool, OH
DATE OF ASSESSMENT * June 5, 1995
NAME OF DISK FILE = SC2CONP.ASF
*** SCENARIO DESCRIPTION
WTI Accident Analysis, Scenario 2 (conservative)
Storage tank rupture in organic waste tank farm
20,000 gallon spill and fire
DISCHARGE RATE/DURATION ESTIMATES
Liquid discharge from nonpressurized container
Average discharge rate * 15352 Ibs/min
Duration of discharge « 10.2 minutes
Amount discharged * 156095 Ibs
State of material * Liquid
LIQUID POOL SIZE ESTIMATES
Evaporating pool area * 1940 ft2
Burning pool area » 1940 ft2
Note: Pool is assumed to ignite after pool achieves max-
imum size. i
******* POOL FIRE HAZARD ESTIMATION RESULTS
Burning pool radius » 24.9 feet
Flame height « 70 feet
Fatality zone radius * 65 feet
Injury zone radius * 93 feet
FIREBALL HAZARD RESULTS
Max fireball diameter « 859 feet
Maximum fireball height - 1411 feet
Fireball duration - 16.5 seconds
Fatality zone radius » 1199 feet
Injury zone radius « 2274 feet
Note should read "Pool is assumed to ignite immediately
upon initiation of discharge." This is due to a scrambled
flag in the program's reportable module. This was verifed
by the company which wrote the program, Hazmat America Inc.
-------
INPUT PARAMETER SUMMARY
233
96.68
.94
.406
21.1
.408
21.1
PHYSIOCHEMICAL PROPERTIES OF MATERIAL
NORMAL BOILING POINT
MOLECULAR WEIGHT
LIQUID SPECIFIC GRAVITY
VAPOR PRES AT CONTAINER TEMP *
VAPOR PRES AT AMBIENT TEMP
CONTAINER CHARACTERISTICS •
CONTAINER TYPE
TANK DIAMETER
TOTAL WEIGHT OF CONTENTS
LIQUID HEIGHT IN-CONTAINER
DISCHARGE HOLE DIAMETER
DISCHARGE COEFFICIENT OF HOLE
TEMP OF CONTAINER CONTENTS
TANK CONTENTS DURING FIREBALL
ENVIRONMENTAL/LOCATION CHARACTERISTICS
AMBIENT TEMPERATURE * 68
WIND VELOCITY - 3.4
LIQUID CONFINEMENT AREA - NONE
degrees F
psia
mm Hg
psia
mm Hg
_
s
B
.
«
m
Vertical
13.046
156095
20
8.5
.62
68
156095
cylinder
feet
Ibs
feet
inch(es)
degrees
Ibs
degrees F
mph
KEY RESULTS PROVIDED BY USER INSTEAD OF BY EVALUATION METHODS
NONE OBSERVED
KEY RESULTS OVERRIDDEN BY USER AT SOME POINT AFTER COMPUTATION
NONE OBSERVED
-------
HAZARDOUS MATERIAL
ADDRESS \ LOCATION
DATE OF ASSESSMENT
NAME OF DISK FILE
- PCE/toluene
= WTI, Ease Liverpool,
= June 5, 1995
* SC2TYPP.ASF
OH
*•**
SCENARIO DESCRIPTION
WTI Accident Analysis, Scenario 2 (typical)
Four drums rupture indoors
200 gallon spill and fire
DISCHARGE RATE/DURATION ESTIMATES
Liquid discharge from nonpressurized container
Note;
Average discharge rate « 156.5
Duration of discharge « 9.99
Amount discharged « 1561
State of material « Liquid
LIQUID POOL SIZE ESTIMATES
Evaporating pool area « 812
Burning pool area » 227.9
Pool is assumed to ignite immediately
tion of discharge.
Ibs/min
minutes
Ibs
******* POOL FIRE HAZARD ESTIMATION RESULTS
Burning pool radius - 8.6
'Flame height ' « 34
Fatality zone radius * 23
Injury zone radius » 32
******* FIREBALL HAZARD RESULTS
Max fireball diameter 186
Maximum fireball height 305
Fireball duration 7.7
Fatality zone radius 53
-Injury zone radius 208
ft2
ft2
upon initia-
feet
feet
feet
feet
feet
feet
seconds
feet
feet
-------
INPUT PARAMETER SUMMARY
PHYSIOCHEMICAL PROPERTIES OF MATERIAL
NORMAL BOILING POINT
MOLECULAR WEIGHT
LIQUID SPECIFIC GRAVITY
VAPOR PRES AT AMBIENT TEMP
233
98.68
.94
.409
21.13
CONTAINER'CHARACTERISTICS
CONTAINER TYPE
TANK DIAMETER
TOTAL WEIGHT OF CONTENTS
LIQUID HEIGHT IN CONTAINER
DISCHARGE HOLE DIAMETER
DISCHARGE COEFFICIENT OF HOLE
TEMP OF CONTAINER CONTENTS
TANK CONTENTS DURING FIREBALL
degrees F
psia
mm Hg
Vertical cylinder
3.53
1561
2.8
1.42
.62
68
1561
ENVIRONMENTAL/LOCATION CHARACTERISTICS
AMBIENT TEMPERATURE « 68
WIND VELOCITY « 3.4
LIQUID CONFINEMENT AREA « NONE
feet
Ibs
feet
inch(es)
degrees F
Ibs
degrees F
mph
KEY RESULTS PROVIDED BY USER INSTEAD OF BY EVALUATION METHODS
NONE OBSERVED
KEY RESULTS OVERRIDDEN BY USER AT SOME POINT AFTER COMPUTATION
NONE OBSERVED
-------
HAZARDOUS MATERIAL
ADDRESS \ LOCATION
DATE OF ASSESSMENT
NAME OF DISK FILE
* PCE/toluene
= WTI, East Liverpool, OH
= June 5, 1995
= SC5CONP.ASF
*** SCENARIO DESCRIPTION
WTI Accident Analysis, Scenario #5 (conservative)
Off-site tanker truck accident
5,000 gallon spill and fire
******* DISCHARGE RATE/DURATION ESTIMATES
Liquid discharge from nonpressurized container
Note
Average discharge rate * 3854.3
Duration of discharge =10.2
Amount discharged * 39024
State of material « Liquid
LIQUID POOL SIZE ESTIMATES
Evaporating pool area » 7907
Burning pool area » 5611
Pool is assumed to ignite immediately
tion of discharge.
Ibs/min
minutes
Ibs
******* poOL FIRE HAZARD ESTIMATION RESULTS
Burning pool radius * 42.3
•Flame height " * 102
Fatality zone radius * 110
Injury zone radius » 158
FIREBALL HAZARD RESULTS
Max fireball diameter » 541
Maximum fireball height * 889
Fireball duration * 13.1
Fatality zone radius * 552
Injury zone radius * 1106
ft2
ft2
upon initia-
feet
feet
feet
feet
feet
feet
seconds
feet
feet
-------
INPUT PARAMETER SUMMARY
PHYSIOCHEMICAL PROPERTIES OF MATERIAL
NORMAL BOILING POINT « 233
MOLECULAR WEIGHT - 98.68
LIQUID SPECIFIC GRAVITY « .94
VAPOR PRES AT AMBIENT TEMP « .409
= 21.13
degrees F
psia
mm Hg
CONTAINER CHARACTERISTICS
CONTAINER TYPE
TANK DIAMETER
TANK LENGTH
TOTAL WEIGHT OF CONTENTS
LIQUID HEIGHT IN CONTAINER
DISCHARGE HOLE DIAMETER
DISCHARGE COEFFICIENT OF HOLE
TEMP OF CONTAINER CONTENTS
TANK CONTENTS DURING FIREBALL
Horizontal cylinder
4.2
48.3
39024
4.2
5.8
.62
68
39024
ENVIRONMENTAL/LOCATION CHARACTERISTICS
AMBIENT TEMPERATURE « 68
WIND 'VELOCITY - 3.4
LIQUID CONFINEMENT AREA - NONE
feet
feet
Ibs
feet
inch(es)
degrees F
Ibs
degrees F
mph
KEY RESULTS PROVIDED BY USER INSTEAD OF BY EVALUATION METHODS
NONE OBSERVED
KEY RESULTS OVERRIDDEN BY USER AT SOME POINT AFTER COMPUTATION
NONE OBSERVED
-------
HAZARDOUS MATERIAL
ADDRESS \ LOCATION
DATE OF ASSESSMENT
NAME OF DISK FILE
- PCE/toluene
= WTI, East Liverpool, OH
= June 5, 1995
s SC5TYPP.ASF
*** SCENARIO DESCRIPTION
WTI Accident Analysis, Scenario 5 (typical)
Off-site tanker truck accident
100 gallon spill and fire
DISCHARGE RATE/DURATION ESTIMATES
Liquid discharge from nonpressurized container
Average discharge rate
Duration of discharge
Amount discharged
State of material
78.4
10
784
Liquid
Ibs/min
minutes
Ibs
Note: Duration of discharge was intentionally shortened
by user to account for response to spill. Computed
duration was originally 498.1 minutes.
*******
LIQUID POOL SIZE ESTIMATES
Evaporating pool area *
Burning pool area *
408
114.2
ft2
ft2
Note: Pool is assumed to ignite immediately upon initia-
tion of discharge.
******* pooL FIRE HAZARD ESTIMATION RESULTS
Burning pool radius » 6.1
Flame height « 27
Fatality zone radius * 16
Injury zone radius » 23
******* FIREBALL HAZARD RESULTS
Max fireball diameter « 148
Maximum fireball height * 242
Fireball duration » 6.8
Fatality zone radius - 74
Injury zone radius « 145
feet
feet
feet
feet
feet
feet
seconds
feet
feet
-------
INPUT PARAMETER SUMMARY
PHYSIOCHEMICAL PROPERTIES OF MATERIAL
NORMAL BOILING POINT « 233
MOLECULAR WEIGHT - 98.68
LIQUID SPECIFIC GRAVITY « .94
VAPOR PRES AT AMBIENT TEMP * .409
- 21.13
degrees F
psia
mm' Hg
CONTAINER CHARACTERISTICS
CONTAINER TYPE
TANK DIAMETER
TANK LENGTH
TOTAL WEIGHT OF CONTENTS
LIQUID HEIGHT IN CONTAINER
DISCHARGE HOLE DIAMETER
DISCHARGE COEFFICIENT OF HOLE
TEMP OF CONTAINER CONTENTS
TANK CONTENTS DURING FIREBALL
«. Horizontal cylinder
4.2
48.3
39024
4.2
.827
.62
68
784
ENVIRONMENTAL/LOCATION CHARACTERISTICS
AMBIENT TEMPERATURE » 68
WIND VELOCITY - 3.4
LIQUID CONFINEMENT AREA - NONE
feet
feet
Ibs
feet
inch(es)
degrees
Ibs
degrees F
mph
KEY RESULTS PROVIDED BY USER INSTEAD OF BY EVALUATION METHODS
NONE OBSERVED
KEY RESULTS OVERRIDDEN BY USER AT SOME POINT AFTER COMPUTATION
NONE OBSERVED
-------
APPENDIX Vn-4
Atmospheric Dispersion Modeling
-------
CONTENTS
Page
I. ATMOSPHERIC DISPERSION MODELING 1
A. Model Selection 1
1. SLAB Model . 1
2. ISC-COMPDEP Model 2
B. Meteorological Data 2
1. Typical Condition 2
2. Conservative Condition 4
3. Calm/Inversion Condition 4
C. Dispersion Categories 5
D. Modeling Parameters 7
1. SLAB 7
2. ISC-COMPDEP 13
E. Results and Discussions 15
1. Initial Concentration 15
2. Ambient Temperature 17
3. Relative Humidity 17
4. Modeling Emission Under Calm/Inversion Conditions 17
5. Distances to LOG and IDLH Concentrations 20
6. Modeling Emissions from Large Fires Using ISC-COMPDEP 21
a) ISC-COMPDEP Modeling Results for
Conservative Meteorological Condition 21
b) ISC-COMPDEP Modeling Results for Typical
Meteorological Condition 22
7. Interpreting ISC-COMPDEP Results to 10-min Release
Scenario 23
8. Modeling Emissions from Small Fires Using the ISC-
COMPDEP Output for Large Fires 23
9. ISC-COMPDEP Modeling Results Using 1-yr Real-time
Meteorological Data 24
10. Modeling Emissions from Mixing of Incompatible Waste 25
11. Concentration Averaging Time at Receptors 26
12. Unconfined On-site Spill 27
II. REFERENCES 62
Volume VII External Review Draft
Appendix VII-4 Do not cite or quote
-------
CONTENTS
(continued)
FIGURES
age
Table 1:
Table 2:
Table 3:
Table 4:
Table 5:
Table 6:
Table 7:
Table 8:
Table 9:
Table 10:
Table 11:
Table 12:
Table 13:
Table 14:
Table 15:
Table 16:
Table 17:
TABLES
Stability Wind Speed Combinations Used to Determine the
Conservative Meteorological Conditions
Summary of Input Parameters for the On-Site Spill
Scenario (Conservative Emissions)
Summary of Input Parameters for the On-Site Spill
Scenario (Typical Emissions)
Summary of Input Parameters for the Mixing of
Incompatible Waste
Summary of Input Parameters for the Off-Site Spill
Scenario (Conservative Emissions)
Summary of Input Parameters for the Off-Site Typical
Spill Scenario (Typical Emissions)
Definition of Input Variables for SLAB Modeling
Summary of Air Dispersion Modeling Results
(On-site Spill)
Summary of Air Dispersion Modeling Results
(On-site Fire)
Summary of Air Dispersion Modeling Results
(On-site Mixing of Incompatible Wastes)
Summary of Air Dispersion Modeling Results
(Off-site Spill)
Summary of Air Dispersion Modeling Results
(Off-site Fire)
Average Vapor Mole Fraction Used in SLAB Modeling
Summary of ISC-COMPDEP Screening Results for the On-
Site Fire Scenario
Summary of ISC-COMPDEP Screening Results for the
Off-Site Fire Scenario
Maximum and Typical Phosgene and HC1 Concentrations
for the Conservative Unmitigated
On-site Fire Scenario
Maximum and Typical Phosgene and HC1 Concentrations
for the Conservative Off-site Fire Scenario
29
30
31
32
33
34
35
36
37
39
40
41
43
43
48
53
54
Volume VII
Appendix VII-4
External Review Draft
Do not cite or quote
-------
Table 18:
Table 19:
Table 20:
CONTENTS
(continued)
Maximum and Typical Phosgene and HC1 Concentrations
for the Conservative Mitigated On-site Fire Scenario 55
Average Emission Rates and Emission Duration for the Release Scenarios 56
Air Dispersion Modeling Results Based on Various Concentration Averaging
Time 57
FIGURES
Figure 1: Source Area for On-Site Spill 3129
Figure 2: Location for the Off-Site Spill 3230
Figure 3: Rate of Evaporation of 10% Formaldehyde/90% Methanol Liquid
Pool for the On-Site Spill Scenario (Conservative Emissions) 3331
Figure 4: Rate of Evaporation of 10% Acetone/90% Toluene Liquid Pool for
the On-Site Spill Scenario (Conservative Emissions) 3432
58
59
60
61
Attachment 1:
Attachment 2:
Attachment 3:
Attachment 4:
Attachment 5:
ATTACHMENTS
Program AIRCONC
SLAB Output for the On-Site Spill Scenario
Summary of Exposure Concentrations at Specific Receptor Locations
ISC-COMPDEP Output Using Screening Meteorology
ISC-COMPDEP Output Using Real-Tune Meteorology
Volume VII
Appendix VII-4
External Review Draft
Do not cite or quote
-------
I. ATMOSPHERIC DISPERSION MODELING
A. Model Selection
Atmospheric dispersion modeling of accidental releases is conducted using the
following approaches:
1. SLAB Model
SLAB is a computer model that simulates the atmospheric dispersion of denser-
than-air releases (Ermak 1990) and is one of the five refined models used in
developing guidance on the application of refined dispersion models to
hazardous/toxic air pollutant releases (U.S. EPA 1993). The model is capable of
modeling continuous, finite duration, and instantaneous releases from four types of
sources: 1) a ground level evaporating pool; 2) an elevated horizontal jet; 3) a stack
or elevated vertical jet; and 4) a ground-based instantaneous release. The SLAB
model is used to model the vapor releases for the WTI accident scenarios for the
following reasons:
• SLAB is a fully-documented model released by Lawrence Livermore
National Laboratory and listed by the U.S. EPA for use when modeling
hazardous/toxic air pollutant releases.
• SLAB simulates both neutral and denser-than-air releases.
• SLAB allows for continuous, finite duration, and instantaneous releases as
well as automatic transition of continuous plume into transient plume with
various time-averaged concentrations at the receptor locations.
Volume VII External Review Draft
Appendix VII-4 Do not cite or quote
-1-
-------
2. ISC-COMPDEP Model
The ISC-COMPDEP air dispersion model is used for modeling steady-state or
quasi-steady-state buoyant emissions resulting from accidents involving fire. It was
. previously modified to allow the use of wind and temperature data at multiple levels
derived from local meteorological observations at the WTI site (See Volume IV).
Selection of ISC-COMPDEP for modeling the off-site air concentrations resulting
from emissions from fire scenarios is based on the following considerations:
• The model is used in the WTI risk assessment report for modeling stack and
fugitive emissions from the facility;
• The model is capable of estimating off-site air concentrations in simple and
complex terrain; and
• The emissions associated with fire scenarios can be conservatively treated as
continuous buoyant plumes due to high temperature and strong mixing with
the entrained air.
B. Meteorological Data
For each identified accident scenario, off-site chemical concentrations in air are
evaluated for three meteorological conditions: 1) typical; 2) conservative; and 3)
calm/inversion. The modeling under each of these conditions is described below.
1. Typical Condition
Typical meteorological condition may be best represented by the real-time
meteorological data observed at the site. A hybrid hourly surface meteorological
data set, DEPBIN.MET, was developed mainly from wind data observed at the on-
site meteorological towers and supplemented with the data observed at other off-site
meteorological towers (the Beaver Valley Power Station meteorological tower and
the National Weather Service Station at the Greater Pittsburgh International
Airport) for ceiling height, cloud cover, and stability. The preprocessed data
contains 8,760 hourly entries of wind direction, wind speed, ambient temperature,
atmospheric stability, and mixing height (April 1992 through March 1993). It is used
in the air quality modeling of stack and fugitive emissions from the WTI facility (See
Volume IV).
Volume VII External Review Draft
Appendix VII-4 Do not cite or quote
-2-
-------
The typical meteorological condition is defined based on the most frequent
single type of stability conditions at the facility to provide a simplified approach to
estimate the average zone of impact if an accidental release were to occur. The
typical meteorological condition is defined as neutral atmosphere (Pasquill-Gifford
Stability Category D) with average wind speed (3.2 m/sec). Selection of this
condition to represent the typical meteorology for the accident analysis is based on
the hourly surface meteorological data recorded between April 1, 1992, and March
31, 1993, at the WTI facility, which indicates the following:
• The most common prevailing atmospheric stability at the WTI facility is stability
category D, which occurs approximately 57% of the time; the next most
common stability category is F/G, which occurs approximately 2.1% of the time.
• The average wind speed for non-calm hours at the WTI facility is 3.2 m/s.
The approach of using a typical condition is relatively simple because it assumes
a meteorology independent of wind direction and terrain elevation. While the
average zone of impact for a receptor could be direction-specific and terrain-specific,
it could alternatively be estimated using real-time meteorological conditions and site-
specific terrain elevations, averaging only the concentrations directly downwind of
the release. However, this would require advanced ISC-COMPDEP and SLAB air
modeling involving modification of the source codes. The advanced modeling is not
warranted given the range of meteorological conditions considered for each accident
scenario.
It should be emphasized that the radius of the zone impacted by an accidental
release is usually developed primarily for emergency planning purposes. During an
accident, the wind may suddenly change direction, thus affecting different off-site
populations. The use of a typical meteorological condition reflecting a combination
of average stability and wind speed is considered adequate for a screening
assessment to define an average zone of impact during an accident, independent of
the wind direction. The average zone of impact is presented in additional to the
maximum zone of impact, determined from the worst-case meteorological condition,
to assist the emergency planner in defining the radius of the impacted zone under
different meteorology regardless of the wind direction. This is consistent with the
guidance for estimating vulnerable zones to actual releases recommended by U.S.
EPA (1987) where it is suggested that emergency planners use a circle for fixed sites
Volume VII External Review Draft
Appendix VII-4 Do not cite or quote
-3-
-------
/"" " or a corridor for transportation routes when estimating vulnerable zones because
V _/ both wind speed and direction may change during the course of the release.
2. Conservative Condition
The screening meteorological conditions used in the SCREEN2 air dispersion
model (U.S. EPA 1992) are used for identifying the conservative meteorological
condition and for determining the maximum vapor concentration at each receptor.
The 54 combinations of atmospheric stability and wind speed used in'SCREEN2 for
determining the conservative off-site vapor concentrations are summarized in
Table 1. The conservative meteorological condition could be different for each
downwind distance depending upon other parameters (such as plume rise, receptor
downwind distance, source elevation, terrain elevation and receptor height) that
characterize the dispersion. By examining all 54 combinations of wind speed and
atmospheric stability, the maximum exposure concentration for each downwind
distance can be determined. The 54 combinations of atmospheric conditions are
considered to be more stringent than the conservative meteorological conditions
defined by various regulatory agencies in quantifying the maximum exposure
/-• --\ concentration for each downwind distance. For example, the screening meteorology
, covers the 1.5 m/sec, F-stability meteorology suggested in U.S. EPA's technical
guidance for hazards analysis (U.S. EPA 1987), and the 2 m/sec, F-stability
meteorology for ground-level and elevated releases affected by gravity or the 2
m/sec, A-stability meteorology for elevated, high flowrate, buoyant releases used in
the Toxic Catastrophe Prevention Act (TCPA) program in New Jersey (NJDEP
1993).
3. Calm/Inversion Condition
Ground-level vapor concentrations could be significantly increased during certain
meteorological conditions under which the plume is confined in the atmospheric
boundary layer. Limited mixing occurs when the vertical mixing of the plume with
the air is limited by a stable layer aloft. The worst meteorological condition during
an inversion for off-site receptors is a stagnation period (calm condition with no
winds) associated with a strong temperature inversion. During this period, air
contaminants would accumulate over the source area before being dispersed
downwind by light winds. In this Accident Analysis, the calm/inversion conditionis
defined as a stable atmosphere with little winds (Stability F and wind speed of 1
m/s) immediately after a long period of calm condition.
^.— -^'
Volume VII External Review Draft
Appendix VII-4 Do not cite or quote
-4-
-------
The calm/inversion meteorological condition represents one of the most stable
conditions that may occur at the WTI site. The hypothetical meteorology assumes
that a temperature inversion with conservative meteorology would occur after calm
hours. The limited mixing in the surface layer imposed by the temperature inversion
is represented by a mixing height of 100 m in the SLAB model and the conservative
meteorology is represented by the combination of low wind speed (1 m/sec) and
stable atmosphere (Monin-Obukov length of 8.3 m, approximately equivalent to
Pasquill-Gifford atmospheric stability of E or F based on the Liu-Durran regression
equation, as referenced by Randerson 1984). It is similar to the calm meteorological
condition previously evaluated in the routine stack and fugitive emissions study (See
Volume IV) where emissions during the calm hours were accumulated and released
at the end of the calm period.
It is assumed that vapor emissions due to a spill would accumulate over the spill
area during the calm hours and disperse slowly downwind in a confined stable
atmospheric boundary layer. The portion of emissions accumulated during the calm
hours would transport downwind, as soon as the atmospheric winds resume, as a puff
with the strength equal to the total emissions accumulated during the calm hours.
The spill area would continue to emit toxic vapors at the same emission rate as
previously calculated for the typical and conservative meteorology. The continuous
emissions, if there is sufficient quantity for further volatilization after the calm hours,
would travel downwind as a continuous plume. Based on a screening analysis, it was
determined that the worst off-site air impact would occur due to short duration (up
to 1 hour) of calm conditions. The screening analysis is provided in Section E.4.
Because ISC-COMPDEP does not simulate instantaneous or transient releases,
this type of meteorological condition is not modeled by ISC-COMPDEP. However,
the exposure concentrations under the calm/inversion condition may be qualitatively
addressed using the results obtained under the conservative non-inversion condition.
C. Dispersion Categories
Five release scenarios were identified in Appendix VII-3 for atmospheric dispersion
modeling in the accident analysis. Two emission conditions, conservative and typical,
were identified for each release scenario. The five dispersion categories identified in the
accident analysis are:
Volume VII External Review Draft
Appendix VII-4 Do not cite or quote
-5-
-------
• Categoiy 1: On Site Spill
(Conservative Emissions) - Spill of 5,000 gallons of liquid organic waste from
one tanker truck at the Organic Waste Tank Farm Truck Unloading Station area
within the WTI facility (Figure 1). The liquid organic waste is assumed to be
stored under atmospheric temperature and atmospheric pressure and contains
either formaldehyde or acetone at 100,000 ppm (10% by weight).
(Typical Emissions) - Spill of 100 gallons of the same waste at the same area.
• Category 2: On-site Fire
(Conservative Emissions) - Storage tank rupture and release of 20,000 gallons of
liquid organic waste over a finite time period in the Organic Waste Tank Farm,
followed by ignition of the released waste and a fire. Phosgene and HC1 are
assumed to be released as combustion products.
(Typical Emissions) - Spill of 200 gallons of the same waste ignites at the same
area.
• Categoiy 3: On-site Mixing of Incompatible Wastes
(Conservative Emissions) - Release of hydrogen chloride gas from the storage
vessel during an accident involving mixing of 10,000 gallons of incompatible
wastes (chlorinated hydrocarbons and mineral acids) a storage vessel. The
potential accident is assumed to occur at the tank storage area.
(Typical Emissions) - Release of hydrogen chloride gas resulting from mixing of
200 gallons of incompatible wastes, as described in Appendix VII-3.
• Category 4: Off-site Tanker Truck Spill
(Conservative Emissions) - Spill of 5,000 gallons of liquid organic waste over a
finite time period from an inbound tanker truck involved in an incident on the
local access route to the WTI facility (Figure 2). The liquid organic waste is
assumed to be stored under atmospheric temperature and atmospheric pressure
and contains either formaldehyde or acetone at 100,000 ppm (10% by weight).
(Typical Emissions) - The same accident scenario as the conservative emission
condition with a 100 gallon spill.
Volume VII External Review Draft
Appendix VII-4 Do not cite or quote
-6-
-------
• Category 5: Off-site Tanker Truck Spill With Fire
(Conservative Emissions) - Spill and subsequent ignition of 100 gallons of liquid
organic waste over a finite time period from an inbound tanker truck involved in
an incident on the local access route. Phosgene and HC1 are assumed to be
released as combustion products.
(Typical Emissions) - Spill of 100 gallons of liquid waste and subsequent ignition
of same at the same area.
Because it is anticipated that the on-site emergency team would be able to respond and
mitigate a spill/fire accident on-site in 10 to 60 minutes, additional evaluation of all on-
site accident scenarios is conducted assuming the fire/emission will be terminated in 10
or 60 minutes.
SLAB is used for modeling all release scenarios except the fire scenarios where
strong buoyancy plumes may impinge on elevated terrains farther away from the source
areas. Fire scenarios are modeled using the ISC-COMPDEP model.
D. Modeling Parameters
1. SLAB
The SLAB modeling analyses are conducted assuming dispersion would occur in
a suburban environment (for modeling purposes, this is defined by the surface
roughness). Tables 2 through 6 show the input parameters used in SLAB modeling.
The definition of each model parameter is presented in Table 7. Detailed
descriptions of these parameters can be found in the SLAB user's manual (Ermak
1990) and in U.S. EPA guidance on the application of refined models (U.S. EPA
1993). Specific modeling techniques requiring further discussions are provided
below.
• Source Area
The source area for the conservative on-site spill scenario (Dispersion
Category 1) is calculated to be 418 m2 for the conservative emission
condition, based on an area of 60 ft by 75 ft at the truck unloading station.
A spill volume of 5,000 gallons was determined to be the maximum release
quantity. For the typical on-site spill volume of 100 gallons, the area was
calculated to be 38 m2. The source area was represented by a square and
Volume VII External Review Draft
Appendix VII-4 Do not cite or quote
-7-
-------
positioned at the center of the area to the north of the Truck Unloading
Station.
Phosgene and HC1 emissions would result from the on-site fire scenario
(Dispersion Category 2). The area of emissions is assumed to be 180 m2
(1/4 of the Organic Waste Tank Farm area) for the conservative emission
condition. The source area is therefore represented by a square of 13.5 m
by 13.5 m, located at the Organic Waste Tank Farm area. For the typical
on-site spill of 200 gallons, the area is calculated to be 76 m2, assuming a
spill depth of 1 cm.
Hydrogen chloride emissions due to mixing of incompatible wastes
(Dispersion Category 3) are expected to be instantaneous as the chemical
reactions occur. HC1 emissions resulting from mixing of incompatibles are
expected to be vented through the vapor recovery system of the storage
vessel and the HC1 generation rate depends on the waste pumping rate.
The duration of release (20 minutes) is determined by the amount of time
required for emptying all of the contents of the tanker truck (5,000 gallons).
For a typical spill of 200 gallons of liquid waste, the duration is assumed to
be 10 minutes and the source area is calculated to be 76 m2.
The source area for the off-site spill (Dispersion Category 4) with
conservatively high emissions is calculated to be less than 1,900 m2, the area
of an unconfined spill is calculated using a spill depth of 1 cm (U.S. EPA
1992; U.S. EPA 1987) and a spill volume of 5,000 gallons. It is assumed that
the spill toward the two sides of the road will be either absorbed by soil or
collected by the storm sewage system and therefore only the spill along the
road will not be confined. The source is thus represented by a rectangular
road segment of 15 m by 49 m (approximately 735 m2 for the conservative
scenario). The width of the road (15 m) is calculated based on a typical
two-lane highway with shoulder on each side. The width of each lane or
road shoulder is assumed to be 3.65 m (12 ft) based on the standard design
of highway construction (Duttenhoeffer et al. 1983). The length of the
source area is determined to be the same as the characteristic length of an
unconfined spill of the same volume (the diameter of an unconfined spill).
For the typical release scenario, the area was calculated to be 38 m2.
Phosgene and hydrogen chloride gases would be generated due to a pool
fire. The source area for the off-site fire scenario (Dispersion Category 5) is
assumed to be the same as Dispersion Category 4. The source will be
Volume VII External Review Draft
Appendix VII-4 Do not cite or quote
-8-
-------
represented by a rectangular road segment of 15 m by 49 m (approximately
735 m2) for the conservative release scenario and 38 m2 for the typical
release scenario.
Source Temperature
For non-buoyant emissions (Dispersion Categories 1, 3, and 4), the source
temperatures are set equal to the ambient temperature. For emissions
associated with a fire (or potential heat release) scenarios (Dispersion
Categories 2 and 5), the scenario-specific source temperature is estimated, as
described in Appendix VII-3.
Source Height
The source height for mixing of incompatible wastes under the conservative
emissions scenario is assumed to be the height of the building vent plus an
additional height due to plume rise as the result of release gas momentum.
The effective stack height, h^, is calculated using the Holland formula
with the release temperature equal to the ambient temperature.
Ah
A* .
u
where:
Ah = plume rise (m);
v, = stack gas exit velocity (m/s);
u = ambient wind speed (m/s);
d = stack diameter (m).
The stack gas exit velocity is calculated as the volumetric flow rate divided
by the cross-sectional area of the stack to be 37 m/s. Therefore,
Volume VII External Review Draft
Appendix VII-4 Do not cite or quote
-9-
-------
= (37 m/,)(0.20 m)
(3.2 m/s)
Thus the release height is:
= 6.1 /» + 2.3 » = 8.4
Sources for all spill scenarios are assumed to be at ground level.
• Source Elevation
For all scenarios, it is assumed that there is no elevation difference between
the source and the receptors. For a ground-level source release, the
maximum exposure-point concentration will occur on the ground and within
a short distance from the source. Treating elevated terrain as flat terrain
would result in more conservative (or higher) exposure concentrations at the
off-site receptors.
• Receptor Locations
The SLAB model automatically computes volume concentrations at 61
downwind locations based on the maximum downwind distance specified by
the user. It does not calculate concentrations at specific downwind locations
because in the transient puff dispersion mode time is the independent
variable rather than the downwind distance. A FORTRAN program,
Program AIRCONC (Attachment A), is thus developed to linearly
interpolate concentrations at specific receptor locations using the 61 values
computed by SLAB. For the conservative release scenarios where the
impacts of the emissions are expected to extend further downwind, the
maximum downwind distance used in the SLAB model was assigned to
20,000 m such that concentrations at 24 hypothetical receptor locations (x =
25, 50, 100, 200, 300, 400, 500, 600, 700, 800, 900, 1,000, 1,250, 1,500, 1,750,
2,000, 2,250, 2,500, 3,000, 4,000, 5,000, 10,000, 15,000, 20,000 m) can be
interpolated. The maximum downwind distance is reduced to 5,000 m and
the hypothetical receptor locations are reduced to 21, excluding the
Volume VII External Review Draft
Appendix VIM Do not cite or quote
-10-
-------
receptors beyond 5,000 m, for the typical release scenarios to increase the
resolution of the model predictions.
• Receptor Height
All receptors are assumed to be at the ground level.
• Receptor Elevation
All receptors are assumed to be at the same elevation as the source.
• Surface Roughness Length
The surface roughness length is a measure of the roughness of a surface
over which air is flowing. For a homogenous surface, its value is sometimes
approximated as 1/10 of the average height of the surface irregularity.
When the landscape contains any obstructions (i.e., is nonhomogeneous), an
effective roughness length must be determined.
The overall effects of increasing surface roughness are to retard the
horizontal, buoyancy-induced spreading of the plume or cloud and to
enhance the mixing between plume and environment as a result of the
ambient and plume turbulence. Large surface roughness values could
significantly decrease modeled concentrations. For low or ground-level
releases, increasing the surface roughness value by a factor of 10 may result
in concentration reductions by a factor of 2 (Britter and McQuaid 1988).
The surface roughness length (z0) for urban areas are reported to be
between 100 cm and 600 cm, and was 60 cm and 80 cm for suburban
medium buildings (U.S. EPA 1985). For suburban residential dwellings, z0 is
found to be approximately 5 cm (U.S. EPA 1985). In the vicinity of grassy
areas or agricultural crop field, z0 varies from 4 cm to 20 cm (U.S. EPA
1985, 1993). Based on the combined surface protrusions in the vicinity of
WTI (suburban medium building, suburban residential dwellings, grassy with
agricultural crops), z0 is estimated to be between 10 cm and 50 cm.
Therefore, a median site-specific value of 30 cm, as used in the ISC-
COMPDEP modeling for routine emissions (See Volume IV), is selected for
the atmospheric dispersion modeling.
Volume VII External Review Draft
Appendix VII-4 Do not cite or quote
-11-
-------
Concentration Averaging Time
The concentration averaging time is set to be one-half hour, which is
consistent with the derivation of the Level of Concern (LOG) and
Immediately Dangerous to Life or Health (IDLH) acute toxicity criteria
used hi the accident analysis.
For instantaneous puff releases or releases with a duration of 5 minutes
or less, the peak average concentrations over time periods of up to one hour
depend not only on the averaging time but also on the ambient wind speed
and the instantaneous horizontal puff dispersion coefficient (U.S. EPA
1988). For continuous plume releases or releases with a duration of more
than 5 minutes, the concentration estimate follows a power relationship with
the averaging time. Using a power exponent of 0.2 suggested by U.S. EPA
(1988), a 15-minute average would be approximately 1.15 times greater than
the 30-minute average. Thus, an averaging time of 30 minutes represents an
averaging duration that is consistent with derivation of the health-based
reference concentrations (IDLH or LOG) used in this assessment and does
not significantly underestimate the concentrations when other short duration
(less than 30 minutes) acute toxicity criteria are applied.
Time-Varying Releases
Vapor emissions associated with unconfined releases are expected to be
time-varying and time-limited. The emission rates are expected to decrease
from their initial large emission rates due to chemical adsorption and
absorption onto soils or surfaces for unconfined releases and due to the
decrease of chemical content in the spilled solution for confined releases.
For unconfined spills, vapor emissions will be retarded because of the
reduction of quantity available for diffusion and the increased diffusion
pathways for chemical vapors to travel in the soil medium after the spills.
Time-varying emission rates are governed by chemical-specific properties
and site-specific conditions that are too complex to be incorporated in the
air dispersion analysis. The steady-state emission model discussed in
Appendix VII-3 is likely to underestimate the emission duration and
overestimate the emission rates. A pseudo steady-state approach using the
steady-state model for each time increment is developed for use in the
current assessment. This approach is discussed in detail in Appendix VII-3.
Volume VII External Review Draft
Appendix VII-4 Do not cite or quote
-12-
-------
• Building Wake Effect
The presence of buildings or structures increases the intensity of
atmospheric turbulence near an emission source. As a result, chemical
vapors are rapidly mixed with large volume of air at the source, and the
plume would travel downwind with wider vertical and horizontal spread but
lower concentration at the plume centerline than that for the same release
without nearby buildings. For a release that is confined within a
building/warehouse, chemical vapors escaping from the building would be
significantly less than the release. The current dispersion modeling
conservatively assumes that the release is in an open area without
considering the building wake effect (caused by the nearby structures) or
building confinement effect on the plume dispersion and, consequently,
overestimates the maximum downwind concentrations.
• Relative Humidity
The mean relative humidity at the WTI site is obtained from the historical
humidity data for Pittsburgh, Pennsylvania, complied by the U.S.
Department of Commerce (U.S. DOC 1993). An annual averaged relative
humidity of 68% is used in the SLAB modeling.
2. ISC-COMPDEP
The ISC-COMPDEP modeling analyses are conducted for the conservative on-
site and off-site fire scenarios. Typical fire scenarios are addressed using the
modeling results developed for the conservative scenarios, discussed in the following
section. Common modeling parameters, such as source size, fire temperature,
roughness length, are kept the same as used in SLAB modeling. Specific modeling
parameters requiring further discussions are provided below:
• Source Elevation
The elevation for the source area is obtained from the USGS topographical
maps of the region.
Volume VII External Review Draft
Appendix VII-4 Do not cite or quote
-13-
-------
Receptor Locations
A radial grid of receptors, the same as is used in the incinerator stack emission
modeling, is used in ISC-COMPDEP modeling. Receptors are placed in rings at
distances of 100, 200, 300, 400, 500, 600, 700, 800, 900, 1,000, 1,250, 1,500, 1,750,
2,000, 2,250, 2,500, 3,000, 4,000, 5,000, 7,500, 10,000, 15,000, 20,000, 30,000,
40,000, and 50,000 m from the source. Each receptor ring consists of 36
receptors located at 10° intervals.
Receptor Elevation
The terrain elevation for each receptor is determined from the USGS
topographical maps as the maximum terrain height located with a sector defined
as ± 5° on either side of the receptor including the area from the receptor ring
out to the next distant receptor ring.
For the analyses involving the hypothetical conservative and typical
meteorological conditions, the highest elevation among receptors of a fixed-
distance ring is selected to represent the receptor elevation of the receptor at
that downwind distance since the most elevated receptor would yield the
maximum concentrations for a given ring. This application implies that the
worst receptor elevation is used in addition to the conservative meteorological
condition in the ISC-COMPDEP dispersion analysis.
Concentration Averaging Time
The minimum concentration averaging time implied by ISC-COMPDEP is one
hour because ISC-COMPDEP is a continuous plume model, which does not
allow the use of various averaging time at receptors, and the duration for each
meteorological observation is one hour. However, concentrations of shorter
averaging time can be estimated from the 1-hour average using the peak to
mean concentrations observed for sampling periods from 3 minutes to about half
an hour. The concentration of shorter averaging time can be obtained as
(Turner 1967, U.S. EPA 1988):
where, C, = Concentration averaged over t,, (ppm);
Volume VII External Review Draft
Appendix VIM Do not cite or quote
-14-
-------
ts = the averaging tune (minutes);
Cj^ = the 1-hr average concentration (ppm); and
p = 0.2 (U.S. EPA 1988).
One notices the above equation only accounts for the plume meandering due to
wind direction and may not be applicable for puff or transient plume releases.
• Building Wake Effect
The building wake effect is considered in the on-site fire scenario because there
are large storage tanks located in the potential spill area. The building wake
effect is studied using the U.S. EPA Building Profile Input Program. Detailed
building information of the storage tanks is provided in Attachment 4. The
building wake analysis is discussed in Volume IV.
£. Results and Discussions
Attachment 2 presents the SLAB model output for the conservative and typical on-
site spill of formaldehyde and methanol. Complete SLAB model outputs are available
on two 3 1/2-inch floppy diskettes or can be reproduced using the input parameters
listed in Tables 2 through 6 and the public-accessible SLAB model. Attachment 3 shows
the computer outputs from AIRCONC which display the 30-minute average exposure
concentrations at specific receptor locations. Tables 8 through 12 summarize the impact
distances associated with each chemical of concern and release scenario. Concentration
estimates and associated modeling techniques are addressed below.
1. Initial Concentration
All release scenarios involving low volatility liquid spill are modeled in the
SLAB modeling as releases of the mixtures. The SLAB outputs are summarized as
volumetric concentrations of the initial mixtures. U.S. EPA's guidance on the
application of refined dispersion models for hazardous/toxic air releases suggests
that the SLAB results should be adjusted to account for the chemical-specific portion
of the release by multiplying the concentration results by the fraction of the chemical
in the initial vapor-phase concentration (U.S. EPA 1993). However, it should be
noted that the real emission rate from a spill will not be constant in time. Effects
such as cooling of the spill as a result of evaporation will suppress the emission rate.
Chemicals with higher evaporation potential will escape from the pool faster than
other chemicals but slow down as the residual concentration in the spill decreases.
Volume VII External Review Draft
Appendix VII-4 Do not cite or quote
-15-
-------
For volatile chemicals such as formaldehyde, the initial mole fraction in the vapor
phase is much greater than the mole fraction in the liquid. The mole fraction of
formaldehyde in vapor phase will decrease in time because the vapor pressure of
formaldehyde will decrease in the formaldehyde-depleted liquid as time increases.
Therefore, adjusting the concentration results by multiplying the results by the mole
fraction of chemical in the initial vapor-phase concentration would result in
significant overestimation of the total mass available in the liquid for emissions. The
algorithm developed in Appendix VII-3 is used to estimate the average mole fraction
of a chemical in vapor during an accidental release. The methodology is developed
from the principle of mass conservation and takes into consideration the fact that
chemicals with higher volatility will evaporate from the spill pool faster than
chemicals with lower volatility.
Figure 3 shows the mass evaporation rates of formaldehyde and methanol for a
conservative on-site spill scenario. According to the steady-state approach, the liquid
will emit the chemical mixture at a constant rate of 2.5 kg/sec for approximately
6,000 seconds (1 hour and 40 minutes) and the vapor contains approximately 80% of
formaldehyde and 20% of methanol throughout the emissions. This would result in
an overestimation of formaldehyde by approximately 8-fold since formaldehyde
initially constitutes only 10% of the liquid waste. By using the chemical-specific
time-varying emissions, the principle of mass conservation is preserved, as seen in
Figure 3 where the area under the formaldehyde emission curve that represents the
total mass of formaldehyde emitted is 10% of the total mass available in the liquid
waste, and the emission duration is predicted to last for approximately 3,000 seconds
(50 minutes). As shown in the figure, formaldehyde leaves the liquid much faster
than methanol and the time for the rest of methanol to evaporate is actually much
longer than the steady-state emission approach predicted due to the low volatility of
methanol. Figure 4 shows the time-varying acetone and toluene emission rates for a
conservative on-site spill scenario. Acetone leaves the liquid faster than toluene due
to its higher volatility.
The average mole fraction obtained for each chemical for each accident scenario
is used to convert the SLAB output of mixture concentrations to the desired
chemical concentrations. Table 13 summarizes the average mole fractions used for
estimating the chemical air concentrations.
Volume VII External Review Draft
Appendix VII-4 Do not cite or quote
-16-
-------
2. Ambient Temperature
The ambient temperature may have significant effect on hazardous releases.
The ambient temperature has a more significant effect on vapor emissions than air
dispersion. If the ambient temperature is above the boiling point of the mixture, the
liquid waste may flash rather than evaporate. In addition, increased ambient
temperatures would increase the evaporation rate of the liquid waste. The boiling
points for the liquid waste examined in this assessment are well above the room
temperature or the extreme high temperature of summer time in the area. The
maximum temperature for the Pittsburgh area is 103 °F (or 312 K) with a monthly
normal maximum of 83 °F (or 307 K), based on the historical climatic data published
by the U.S. DOC (1993). Hence, flashing, which can significantly increase the
emission rate and alter the air dispersion characteristics, is not expected to occur
during a spill accident. The monthly normal maximum is only approximately 5%
higher than the average ambient temperature used in the analysis (307 K vs 293 K)
and therefore the temperature effect on emission and air dispersion is not
considered significant.
3. Relative Humidity
The relative humidity can affect the dynamics of elevated jet release and alter
the plume height above the ground (U.S. EPA 1993). Higher humidity will increase
the water vapor content in the initial vapor concentration and slightly increase the
buoyancy effect of the plume. However, the increase in plume buoyancy is not
expected to be significant because the mole fraction of water vapor in the ambient
air could not exceed 0.7% based on the vapor pressure of H2O. Two SLAB
modeling runs are performed to examine the impact of relative humidity on plume
dispersion using identical meteorology and modeling parameters. It is found that the
off-site concentrations predicted by SLAB vary insignificantly (less than 1%) as the
relative humidity increases from 0 to 100%. Hence, the effect of relative humidity
on vapor emission and plume dispersion is considered negligible, particularly in the
greater Pittsburgh area where the. seasonal humidity average varies in a relatively
narrow range of 56 to 77%, with an average of 68% (U.S. DOC 1993).
4. Modeling Emissions Under Calm/Inversion Conditions
As discussed in Section II.B.3, emissions during the calm/inversion conditions
are modeled by superimposing the exposure concentration resulting from a puff
release to that from a continuous or transient plume release. In the SLAB
Volume VII External Review Draft
Appendix VII-4 Do not cite or quote
-17-
-------
modeling, only the puff model is conducted for releases that last for less than an
hour. For releases lasting more than an hour, it is assumed that the release would
accumulate for a maximum duration of one hour prior to the occurrence of
conservative meteorology (1 m/sec wind in a stable limited mixing layer). However,
releases resulting from fire scenarios under the calm/inversion conditions are not
studied due to the unavailability of appropriate models.
a. The Vapor Accumulation Time
The duration for vapors to accumulate during the calm hours is assumed to
be the actual emission time or a maximum of 1 hour. Although the calm
meteorological condition may occur at the WTI site for several consecutive
hours, one hour is selected to represent the duration that could possibly result in
the worst impact to the off-site community (with largest impact zone) based on
the following considerations:
• Although the mean motion of the atmospheric current ceases (or subsides to
less than 1 m/sec) during the calm hours, both lateral and vertical velocity
fluctuations (atmospheric turbulence) will continue to disperse the vapor
cloud accumulated above the spill. The atmospheric turbulence will
uniformly disperse the vapor cloud in all directions during the calm hours.
The average concentration within this cloud is expected to be high, but not
as high as the concentration at the center of an instantaneously released
puff.
The average concentration in the neutrally buoyant vapor cloud during a
one hour stagnation period can be estimated using the following
assumptions:
a turbulent intensity of 3% for both lateral and vertical velocity
fluctuations;
a virtual wind speed of 1 m/sec in a moderately stable atmosphere
for quantifying the atmospheric turbulence; and
homogeneous mixing of neutrally buoyant gases in all directions.
The value of 3% for the atmospheric turbulent intensity has been
referenced as a typical value ( = 1/30) in the literature (Tennekes and
Lumley 1972). A wind speed of 1 m/sec is selected to represent the wind
Volume VII External Review Draft
Appendix VII-4 Do not cite or quote
-18-
-------
conditions below which wind measurements are generally considered "calm".
The characteristic length scale (L) developed by the cloud in one hour can
be calculated to be:
= 0-03 x 1 m/sec x 3600 sec
= 108 m;
= minimum(Lbteral, 1^^ ^
= minimum (108 m, 100 m)
= 100 m.
Using these characteristic length scales, the average concentration of a stagnant
vapor cloud for acetone/toluene mixture for the conservative on-site spill
scenario can thus be estimated to be (acetone/toluene mixture is selected
because of the low volatility and potentially longer emission duration if not
mitigated):
C = 1674 kg/(108 m)2 (100 m)
= 1.44 x 10'3 kg/m3
= 594 ppm.
This value is approximately twice the concentration of 280 ppm a resident
residing approximately 100 meters directly downwind of the spill would be
exposed to in less than 2 minutes during the low wind stable condition. The size
of the vapor cloud will continue to grow as time increases and the average
concentration within the cloud will continue to decrease since the increase in
volume outgrows the increase hi emissions. Therefore, if the calm condition
persists for another hour, the average concentration within the 200 meter radius
area would be approximately 150 ppm, slightly more than the 120 ppm
concentration 200 meters downwind of the source during the stable low wind
condition.
• As indicated in Equation (11) of Appendix VII-3, emissions from a liquid
spill during the calm condition could be significantly overestimated because
without the atmospheric current the vapors accumulated above the liquid
pool will significantly reduce the evaporation potential of the liquid. Indeed,
Equation (11) of Appendix VII-3 is not applicable to the calm condition
Volume VII External Review Draft
Appendix VIM Do not cite or quote
-19-
-------
/ " since it predicts zero emissions from the pool. Nevertheless, Equation (11)
\, ^ of Appendix VII-3 is used in conjunction with an average wind speed at the
WTI site to provide conservative emission estimates for the calm condition
defined in this assessment. The emission rates during calm hours are
obviously overestimated by applying this emission model with an average
wind speed. The total emissions from the liquid pool during the calm
condition could be unrealistically overestimated if the emissions' are allowed
to continue for a long period of time. A reasonable cut-off time is therefore
assumed to be 1 hour.
• Due to the size of the vapor cloud developed by the spill during the calm
hours, although much simplified without considering the density effect, the
emissions will be rapidly dispersed when the atmospheric current resumes
after a period of calm hours.
In addition, the initial dilution during the calm hour can not be simulated in
the SLAB model and, therefore, the accumulated vapor is released in the model
f x as a highly concentrated puff, which may result in unrealistic overestimation for
v the off-site exposure concentration estimates, particularly when the conservative
meteorology is used to represent the resumed wind conditions. A long
accumulation duration would result in misrepresentation of the source size in
SLAB modeling.
While the conservative meteorology defines a very narrow area (an elliptic-
shape area) along the prevailing wind direction that may be impacted by a
release, the above calculation for calm condition does not necessarily define a
smaller impact zone than the conservative meteorology. It simply indicates that
an area of approximately 100 m in radius will be impacted by an average
concentration of 594 ppm regardless of wind direction, which can actually be
larger than the elliptic-shape impact zone defined by the conservative
meteorology.
5. Distances to LOG and IDLH Concentrations
It is desirable to identify the region that could be exposed to concentrations
greater than 1 x LOG or 1 x IDLH for the chemicals of concern. This is handled by
Program AIRCONC such that the maximum distance from the source area to 1 x
Volume VII External Review Draft
Appendix VII-4 Do not cite or quote
-20-
-------
LOG or 1 x IDLH is calculated. Tables 8 through 12 show the maximum distances
from the source area to 1 x LOG and 1 x IDLH for the five release scenarios.
6. Modeling Emissions from Conservative Fires Using ISC-COMPDEP
The ISC-COMPDEP was used for modeling emissions from conservative fires
based on two assumptions:
• The denser-than-air toxic vapors would rapidly mix in the fire with the entrained
air such that the density of the gas mixture is approximately the same as air; and
• The plume would rise significantly and impact elevated receptors due to the
buoyancy flux generated by the fire.
Emissions from a fire are simulated as emissions from a stack. The flame height
is used to represent a virtual stack height of the emissions and the area of the fire is
used to characterize the size of the virtual stack. An effective stack velocity is
derived for the emissions using the buoyancy flux calculated in Appendix VII-3 and
Brigg's equation (Briggs 1975). The modeling parameters are listed in Attachment 4.
Complete ISC-COMPDEP model outputs are available on a 3.5" floppy diskette.
a) ISC-COMPDEP Modeling Results for Conservative Meteorological
Condition
The one-hour average concentrations predicted by the ISC-COMPDEP
model for each of the 54 screening meteorological conditions is presented in
Table 14 for the on-site accidental release scenario. The concentrations are
based on a unit emission rate (i.e., 1 g/s). The highest concentration of 63.4
|u,g/m3 is predicted under low wind speed stable conditions (1.0 m/s, F stability).
Low wind speed conditions result in lower plume dilution rates, and the stable
atmospheric lapse rate assumed during F stability conditions reduces the plume
rise associated with the buoyant source. The highest concentrations are
predicted at a distance of 800 meters from origin of the receptor grid, which is
centered at the WTI incinerator stack. The second highest concentrations are
predicted under moderate wind-speed neutral conditions (5 m/s, D stability). In
general, concentrations predicted during unstable (daytime) conditions are much
lower than the peak values predicted under the stable and neutral conditions.
Volume VII External Review Draft
Appendix VII-4 Do not cite or quote
-21-
-------
Table 15 shows the predicted concentrations for the off-site accidental fire
scenario. The highest predicted concentrations are predicted during E and F
stability conditions. The peak concentration of 218 ng/m3 is predicted under 2.5
m/s winds with F stability. The concentrations under unstable conditions are
typically an order of magnitude lower than those predicted during the
conservative stable conditions.
b) ISC-COMPDEP Modeling Results for Typical Meteorological Condition
The one-hour average concentrations predicted by the ISC-COMPDEP
model for conservative on-site fire scenario under the typical meteorological
condition are contained in Table 14. The concentrations for the typical
meteorological condition can be obtained by taking the average of the
concentrations for the 3.0 m/sec D-stability condition and the 3.5 m/sec D-
stability condition. The one-hour average concentrations predicted by the ISC-
COMPDEP model need to be converted to 30-minutes averages for comparison
with the health-related reference concentrations. The 30-minute average
concentration can be obtained by multiplying the ISC-COMPDEP results by a
factor of 1.15 using the equation presented in Section D.2 of this appendix:
(60/30)02 = 1.15
Tables 16 and 17 shows the 30-minute average concentration at each downwind
distance for the on-site and off-site fire scenarios, respectively. The mass
concentrations are converted to volumetric concentrations and compared to the
respective LOC and IDLH concentrations. It is shown in Table 9 that the off-site air
concentrations would not exceed any LOC concentrations with one exception - under
the conservative meteorological condition, there will be areas impacted by the
emissions exceeding the LOC concentrations. Tables 9 lists the zone that may
contain pocket areas with concentrations exceeding the LOC. For example, the off-
site concentrations at locations 675 to 1,125 m downwind of the WTI facility may
exceed the LOC concentrations during an on-site fire scenario. However, because
the ISC-COMPDEP model is used with the conservative receptor elevation,
discussed in Section D.2, in conjunction with the conservative meteorology, a
receptor which is within 675 to 11,25 m downwind of the spill but is located on a
terrain with elevation less than the identified conservative terrain may not be
Volume VII External Review Draft
Appendix VII-4 Do not cite or quote
-22-
-------
impacted by the LOG concentration or, if impacted, may have a very small impact
radius.
For the off-site fire scenario, a few pocket areas located up to 2100 m downwind
of the fire may be exposed to concentrations exceeding the LOG concentrations
under the conservative meteorological condition. As discussed above, these pocket
areas are the areas with high terrain elevations and may have small impact zones.
7. Interpreting ISC-COMPDEP Results to a 10-min Release Scenario
Emissions from an on-site fire are assumed to be terminated/controlled 10
minutes after the occurrence by either the emergency response team or any of the
activated mitigation devices on-site. The 60-minute average concentration resulting
from a 10-minute fire is estimated to be 1/6 of that resulting from a 1-hour fire.
Therefore, the 30-minute average concentrations resulting from a 10-minute on-site
fire can be estimated from the ISC-COMPDEP results by multiplying the results by a
scaling factor of 1/6 to account for the shorter release time at the source and by a
scaling factor of 1.15 to account for the shorter averaging time at the receptor.
Table 18 summarizes the estimated 30-minute average off-site concentrations
resulting from a 10-minute on-site fire. Due to the unpredictability in the location,
time, and accessibility of an off-site fire accident and in the availability of a local
emergency response team and in the effectiveness of the available mitigation
reagents/devices, the off-site fire scenario is considered to be uncontrollable within
an hour.
Based on the 30-minute average off-site concentrations estimated for the 10-
minute on-site fire scenario, no residents will be impacted with concentrations
exceeding either the LOG or IDLH concentrations.
8. Modeling Emissions from Typical Fires Using the ISC-COMPDEP Output for
Large Fires
Because the ISC-COMPDEP results for the conservative fire scenarios are
derived based on a unit emission rate and some physical characteristics of a large
fire, the results can be applied to the typical fire scenarios to yield conservative
concentration estimates.
As indicated in Appendix VII-3, the parameters used in characterizing emissions
from a fire are the flame height, emission rate, buoyancy flux, flame temperature
and time of burning. The exposure concentration can be easily adjusted based on
the emission rate since the exposure concentration is proportional to the emission
Volume VII External Review Draft
Appendix VII-4 Do not cite or quote
-23-
-------
rate. The effective stack exit velocity derived from the buoyancy flux, fire size, and
Brigg's equation (Briggs 1975) for the typical fire is the same as the large fire. The
plume rise caused by the small fire is somewhat less than the large fire due to lower
buoyancy flux and flame height. However, the impact of this difference is not
expected to be significant. The flame temperature is the same for both large and
small fire while the time of burning (release) for a small fire is less than large fire.
The 30-minute average emission rates of HC1 and phosgene for the typical fire
scenarios are at least 20 times less than the 30-minute average emission rates for
conservative fire scenarios, and the underestimation of using a slightly larger plume
rise for the typical fire scenarios is not expected to cause order-of-magnitude
underestimation of the off-site concentrations. Therefore, it is safe to say that the
off-site impacts caused by typical fire scenarios are at least one order-of-magnitude
(10 times) less than the off-site concentrations caused by conservative fire scenarios.
It is thus concluded and shown in Tables 9 and 12, based on the low off-site
concentrations predicted for the conservative fire scenarios and the low emission
rates calculated for the typical fire scenarios, that the off-site impacts caused by
typical fire scenarios will not exceed either the LOC or IDLH concentrations for
HC1 and phosgene.
9. ISC-COMPDEP Modeling Results Using 1-yr Real-time Meteorological Data
The ISC-COMPDEP model is used in conjunction with one-year of site-specific
hourly surface meteorological data (DEPBIN.MET) to evaluate the results predicted
by the same model using the screening meteorology. Both 1-hr and annual average
concentrations are calculated and summarized in Attachment 5.
For the on-site fire scenario, the grid receptors indicate that the maximum 1-hr
average concentration occurs at a distance approximately 300 m northeast of the
incinerator with a concentration coefficient of 100.3 ug/m3/(g/sec), compared to 64.4
Hg/m3/(g/sec) at a distance 800 m downwind of the facility predicted with the
conservative meteorology. The difference is attributed to the receptor elevations
used in the two analyses. For a buoyant plume release with significant plume rise,
the concentration at a receptor close to the source is heavily affected by the terrain
elevation. A polar grid system with previously determined terrain elevations
centered at the incinerator stack, available from the routine and fugitive emission
analysis (See Volume IV) is used in the ISC-COMPDEP modeling with real-time
meteorological data. For the ISC-COMPDEP run with the screening meteorology,
Volume VII External Review Draft
Appendix VII-4 Do not cite or quote
-24-
-------
however, the grid system is relocated to the center of the spill and the receptor
elevations are redefined.
Based on the use of real-time meteorology, IDLH values are not predicted to be
exceeded for the on-site fire scenario. Only pocketed areas located within 1000 m
downwind of the facility are predicted by the ISC-COMPDEP run with real-time
meteorology to exceed the LOC concentration for HC1, compared to an impact zone
of approximately 1,100 m downwind of the facility predicted by the ISC-COMPDEP
run with conservative meteorology. Off-site phosgene concentrations are found to be
less than the LOC concentration with one exception at an elevated individual
receptor where the concentration is approximately the same as the LOC
concentration.
The annual average off-site air concentrations for the on-site fire scenario are
also presented in Attachment 5. These concentrations should not be compared to
the off-site concentrations predicted using the typical meteorological condition
because the annual average concentration at a specific receptor is obtained by
averaging the hourly air concentrations at the receptor regardless of the wind
direction. Hence, the annual average concentration at a receptor could be
significantly less than the hourly concentration obtained when the receptor is
downwind of the source.
For the off-site fire scenario, the ISC-COMPDEP run with real-time
meteorology indicates that the maximum 1-hr average concentration occurs 1000 m
west of the facility (or approximately 100 m west of the fire) with a concentration
coefficient of 102.8 ug/m3/(g/sec), compared to 218 ng/m3/(g/sec) at a distance 100
m off the fire predicted by the ISC-COMPDEP run with conservative meteorology.
The difference is again attributed to the difference in terrain elevation used in the
two analyses. The impacted zone that may exceed the LOC concentration for HC1
extends from the fire to approximately 3,000 m, east of the facility, consistent with
that predicted by the conservative meteorology.
10. Modeling Emissions from Mixing of Incompatible Waste
In the current SLAB modeling, HC1 releases from mixing of incompatible waste
are simulated as dense plume stack release which may have overestimated the initial
slumping of the release and resulted in higher exposure concentration estimates.
Volume VII External Review Draft
Appendix VII-4 Do not cite or quote
-25-
-------
/- N
11. Concentration Averaging Time at Receptors
The concentration averaging time should be the appropriate averaging time for
the health and safety standard of interest. For comparison with the IDLH
concentrations, the averaging time is selected to be 30 minutes. However, it is
desirable to find out the averaging concentrations for periods less than 30 minutes. •
For a continuous plume, the concentrations downwind of a source generally
decrease with increasing averaging time due to the increased meandering of wind
direction (Turner 1967). The decrease in concentration follows a one-fifth power
law with the averaging time for averaging periods from about 3 minutes to about 30
minutes (Steward et al, as cited by Turner 1967). Studies also indicate the power
law exponent could vary between 0.17 and 0.2 and the power law relationship could
be applied to averaging times up to 24 hours (Turner 1967). Based on the one-fifth
power law relationship, a 15-minute average concentration will be approximately
15% greater than a 30-minute average. This magnitude of concentration increase is
considered relatively insignificant and does not transfer into any meaningful increase
in the development of the zone/distance impacted by the release. Releases last for
more than one hour are normally treated as continuous plume and the concentration
averaging time does not have any significant impacts on the off-site air
concentrations as well as the radius of impacted zone. It is shown in Table 19 that
the releases due to acetone/toluene spills can be treated as continuous plume based
on the emission duration, and therefore the difference between a 30-minute average
and a 10-minute average is not considered significant.
For a continuous finite-duration release, the average concentration will be
reduced from the peak concentration if the averaging time is greater than the source
release time because the release is relatively short and the receptor is exposed to the
material for only a fraction of the concentration averaging time. For receptors
located within a short distance downwind of the source (e.g., 1 km downwind of the
source), the exposure time is approximately the same as the source release time.
Therefore, a 10-minute average concentration could be 3 times higher than a 30-
minute average concentration if the release duration is only 10 minutes and the
receptor is located close to the release. Accordingly, the distance, based on the 10-
minute average concentration, to the IDLH concentration will be greater than that
defined by the 30-minute average concentration. Table 20 shows the distances to
IDLH and LOG concentrations for two emission scenarios. The averaging time is
set to be the same as the release duration. It is observed from Table 20 that the
maximum distance to the LOG concentration for formaldehyde increases by 2.5-fold
Volume VII External Review Draft
Appendix VII-4 Do not cite or quote
-26-
-------
(from 100 m to 240 m downwind) when the averaging time decreases from 30
minutes (1800 seconds) to 11.5 minutes (680 seconds). However, the cloud duration
increases as the cloud moves farther away from the spill. Therefore a receptor
located 1,000 m downwind of a 10 minute release would be exposed to the cloud for
approximately twice the duration of the release, longer than the release time. The
difference in concentration caused by the averaging time for such a receptor
becomes less significant than that for a receptor located nearby the release. Table
20 shows that the distance to either LOG or IDLH concentration increases by less
than 50% for the receptors farther away from the spill.
If the release is instantaneous or very short, it is difficult to estimate the cloud
length and cloud duration (Ermak 1990). A comparison of the concentration
averaging time and the cloud duration can only be made by additional dispersion
modeling. It is found from the SLAB modeling that the cloud duration for a puff
release (under calm/inversion condition) is 305 seconds near the source. As the
cloud moves farther downwind the cloud duration is expected to increase. A
receptor located at least 1,000 m downwind of the release would be exposed to the
elongated cloud for a period much greater than 305 seconds. Therefore, the
maximum distance that already extends to 10 km from the release is not expected to
increase much if the concentration averaging time is decreased from 30 minutes to
10 or less minutes.
12. Unconfmed On-site Spill
The size of the on-site spill scenario dictates the zone that could be impacted by
the release. The larger the source area is the higher the downwind concentration
will be. This could happen if a spill occurs on site at areas outside the berms. The
source area for such an unconfined release scenario would be approximately 4.5
times greater than the area confined by the berms, based on the assumption that the
spill will form a liquid pool of 1 cm in depth. A sensitivity analysis is performed to
examine the distance to the IDLH concentration for the on-site spill scenario.
For the formaldehyde/methanol spill, the distance to the IDLH concentration
increases slightly for the unmitigated release. Under the typical meteorological
condition, the distance to the LOG concentration increases from 1,000 m (for the
confined release) to 1,500 m, and from 640 m to 980 m for the IDLH concentration.
Under the conservative meteorological condition, the distance increases from
8,190 m to 8,400 m for LOG, and from 4,800 m to 5,000 m for IDLH. If the release
were to be put out within 10 minutes after the spill under the typical meteorological
Volume VII External Review Draft
Appendix VII-4 Do not cite or quote
-27-
-------
condition, the distance to the LOG concentration would be 1,500 m, or 980 m to the
IDLH concentration. Under the conservative meteorological condition, the distance
to the LOG concentration would be 8400 m, or 5000 m to the IDLH concentration.
The slight increase is due to the following two facts:
• The off-site concentration increases as the source area increases; and
• For the same concentration averaging time at the receptor, the off-site
concentration decreases as the emission duration decreases.
For the acetone/toluene spill, the distance to either the IDLH concentration or
the LOG concentration is less than 25 m, measured from the source area, for both
typical and conservative meteorological conditions.
01-3999C:PCCOOB83.W51
Volume VII External Review Draft
Appendix VII-4 Do not cite or quote
-28-
-------
TABLE 1
Stability Wind Speed Combinations Used
to Determine the Conservative Meteorological Conditions
Atmospheric
Stability
Categories
A
B
C
D
E
F
Wind Speed (m/s)
1
*
*
*
*
#
*
1.5
*
*
*
*
*
*
2
*
*
*
*
*
*
2.5
*
*
*
*
*
*
3
*
*
*
*
*
*
3.5
*
*
*
*
*
4
*
*
*
*
*
4.5
*
*
*
*
5
*
*
*
*
8
*
*
10
*
*
15
*
20
*
Note:
* It is only necessary to consider the stability-wind speed conditions marked with an asterisk.
Volume VII
Appendix VII-4
External Review Draft
Do not cite or quote
-29-
-------
TABLE 2
Summary of Input Parameters for
the On-Site Spill Scenario (Conservative Emissions)
Run No.:
Modeling Parameter1
IDSPL
NCALC
WMS
CPS
TBP
CMEDO
DUE
CPSL
RHOSL
SPB
SPC
TS
QS
AS
TSD
QTIS
HS
TAV
XFFM
Meteorology
1
1
1
0.03188
909.8
309.35
0
1070000
2716
793.7
-1
0
293
1.04
418
3120
0
0
1800
20000
Typical
2
1
1
0.03188
909.8
309.35
0
1070000
2716
793.7
-1
0
293
1.99
418
600
0
0
1800
20000
Typical
3
1
1
0.03188
909.8
309.35
0
1070000
2716
793.7
-1
0
293
1.04
418
3120
0
0
1800
20000
Conservative
4
1
1
0.03188
909.8
309.35
0
1070000
2716
793.7
-1
0
293
1.99
418
600
0
0
1800
20000
Conservative
5
4
1
0.03188
909.8
309.35
0
1070000
2716
793.7
-1
0
293
0
418
.0
3244.8
0
1800
20000
Calm/Invers
ion
6
4
1
0.03188
909.8
309.35
0
1070000
2716
793.7
-1
0
293
0
418
0
1194
0
1800
20000
Calm/Inver
sion
7
1
1
0.08704
1204
367.5
0
375000
1781.5
861.3
-1
0
293
0.465
418
18240
0
0
1800
20000
Typical
8
1
1
0.08704
1204
367.5
0
375000
1781.5
861.3
-1
0
293
0.712
418
600
0
0
1800
20000
Typical
9
1
1
0.08704
1204
367.5
0
375000
1781.5
861.3
-1
0
293
0.465
418
18240
0
0
1800
20000
Conservative
10
1
1
0.08704
1204
367.5
0
375000
1781.5
861.3
-1
0
293
0.712
418
600
0
0
1800
20000
Conservative
11
4
1
0.08704
1204
367.5
0
375000
1781.5
861.3
-1
0
293
0
418
0
1674
0
1800
20000
ersion
12
4
1
0.08704
1204
367.5
0
375000
1781.5
861.3
-I
0
293
0
418
0
427.2
0
1800
20000
rsion
Note:
1 See TABLE 7 for definition.
Volume VII
Appendix VII-4
-30-
Extcrnal Review Drafl
Do not cite or quote
-------
TABLE 3
Summary of Input Parameters for
the On-Site Spill Scenario (Typical Emissions)
Run No.:
Modeling
Parameter1
IDSPL
NCALC
WMS
CPS
TBP
CMEDO
DHE
CPSL
RHOSL
SPB
SPC
TS
QS
AS
TSD
QTIS
HS
TAV
XFFM
Meteorology
13 | 14
1
1
0.03188
909.8
309.35
0
1070000
2716
793.7
-1
0
293
0.094
37.9
680
0
0
1800
5000
Typical
1
1
0.03188
909.8
309.35
0
1070000
2716
793.7
-1
0
293
0.10
37.9
600
0
0
1800
5000
Typical
15
1
1
0.03188
909.8
309.35
0
1070000
2716
793.7
-1
0
293
0.094
37.9
680
0
0
1800
5000
Conservative
16
1
1
0.03188
909.8
309.35
0
1070000
2716
793.7
-1
0
293
0.10
37.9
600
0
0
1800
5000
Conservative
17
4
1
0.03188
909.8
309.35
0
1070000
2716
793.7
-1
0
293
0
37.9
0
63.92
0
1800
5000
Calm/Inve
rsion
18
4
1
0.03188
909.8
309.35
0
1070000
2716
793.7
-1
0
293
0
37.9
0
60.0
0
1800
5000
Calm/Inve
rsion
19
1
1
0.08704
1204 .
367.5
0
375000
1781.5
861.3
-1
0
293
0.042
37.9
3960
0
0
1800
5000
Typical
20
1
1
0.08704
1204
367.5
0
375000
1781.5
861.3
-1
0
293
0.06
37.9
600
0
0
1800
5000
Typical
21
1
1
0.08704
1204
367.5
0
375000
1781.5
861.3
-1
0
293
0.042
37.9
3960
0
0
1800
5000
Conservative
22
1
1
0.08704
1204
367.5
0
375000
1781.5
861.3
-1
0
293
0.06
37.9
600
0
0
1800
5000
Conservative
23
4
1
0.08704
1204
367.5
0
375000
1781.5
861.3
-1
0
293
0
37.9
0
151.2
0
1800
5000
Calm/Inve
rsion
24
4
1
0.08704
1204
367.5
0
375000
1781.5
861.3
-1
0
293
0
37.9
0
36
0
1800
5000
Calm/Inversion
Note:
1 See TABLE 7 for definition.
Volume VII
Appendix VII-4
External Review Draft
Do not cite or quote
-------
TABLE 4
Summary of Input Parameters for
the Mixing of Incompatible Waste
Emissions
Run No.:
Modeling
Parameter1'1
IDSPL
NCALC
WMS
CPS
TBP
CMEDO
DHE
CPSL
RHOSL
SPB
SPC
TS
QS
AS
TSD
QTIS
HS
TAV
XFFM
Meteorology
Conservative
49
3
1
0.03647
797.812
188.15
0
441459
1655.85
1187
-1
0
293
1.79
0.0324
1200
0
8.4
1800
20000
Typical
50
3
1
0.03647
797.812
188.15
0
441459
1655.85
1187
-1
0
293
1.79
0.0324
600
0
8.4
1800
20000
Typical
51
3
1
0.03647
797.812
188.15
0
441459
1655.85
1187
-1
0
293
1.79
0.0324
1200
0
8.4
1800
20000
Conservative
Notes:
1 Properties of HC1.
2 See TABLE 7 for definition.
52.
3
1
0.03647
797.812
188.15
0
441459
1655.85
1187
-1
0
293
1.79
0.0324
600
0
8.4
1800
20000
Conservative
53
4
1
0.03647
797.812
188.15
0
441459
1655.85
1187
-1
0
293
0
167.6
0
2148
8.4
1800
20000
Calm/Invers
ion
54
4
1
0.03647
797.812
188.15
0
441459
1655.85
1187
-1
0
293
0
83.8
0
1074
8.4
1800
20000
Calm/Inve
rsion
Typical
55
1
1
0.03647
797.812
188.15
0
441459
1655.85
1187
-1
0
293
0.0714
75.71
600
0
0
1800
5000
Typical
56
1
1
0.03647
797.812
188.15
0
441459
1655.85
1187
-1
0
293
0.0714
75.71
600
0
0
1800
5000
Typical
57
1
1
0.03647
797.812
188.15
0
441459
1655.85
1187
-1
0
293
0.0714
75.71
600
0
0
1800
5000
Conservative
58
1
1
0.03647
797.812
188.15
0
.441459
1655.85
1187
-1
0
293
0.0714
75.71
600
0
0
1800
5000
Conservative
59
4
1
0.03647
797.812
188.15
0
441459
1655.85
1187
-1
0
293
0
75.71
0
42.84
0
1800
5000
Inversion/
Calm
60
4
1
0.03647
797.812
188.15
0
441459
1655.85
1187
-1
0
293
0
75.71
0
42.84
0
1800
5000
Inversion/
Calm
Volume VII
Appendix VII-4
-32-
Extcrnal Review Draft
Do not cite or quole
-------
TABLES
Summary of Input Parameters for
the Off-site Spill Scenario (Conservative Emissions)
Run No.:
61
62
63
Modeling Parameter*
IDSPL
NCALC
WMS
CPS
TBP
CMEDO
DHE
CPSL
RHOSL
SPB
SPC
TS
QS
AS
TSD
QTIS
HS
TAV
XFFM
Meteorology
1
1
0.03188
909.8
309.35
0
1070000
2716
793.7
-1
0
293
1.84
735.0
1740.0
0
0
1800
20000
Typical
1
1
0.03188
909.8
309.35
0
1070000
2716
793.7
-1
0
293
1.84
735.0
1740.0
0
0
1800
20000
Conservative
4
1
0.03188
909.8
309.35
0
1070000
2716
793.7
-1
0
293
0
735.0
0
3201.6
0
1800
20000
Calm/Inversion
64
1
1
0.08704
1204
367.5
0
375000
1781.5
861.3 ,
-1
0
293
0.818
735.0
10320
0
0
1800
20000
Typical
65
66
1
1
0.08704
1204
367.5
0
375000
1781.5
861.3
-1
0
293
0.818
735.0
10320
0
0
1800 .
20000
Conservative
4
1
0.08704
1204
367.5
0
375000
1781.5
861.3
-1
0
293
0
735.0
0.0
2944.8
0
1800
20000
Calm/Inversion
Note:
1 See TABLE 7 for definition.
Volume VII
Appendix VII-4
External Review Draft
Do not cite or quote
i
-------
TABLE 6
Summary of Input Parameters for
the Off-site Typical Spill Scenario (Typical Emissions)
Run No.:
67
68
69
70
71
72
Modeling Parameter1
rospL
NCALC
WMS
CPS
TBP
CMEDO
DHE
CPSL
RHOSL
SPB
SPC
TS
QS
AS
TSD
QTIS
HS
TAV
XFFM
Meteorology
1
1
0.03188
909.8
309.35
0
1070000
2716
793.7
-1
0
293
0.094
37.9
680
0
0
1800
5000
Typical
1
1
0.03188
909.8
309.35
0
1070000
2716
793.7
-1
0
293
0.094
37.9
680
0
0
1800
5000
Conservative
4
1
0.03188
909.8
309.35
0
1070000
2716
793.7
-1
0
293
0
37.9
0
63.92
0
1800
5000
Calm/Inversion
1
1
0.08704
1204
367.5
0
375000
1781.5
861.3
-1
0
293
0.042
37.9
3960
0
0
1800
5000
Typical
1
1
0.08704
1204
367.5
0
375000
1781.5
861.3
-1
0
293
0.042
37.9
3960
0
0
1800
5000
Conservative
4
1
0.08704
1204
367.5
0
375000
1781.5
861.3
-1
0
293
0
37.9
0
151.2
0
1800
5000
Calm/Inversion
Note:
1 See TABLE 7 for definition.
Volume VII
Appendix VII-4
-34-
External Review Draft
Do not cite or quote
-------
TABLE?
Definition of Input Variables for SLAB Modeling
- IDSPL
- NCALC
Source Properties
- WMS
- CPS
- TBP
- CMEDO
- DHE
- CPSL
- RHOSL
- SPB
- SPC
Spill Parameters
- TS
- QS
- AS
- TSD
- QTIS
- HS
Field Parameters
- TAV
- XFFM
- ZP(I)
Source Type and Numerical Substep Parameter
Spill source type
1 - evaporating pool release
2 - horizontal jet release
3 - vertical jet or stack release
4 - instantaneous or short duration evaporating pool release
Numerical substep parameter
Molecular weight of source material (kg)
Vapor heat capacity at constant pressure (J/kg-K)
Boiling point temperature (K)
Initial liquid mass fraction
Heat of vaporization (J/kg)
Liquid heat capacity (J/kg-K)
Liquid density of source material (kg/M3)
Saturation pressure constant (Default: SPB = -1.0)
Saturation pressure constant (Default: SPC = 0.0)
Temperature of source material (K)
Mass source rate (kg/S)
Source area (M2)
Continuous source duration (s)
Instantaneous source mass (kg)
Source height (M)
Concentration averaging time (s)
Maximum downwind distance (M)
Heights of concentration calculation (M); I = 1, 4
Volume VII
Appendix VII-4
External Review Draft
Do not cite or quote
-35-
-------
TABLE 8
Summary of Air Dispersion Modeling Results (On-site Spill)
Run
No.
1
2
3
4
5
6
7
8
9
10
11
12
13
14
15
16
17
18
19
20
21
22
23
24
Chemical of
Concern
Formaldehyde
Acetone
Formaldehyde
Acetone
Emission
Scenario
Conservative
Conservative
Typical
Typical
Meteorology
Typical
Conservative
Calm/Inversion
Typical
Conservative
Calm/Inversion
Typical
Conservative
Calm/Inversion
Typical
Conservative
Calm/Inversion
Spill Duration
Unmitigated3
10 minutes
Unmitigated
10 minutes
Unmitigated
10 minutes
Unmitigated
10 minutes
Unmitigated
10 minutes
Unmitigated
10 minutes
Unmitigated
10 minutes
Unmitigated
10 minutes
Unmitigated
10 minutes
Unmitigated
10 minutes
Unmitigated
10 minutes
Unmitigated
10 minutes
LOC
(ppm)
9.6
9.6
9.6
9.6
9.6
9.6
1960
1960
1960
1960
1960
1960
9.6
9.6
9.6
9.6
9.6
9.6
1960
1960
1960
1960
1960
1960
IDLH
(ppm)
19.6
19.6
19.6
19.6
19.6
19.6
2442
2442
2442
2442
2442
2442
19.6
19.6
19.6
19.6
19.6
19.6
2442
2442
2442
2442
2442
2442
Max. Dist. to
LOC (m)1
1000
10002
8190
. 6470
11400
9360
<25
<25
<25
<25
<25
<25
100
1002
910
900
1600
16002
<25
<25
<25
<25
<25
<25
Max. Dist. to
IDLH (m)1
640
6402
4800
3920
8450
6720
<25
<25
<25
<25
<25
<25
40
402
550
5502
1000
10002
<25
<25
<25
<25
<25
<25
Notes:
1 All distances are measured from the property line to the east or west, across the Ohio river to the south, or from the existing railroad to the north,
whichever is closer to the spill.
2 Mitigation does not decrease maximum distance.
' Based on the preliminary calculations, the maximum distances to LOG and IDLH due to emissions from a spill mitigated in 1 hour (i.e., with an
emission duration of 60 minutes) is approximately the same as an unmitigated spill.
Volume VII
Appendix VII-4
External Review Draft
Do not cite or quote
-36-
-------
TABLE 9
Summary of Air Dispersion Modeling Results (On-site Fire)
Run
No.
25
26
27
28
29
30
31
32
33
34
35
36
Chemical of
Concern
HC1
Phosgene
Emission
Scenario
Conservative
Conservative
Meteorology
Typical
Conservative
Calm/Inversion
Typical
Conservative
Calm/Inversion
Emission
Duration
Unmitigated4
10 minutes
Unmitigated
10 minutes
Unmitigated
10 minutes
Unmitigated
10 minutes
Unmitigated
10 minutes
Unmitigated
10 minutes
LOC
(ppm)
9.9
9.9
9.9
9.9
9.9
9.9
0.2
0.2
0.2
0.2
0.2
0.2
IDLH
(ppm)
49.1
49.1
49.1
49.1
49.1
49.1
2
2
2
2
2
2
Max. Dist. to
LOC (m)1
NO2
NO3
675-1125
NO
NA'
NA
NO
NO
NO
NO
NA
NA
Max. Dist. to
IDLH (m)1
NO
NO
NO
NO
NA
NA
NO
NO
NO
NO
NA
NA
Notes:
1 All distances are measured from the property line to the east or west, across the Ohio river to the south, or from the existing railroad to the north,
whichever is closer to the spill.
2 NO = Do not occur.
' NA = Not analyzed.
4 Based on the preliminary calculations, the maximum distances to LOC and IDLH due to emissions from a spill mitigated in 1 hour (i.e., with an
emission duration of 60 minutes) is approximately the same as an unmitigated spill.
Volume VII
Appendix VII-4
/ i
External Review Draft
Do not cite or quote
-------
V J
TABLE 9 (continued)
Summary of Air Dispersion Modeling Results (On-site Fire)
Run
No.
37
38
39
40
41
42
43
44
45
46
47
48
Chemical of
Concern
HC1
Emission
Scenario
Typical
Meteorology
Typical
Conservative
Calm/Inversion
Typical
Conservative
Calm/Inversion
Emission
Duration
Unmitigated4
10 minutes
Unmitigated
10 minutes
Unmitigated
10 minutes
Unmitigated
10 minutes
Unmitigated
10 minutes
Unmitigated
10 minutes
LOC
(ppm)
9.9
9.9
9.9
9.9
9.9
9.9
0.2
0.2
0.2
0.2
0.2
0.2
IDLH
(ppm)
49.1
49.1
49.1
49.1
49.1
49.1
2
2
2
2
2
2
Max. Dist. to
LOC (m)1
NO2
NO
NO
NO
NA
NA
NO
NO
NO
NO
NA
NA
Max. Disl. to
IDLH (m)1
NO
NO
NO
NO
NA
NA
NO
NO
NO
NO
NA
NA
Notes:
1 All distances are measured from the property line to the east or west, across the Ohio river to the south, or from the existing railroad to the north,
whichever is closer to the spill.
? NO = Do not occur.
' NA = Not analyzed.
* Based on the preliminary calculations, the maximum distances to LOC and IDLH due to emissions from a spill mitigated in 1 hour (i.e., with an
emission duration of 60 minutes) is approximately the same as an unmitigated spill.
Volume VII
Appendix VI1-4
External Review Draft
Do not cite or quote
-38-
-------
TABLE 10
Summary of Air Dispersion Modeling Results (On-site Mixing of Incompatible Wastes)
Run
No.
49
50
51
52
53
54
55
56
57
58
59
60
Chemical of
Concern
HC1
HC1
Emission
Scenario
Conservative
Typical
Meteorology
Typical
Conservative
Calm/Inversion
Typical
Conservative
Calm/Inversion
Emission
Duration
Unmitigated2
10 minutes
Unmitigated
10 minutes
Unmitigated
10 minutes
Unmitigated
10 minutes
Unmitigated
10 minutes
Unmitigated
10 minutes
LOC
(ppm)
9.9
9.9
9.9
9.9
9.9
9.9
9.9
9.9
9.9
9.9
9.9
9.9
IDLH
(ppm)
49.1
49.1
49.1
49.1
49.1
49.1
49.1
49.1
i 49.1
49.1
49.1
49.1
Max. Dist. to
LOC (m)
1780
1260
8790
6260
12200
9190
125
125
980
980
1700
1700
Max. Dist. to
IDLH (m)
680
<25
3190
2170
4620
3380
<25
<25
270
270
520
520
Notes:
1 All distances are measured from the property line to the east or west, across the Ohio river to the south, or from the existing railroad to the north,
whichever is closer to the spill.
2 The unmitigated releases are assumed to last for 20 minutes.
Volume VII
Appendix VII-4
External Review Draft
Do not cite or quote
-------
TABLE 11
Summary of Air Dispersion Modeling Results (Off-site Spill)
Run
No.
61
62
63
64
65
66
67
68
69
70
71
72
Chemical of
Concern
Formaldehyde
Acetone
Formaldehyde
Acetone
Emission
Scenario
Conservative
Conservative
Typical
Typical
Meteorology
Typical
Conservative
Calm/Inversion
Typical
Conservative
Calm/Inversion
Typical
Conservative
Calm/Inversion
Typical
Conservative
Calm/Inversion
Emission
Duration
Unmitigated
Unmitigated
Unmitigated
Unmitigated
Unmitigated
Unmitigated
Unmitigated
Unmitigated
Unmitigated
Unmitigated
Unmitigated
Unmitigated
LOC
(ppm)
9.6
9.6
9.6
1960
1960
1960
9.6
9.6
9.6
1960
1960
1960
IDLH
(ppm)
19.6
19.6
19.6
2442
2442
2442
19.6
19.6
19.6
2442
2442
2442
Max. Dist. to
LOC(m)
1490
8490
11540
<25
<25
57
190
980
1670
<25
<25
<25
Max. Dist. to
IDLH (m)
980
5120
8550
<25
<25
47
130
630
1080
<25
<25
<25
Volume VII
Appendix VII-4
-40-
Extemal Review Draft
Do not cite or quote
-------
TABLE 12
Summary of Air Dispersion Modeling Results (Off-site Fire)
Run
No.
73
74
75
76
77
78
79
80
81
82
83
84
Chemical of
Concern
HC1
Phosgene
HC1
Phosgene
Emission
Scenario
Conservative
Conservative
Typical
Typical
Meteorology
Typical
Conservative
Calm/Inversion
Typical
Conservative
Calm/Inversion
Typical
Conservative
Calm/Inversion
Typical
Conservative
Calm/Inversion
Emission
Duration
Unmitigated
Unmitigated
Unmitigated
Unmitigated
Unmitigated
Unmitigated
Unmitigated
Unmitigated
Unmitigated
Unmitigated
Unmitigated
Unmitigated
LOC
(ppm)
9.9
9.9
9.9
0.2
0.2
0.2
9.9
9.9
9.9
0.2
0.2
0.2
IDLH
(ppm)
49.1
49.1
49.1
2
2
2
49.1
49.1
49.1
2
2
2
Max. Dist. to
LOC (m)
NO1
2,100
NA2
NO
1,100
NA
NO
NO
NA
NO
NO
NA
Max. Dist. to
IDLH (m)
NO1
275
NA
NO
125
NA
NO
NO
NA
NO
NO
NA
Notes:
1 NO = Do not occur.
2 NA = Not analyzed.
Volume VII
Apr—'dix VII-4
External Review Draft
Do not cite or nuotc
-------
TABLE 13
Average Vapor Mole Fraction Used in SLAB Modeling
Scenario
Conservative On-Site Spill
Conservative On-site Spill
Typical On-Site Spill
Typical On-site Spill
Conservative Off-Site Spill
Conservative Off-Site Spill
Typical Off-Site Spill
Typical Off-Site Spill
Runs
1-6
7-12
13-18
19-24
61-63
64-66
67-69
70-72
Chemical of
Concern
Formaldehyde
Acetone
Formaldehyde
Acetone
Formaldehyde
Acetone
Formaldehyde
Acetone
Time Required
until Chemical of
Concern
Depleted1
(sec)
3120
18240
680
3960
1740
10320
680
3960
Total Evaporation
Time for the Spill
(sec)
24170
39600
5340
8760
13750
22560
5340
8760
Average Vapor
Mole Fraction
Until Depleted1
0.478
0.273
0.482
0.276
0.484
0.274
0.482
0.276
Average Vapor
Mole Fraction for
10 Minutes (with
mitigation)
0.742
.0.585
0.512
0.538
NC:
NC
NC
NC
Notes:
1 = Depletion defined when the liquid mass fraction in the evaporating pool reaches 0.001.
2 = Not calculated because mitigation is not considered.
Volume VII
Appendix VII-4
External Review Draft
Do not cite or quote
-42-
-------
TABLE 14
Summary of ISC-COMPDEP Screening Results for
the On-Site Fire Scenario
One-hour Average Concentrations (pg/m3)
Emission Rate (1 g/s)
X
Downwind
Distance
(m)
Mixing
Height
100
200
300
400
500
600
700
800
900
1000
1250
1500
1750
2000
2250
2500
3000
4000
5000
7500
10000
15000
20000
30000
40000
50000
Stability Class A
Wind Speed (m/s)
1.000
320
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
1.500
480
0.000
0.000
0.000
0.001
0.023
0.157
1.037
3.763
3.500
3.626
3.115
2.532
2.129
1.837
1.615
1.441
1.185
0.875
0.693
0.456
0.344
0.243
0.190
0.135
0.107
0.089
2.000
640
0.000
0.000
0.001
0.071
0.453
1.037
2.145
4.735
3.615
2.930
1.814
1.425
1.198
1.033
0.908
0.810
0.667
0.492
0.390
0.257
0.193
0.137
0.107
0.076
0.060
0.050
2.500
800
0.000
0.000
0.011
0.495
1.535
2.186
2.693
4.938
3.502
2.631
1.336
0.920
0.766
0.661
0.581
0.519
0.427
0.315
0.249
0.164
0.124
0.087
0.068
0.049
0.038
0.032
3.000
960
0.000
0.000
0.045
1.257
2.700
3.021
2.839
4.766
3.239
2.336
1.108
0.666
0.533
0.459
0.404
0.360
0.296
0.219
0.173
0.114
0.085
0.056
0.042
0.028
0.021
0.017
Stability Class B
Wind Speed (m/s)
1.000
320
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
1.500
480
0.000
0.000
0.000
o.ooo •
0.000
0.000
0.000
0.912
0.716
0.800
1.076
1.274
1.338
1.356
1.340
1.272
1.172
1.002
0.830
0.580
0.451
0.316
0.247
0.174
0.137
0.113
2.000
640
0.000
0.000
0.000
0.000
0.002
0.009
0.023
1.951
1.518
1.637
1.886
1.879
1.693
1.496
1.308
1.115
. 0.852
0.594
0.470
0.326
0.254
0.178
0.139
0.098
0.077
0.064
2.500
800
0.000
0.000
0.000
0.005
0.057
0.155
0.246
3.285
2.512
2.544
2.486
2.172
1.789
1.478
1.230
1.014
0.746
0.456
0.322
0.209
0.162
0.114
0.089
0.063
0.049
0.041
3.000
960
0.000
0.000
0.000
0.050
0.324
0.625
0.802
4.587
3.450
3.284
2.801
2.235
1.739
1.381
1.116
0.904
0.656
0.343
0.216
0.147
0.085
0.056
0.042
0.028
0.021
0.017
3.500
1120
0.000
0.000
0.000
0.164
0.834
1.330
1.516
5.620
4.170
3.767
2.902
2.177
1.634
1.265
1.004
0.809
0.548
0.296
0.184
0.088
0.063
0.041
0.031
0.021
0.015
0.012
4.000
1280
0.000
0.000
0.000
0.329
1.436
2.048
2.175
6.306
4.634
4.019
2.872
2.064
1.513
1.152
0.897
0.716
0.484
0.260
0.161
0.072
0.048
0.032
0.024
0.016
0.012
0.009
4.500
1440
0.000
0.000
0.001
0.496
1.979
2.635
2.679
6.273
4.875
4.098
2.743
1.904
1.381
1.039
0.807
0.643
0.433
0.232
0.143
0.061
0.039
0.025
0.019
0.012
0.009
0.007
5.000
1600
0.000
0.000
0.001
0.636
2.393
3.052
0.000
6.060
4.709
3/" ^
2.i.
1.752
1.262
0.946
0.733
0.582
0.391
0.209
0.129
0.054
0.033
0.020
0.015
0.010
0.008
0.006
Volume VII
Appendix VII-4
-43-
External Review Draft
Do not cite or quote
-------
TABLE 14
Summary of ISC-COMPDEP Screening Results for
the On-Site Fire Scenario
One-hour Average Concentrations (/ig/m3)
Emission Rate (1 g/s)
X
Downwind
Distance
(m)
Mixing
Height
100
200
300
400
500
600
700
800
900
1000
1250
1500
1750
2000
2250
2500
3000
4000
5000
7500
10000
15000
20000
30000
40000
50000
Stability Class C
Wind Speed (m/s)
1.000
320
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
1.500
480
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.498
0.355
0.355
0.414
0.488
0.538
0.610
0.694
0.714
0.796
0.783
0.856
0.769
0.623
0.437
0.339
0.237
0.184
0.152
2.000
640
0.000
0.000
0.000
0.000
0.000
0.000
0.000
1.035
0.733
0.750
0.891
1.019
1.061
1.113
1.162
1.109
1.062
0.994
0.831
0.514
0.366
0.246
0.190
0.133
0.104
0.085
2.500
800
0.000
0.000
0.000
0.000
0.001
0.003
0.005
1.902
1.341
1.364
1.543
1.631
1.567
1.517
1.466
1.329
1.286
1.026
0.786
0.433
0.275
0.161
0.122
0.085
0.066
0.055
3.000
960
0.000
0.000
0.000
0.000
0.014
0.039
0.060
3.068
2.159
2.144
2.230
2.159
1.930
1.750
1.595
1.538
1.351
0.685
0.459
0.375
0.126
0.061
0.042
0.027
0.020
0.016
3.500
1120
0.000
0.000
0.000
0.001
0.055
0.158
0.239
4.394
3.092
2.972
2.822
2.524
2.130
1.839
1.729
1.598
1.008
0.606
0.402
0.187
0.108
0.051
0.032
0.020
0.015
0.012
4.000
1280
0.000
0.000
0.000
0.003
0.123
0.362
0.543
5.697
4.015
3.730
3.253
2.726
2.204
1.808
1.497
1.255
0.914
0.542
0.357
0.165
0.095
0.044
0.026
0.015
0.012
0.009
4.500
1440
0.000
0.000
0.000
0.004
0.200
0.604
0.906
5.824
4.735
4.290
3.358
2.635
2.093
1.690
1.387
1.155
0.833
0.489
0.320
0.147
0.085
0.039
0.023
0.012
0.009
0.007
5.000
1600
0.000
0.000
0.000
0.006
0.271
0.833
0.000
5.879
4.765
4.274
3.267
2.518
1.975
1.580
1.287
1.067
0.764
0.445
0.291
0.133
0.076
0.035
0.020
0.010
0.007
0.006
8.000
2560
0.000
0.000
0.000
0.009
0.406
0.000
0.000
5.515
4.389
3.750
2.604
1.884
1.417
1.101
0.878
0.717
0.503
0.287
0.185
0.084
0.048
0.022
0.013
0.006
0.003
0.002
10.000
3200
0.000
0.000
0.000
0.008
0.000
0.000
0.000
5.030
3.969
3.325
2.232
1.583
1.176
0.906
0.719
0.584
0.408
0.231
0.149
0.067
0.038
0.018
0.010
0.005
0.003
0.002
Volume VII
Appendix VII-4
-44-
Extemal Review Draft
Do not cite or quote
-------
TABLE 14
Summary of ISC-COMPDEP Screening Results for
the On-Site Fire Scenario
One-hour Average Concentrations (fig/m3)
Emission Rate (1 g/s)
X
Downwind
Distance
(m)
Mixing
Height
100
200
300
400
500
600
700
800
900
1000
1250
1500
1750
2000
2250
2500
3000
4000
5000
7500
10000
15000
20000
30000
40000
50000
Stability Class D
Wind Speed (m/s)
1.000
320
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
1.500
.480
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.359
0.244
0.223
0.213
0.209
0.196
0.202
0.225
0.220
0.274
0.287
0.262
0.229
0.227
0.250
0.272
0.255
0.224
0.197
2.000
640
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.673
0.445
0.416
0.421
0.431
0.411
0.433
0.491
0.479
0.591
0.582
0.501
0.377
0.440
0.420
0.359
0.256
0.192
0.151
2.500
800
0.000
0.000
0.000
0.000
0.000
0.000
0.000
1.196
0.778
0.736
0.767
0.794
0.757
0.791
0.882
0.846
0.981
0.878
0.707
0.660
0.627
0.485
0.374
0.242
0.174
0.133
3.000
960
0.000
0.000
0.000
0.000
0.000
0.000
0.000
1.987
1.281
1.217
1.270
1.297
1.214
1.236
1.330
1.244
1.288
0.987
0.785
0.493
0.342
0.198
0.132
0.073
0.048
0.035
3.500
1120
0.000
-o.ooo
0.000
0.000
0.000
0.002
0.004
3.072
1.976
1.869
1.907
1.891
1.721
1.694
1.676
1.533
1.300
0.972
0.758
0.459
0.312
0.177
0.117
0.064
0.042
0.030
4.000
1280
0.000
0.000
0.000
0.000
0.000
0.006
0.018
3.998
2.851
2.668
2.619
2.361
2.099
1.883
1.701
1.544
1.291
0.943
0.722
0.426
0.286
0.160
0.105
0.057
0.037
0.027
4.500
1440
0.000
0.000
0.000
0.000
0.001
0.015
0.049
4.066
3.383
3.175
2.772
2.419
2.136
1.901
1.704
1.536
1.266
0.906
0.685
0.396
0.262
0.145
0.094
0.051
0.033
0.024
5.000
1600
0.000
0.000
0.000
0.000
0.001
0.027
0.000
4.141
3.456
3.252
2.834
2.457
2.152
1.901
1.691
1.513
1.232
0.867
0.647
0.368
0.241
0.133
0.086
0.046
0.030
0.022
S.OOO
2560
0.000
0.000
0.000 •
0.000
0.002
0.000
0.000
4.503
3.772
3.509
2.901
2.392
2.001
1.697
1.458
1.266
0.982
0.650
0.467
0.252
0.161
0.086
0.055
0.030
0.019
0.014
10.000
3200
0.000
0.000
0.000
0.000
0.000
0.000
0.000
4.566
3.809
3.483
2.766
2.219
1.817
1.515
1.284
1.103
0.842
0.546
0.388
0.206
0.131
0.070
0.045
0.024
0.015
0.011
15.000
4800
0.000
0.000
0.000
0.000
0.000
0.000
0.000
4.288
3.535
3.115
2.305
1.774
1.410
1.150
0.957
0.811
0.607
0.385
0.270
0.141
0.089
0.047
0.030
0.016
0.010
0.007
20,000
6400
0.000
0.000
0.000
0.000
0.000
0.000
0.000
3.815
3.116
/ ^
lv
1.440
1.128
0.910
0.752
0.634
0.470
0.295
0.206
0.107
0.067
0.036
0.023
0.012
0.008
0.006
Volume VII
Appendix VII-4
-45-
External Review Dra
Do not cite or quo
-------
TABLE 14
Summary of ISC-COMPDEP Screening Results for
the On-Site Fire Scenario
One-hour Average Concentrations (pg/m3)
Emission Rate (1 g/s)
X
Downwind
•Distance
(m)
Mixing
Height
100
200
300
400
500
600
700
800
900
1000
1250
1500
1750
2000
2250
2500
3000
4000
5000
7500
10000
15000
20000
30000
40000
50000
Stability Class £
Wind Speed (m/s)
1.000
10000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
62.572
53.023
45.741
33.155
25.412
20.536
16.781
13.783
11.910
8.623
5.529
4.102
2.357
1.476
0.847
0.561
0.324
0.219
0.164
1.500
10000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
44.669
37.699
32.392
23.132
17.593
14.127
11.472
9.364
8.059
5.779
3.663
2.702
1.540
0.957
0.546
0.361
0.208
0.140
0.105
2.000
10000
0.000
0.000
0.000
0.000
0.000
0.000
0.001
34.963
29.415
25.196
17.863
13.508
10.797
8.730
7.096
6.091
4.339
2.729
2.007
1.137
0.704
0.401
0.264
0.152
0.102
0.077
2.500
10000
0.000
0.000
0.000
0.000
0.000
0.000
0.002
28.866
24.223
20.698
14.589
10.984
8.749
7.051
5.713
4.894
3.469
2.170
1.592
0.899
0.554
0.315
0.208
0.119
0.080
0.060
3.000
10000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
24.654
20.644
17.603
12.348
9.264
7.358
5.914
4.780
4.088
2.888
1.799
1.317
0.742
0.456
0.259
0.170
0.098
0.066
0.049
3.500
10000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
21.557
18.017
15.336
10.715
8.014
6.351
5.094
4.109
3.510
2.471
1.535
1.122
0.631
0.387
0.220
0.144
0.083
0.056
0.042
4.000
10000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
19.178
16.002
13.599
9.469
7.064
5.587
4.473
3.602
3.074
2.159
1.337
0.976
0.548
0.336
0.190
0.125
0.072
0.048
0.036
4.500
10000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
17.288
14.405
12.225
8.486
6.317
4.988
3.987
3.206
2.733
1.916
1.184
0.864
0.484
0.296
0.168
0.110
0.063
0.043
0.032
5.000
10000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
15.749
13.105
11.109
7.690
5.714
4.505
3.596
2.888
2.460
1.721
1.061
0.774
0.433
0.265
0.150
0.098
0.056
0.038
0.028
Volume VII
Appendix VII-4
-46-
Extemal Review Draft
Do not cite or quote
-------
TABLE 14
Summary of ISC-COMPDEP Screening Results for
the On-Site Fire Scenario
One-hour Average Concentrations (jig/m3)
Emission Rate (1 g/s)
X
Downwind
Distance
(m)
Mixing Height
100
200
300
400
500
600
700
800
900
1000
1250
1500
1750
2000
2250
2500
3000
4000
5000
7500
10000
15000
20000
30000
40000
50000
Stability Class F
Wind Speed (m/s)
1.000
10000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
63.414
54.020
46.921
34.352
26.604
21.724
17.900
14.796
12.892
9.424
6.233
4.733
2.827
1.826
1.088
0.753
0.448
0.313
0.237
1.500
10000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
45.284
38.467
33.327
24.236
18.656
15.156
12.423
10.213
8.868
6.426
4.209
3.179
1.881
1.205
0.713
0.492
0.292
0.204
0.154
2.000
10000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
35.560
30.142
26.064
18.860
14.454
11.698
9.552
7.824
6.777
4.882
3.176
2.390
1.406
0.896
0.529
0.364
0.215
0.150
0.113
2.500
10000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
29.422
24.897
21.495
15.493
11.832
9.549
7.775
6.350
5.490
3.937
2.549
1.913
1.121
0.712
0.419
0.288
0.170
0.118
0.089
3.000
10000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
25.166
21.265
18.336
13.174
10.033
8.078
6.562
5.347
4.617
3.299
2.128
1.594
0.931
0.590
0.346
0.238
0.140
0.098
0.074
3.500
10000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
22.028
18.591
16.013
11.474
8.718
7.006
5.680
4.620
3.984
2.839
1.825
1.365
0.795
0.503
0.295
0.202
0.119
0.083
0.063
4.000
10000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
J 9.610
16.534
14.228
10.172
7.713
6.188
5.009
4.068
3.505
2.492
1.598
1.194
0.694
0.438
0.256
0.176
0.104
0.072
0.054
Volume VII
Appendix VII-4
-47-
External Review Draft
Do not cite or quote
-------
TABLE 15
Summary of ISC-COMPDEP Screening Results for
the Off-Site Fire Scenario
One-hour Average Concentrations (ftg/m3)
Emission Rate (1 g/s)
X
Downwind
Distance
(m)
Mixing
Height
100
200
300
400
500
600
700
800
900
\ 1000
1250
1500
1750
2000
2250
2500
3000 -
4000
5000
7500
10000
15000
20000
30000
40000
50000
Stability Class A
Wind Speed (mis)
1.000
320
0.819
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
o.ooo
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
1.500
480
1.092
0.625
0.591
0.615
0.750
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
2.000
640
1.552
1.087
1.176
1.298
1.469
1.628
1.630
1.603
1.620
1.647
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
2.500
800
2.275
1.845
2.109
2.282
2.375
2.299
2.024
1.716
1.411
1.196
0.923
0.773
0.663
0.580
0.515
0.464
0.387
0.290
0.232
0.155
0.117
0.083
0.066
0.047
0.037
0.031
3.000
960
3.343
2.953
3.355
3.406
3.201
2.749
2.205
1.743
1.357
1.070
0.669
0.538
0.460
0.403
0.358
0.322
0.268
0.201
0.161
0.107
0.082
0.058
0.046
0.032
0.026
0.021
Stability Class B
Wind Speed (m/s)
1.000
320
0.738
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
1.500
480
0.882
0.421
0.332
0.264
0.213
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
2.000
640
1.109
0.613
0.551
0.468
0.387
0.294
0.230
0.200
0.174
0.169
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
2.500
800
1.446
0.912
0.903
0.802
0.681
0.520
0.409
0.357
0.311
0.303
0.222
0.271
0.315
0.349
0.364
0.389
0.354
0.306
0.270
0.196
0.154
0.109
0.085
0.060
0.047
0.039
3.000
960
1.926
1.352
1.429
1.297
1.106
0.842
0.660
0.574
0.497
0.479
0.344
0.395
0.425
0.437
0.428
0.429
0.357
0.260
0.203
0.137
0.107
0.076
0.059
0.042
0.033
0.027
3.500
1120
2.584
1.965
2.149
1.954
1.653
1.246
0.967
0.832
0.712
0.676
0.475
0.507
0.510
0.494
0.461
0.441
0.348
0.241
0.174
0.103
0.079
0.056
0.043
0.031
0.024
0.020
4.000
1280
3.458
2.771
3.057
2.748
2.282
1.698
1.302
1.104
0.933
0.871
0.598
0.596
0.566
0.523
0.471
0.436
0.333
0.223
0.156
0.083
0.061
0.043
0.033
0.024
0.018
0.015
4.500
1440
4.579
3.774
4.118
3.623
2.940
2.156
1.634
1.364
1.140
1.046
0.703
0.661
0.599
0.534
0.467
0.421
0.319
0.207
0.142
0.071
0.049
0.034
0.026
0.019
0.015
0.012
5.00
160
5.96
4.95
5.27
4.51
3.57
2.58
1.93
1.5S
1.31
US
0.7*
0.7C
0.61
0.52
0.4f
0.4C
0.3(
0.1S
0.1:
0.0<
0.0^
o.o:
o.o:
0.0
0.0
0.0
Volume VII
Appendix VII-4
-48-
External Review I
Do not cite or <
-------
TABLE 15
Summary of ISC-COMPDEP Screening Results for
the Off-Site Fire Scenario
One-hour Average Concentrations (jtg/m3)
Emission Rate (1 g/s)
X
Downwind
Distance
(»)
Mixing
Height
100
200
300
400
500
600
700
800
900
1000
1250
1500
1750
2000
2250
2500
3000
4000
5000
7500
10000
15000
20000
30000
40000
50000
1.000
320
0.689
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
Stability Class C
Wind Speed (m/s)
1.500
480
0.762
0.349
0.267
0.205
0.153
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
2.000
640
0.871
0.456
0.395
0.323
0.246
0.168
0.119
0.096
0.077
0.071
0.045
0.047
0.052
0.061
0.071
0.095
0.113
0:182
0.248
0.321
0.304
0.229
0.179
0.126
0.098
0.081
2.SOO
800
1.023
0.609
0.588
0.507
0.394
0.268
0.188
0.152
0.122
0.115
0.070
0.076
0.087
0.103
0.120
0.161
0.178
0.213
0.239
0.228
0.196
0.146
0.115
0.081
0.063
0.052
3.000
960
1.229
0.823
0.868
0.779
0.614
0.416
0.291
0.236
0.190
0.181
0.110
0.122
0.140
0.165
0.187
0.243
0.253
0.283
0.285
0.225
0.167
0.106
0.080
0.056
0.044
0.036
3.500
1120
1.500
1.115
1.260
1.160
0.922
0.624
0.434
0.353
0.284
0.272
0.164
0.183
0.208
0.238
0.262
0.324
0.316
0.335
0.311
0.219
0.153
0.086
0.061
0.041
0.032
0.026
4.000
1280
1.850
1.501
1.781
1.663
1.326
0.894
0.621
0.504
0.405
0.388
0.233
0.257
0.283
0.314
0.333
0.393
0.378
0.368
0.322
0.210
0.141
0.075
0.049
0.032
0.025
0.020
4.500
1440
2.293
1.996
2.444
2.289
1.819
1.224
0.848
0.687
0.550
0.526
0.315
0.339
0.361
0.386
0.398
0.447
0.429
0.386
0.322
0.198
0.130
0.068
0.043
0.025
0.019
0.016
5.000
1600
2.843
2.612
3.245
3.024
2.388
1.602
1.109
0.894
0.715
0.679
0.405
•0.423
0.436
0.449
0.466
0.485
0.466
0.394
0.317
0.187
0.120
0.062
0.038
0.021
0.016
0.013
8.000
2560
2.089
5.665
5.495
4.605
3.773
3.108
2.591
2.132
1.681
1.520
0.903
0.785
0.747
0.708
0.657
0.497
0.373
0.230
0.156
0.074
0.043
0.020
0.012
0.005
0.003
0.002
10.000
3200
1.590
5.595
5.585
4.671
3.795
3.096
2.558
2.143
1.819
1.567^
1.05^
0.902
0.823
0.737
0.503
0.425
0.314
0.190
0.127
0.060
0.035
0.016
0.009
0.004
0.002
0.002
Volume VII
Appendix VII-4
-49-
Extemal Review Draft
Do not cite or quote
-------
TABLE 15
Summaiy of ISC-COMPDEP Screening Results for
the Off-Site Fire Scenario
One-hour Average Concentrations (pg/m3)
x'
Downwind
Distance
(m)
Mixing
Height
100
200
300
400
500
600
700
800
900
1000
1250
1500
1750
2000
2250
2500
3000
4000
5000
7500
10000
15000
20000
30000
40000
50000
Stability Class D
Wind Speed (mis)
1.000
320
0.659
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
1.500
480
0.692
0.313
0.240
0.183
0.133
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
2.000
640
0.738
0.377
0.329
0.265
0.196
0.128
0.086
0.067
0.052
0.047
0.026
0.022
0.021
0.020
0.020
0.027
0.026
0.026
0.024
0.028
0.036
0.048
0.057
0.070
0.072
0.072
2.500
800
0.799
0.460
0.451
0.384
0.288
0.184
0.121
0.093
0.072
0.067
0.035
0.031
0.029
0.030
0.031
0.044
0.042
0.045
0.043
0.049
0.061
0.073
0.078
0.077
0.069
0.061
3.000
960
0.877
0.567
0.618
0.551
0.419
0.263
0.169
0.131
0.099
0.094
0.048
0.043
0.041
0.043
0.046
0.069
0.067
0.074
0.070
0.080
0.094
0.104
0.104
0.091
0.076
0.064
3.500
1120
0.976
0.703
0.843
0.780
0.601
0.371
0.235
0.181
0.137
0.132
0.065
0.059
0.058
0.062
0.067
0.103
0.102
0.112
0.104
0.116
0.130
0.132
0.122
0.098
0.078
0.064
4.000
1280
1.097
0.875
1.139
1.087
0.844
0.516
0.323
0.249
0.187
0.182
0.087
0.081
0.080
0.088
0.095
0.148
0.146
0.156
0.142
0.155
0.164
0.153
0.134
0.101
0.078
0.062
4.500
1440
1.251
1.091
1.520
1.485
1.159
0.703
0.437
0.335
0.252
0.246
0.115
0.108
0.109
0.120
0.131
0.203
0.197
0.204
0.180
0.193
0.194
0.168
0.141
0.100
0.075
0.059
5.000
1600
1.533
1.357
1.999
1.985
1.553
0.938
0.579
0.444
0.332
0.327
0.151
0.143
0.144
0.159
0.173
0.266
0.254
0.252
0.216
0.228
0.218
0.178
0.144
0.098
0.072
0.056
8.000
2560
0.271
1.718
2.283
2.220
2.010
1.782
1.574
1.393
1.150
1.109
0.524
0.480
0.462
0.478
0.485
0.546
0.472
0.362
0.286
0.178
0.122
0.070
0.047
0.026
0.017
0.012
10.000
3200
0.100
1.308
2.070
2.142
2.002
1.807
1.613
1.438
1.284
1.152
0.852
0.745
0.681
0.648
0.592
0.541
0.457
0.338
0.261
0.155
0.104
0.059
0.039
0.021
0.014
0.010
15.000
4800
0.021
0.949
1.916
2.127
2.043
1.865
1.671
1.489
1.327
1.186
0.897
0.783
0.688
0.607
0.539
0.481
0,389
0.272
0.202
0.114
0.075
0.041
0.027
0.014
0.009
0.007
20.000
6400'
0.010
0.860
1.889
2.121
2.031
1.841
1.636
1.447
1.281
1.137
0.856
0.725
0.621
0.537
.0.468
0.412
0.326
0.222
0.162
0.089
0.058
0.031
0.020
0.011
0.007
0.005
Volume VII
Appendix VII-4
-50-
Extemal Review Drai
Do not cite or quot
-------
TABLE 15
Summary of ISC-COMPDEP Screening Results for
the Off-Site Fire Scenario
One-hour Average Concentrations (/ig/m3)
Emission Rate (1 g/s)
X
Downwind
Distance
(m)
Mixing
Height
100
200
300
400
500
600
700
800
900
1000
1250
1500
1750
2000
2250
2500
3000
4000
5000
7500
10000
15000
20000
30000
40000
50000
Stability Class E
Wind Speed (m/s)
1.000
10000
9.179
5.203
9.788
14.866
17.161
14.433
11.513
11.034
9.903
11.801
7.643
6.218
5.411
5.394
5.345
7.214
5.822
4.325
3.223
1.877
1.339
0.776
0.708
0.563
0.463
0.390
1.500
10000
26.374
5.639
11.202
16.901
18.945
15.837
12.654
11.945
10.644
12.066
7.978
6.424
5.503
5.293
5.062
5.655
4.508
3.059
2.327
1.369
0.894
0.524
0.351
0.205
0.140
0.105
2.000
10000
62.234
11.462
12.354
18.189
19.650
16.330
13.092
12.163
10.766
11.603
7.860
6.282
5.313
4.953
4.598
4.360
3.459
2.300
1.742
1.029
0.660
0.384
0.257
0.150
0.102
0.077
2.500
10000
120.401
22.427
15.664
18.927
19.649
16.244
13.080
11.966
10.533
10.813
7.516
5.976
5.004
4.543
4.114
3.525
2.787
1.841
1.390
0.817
0.521
0.302
0.202
0.117
0.080
0.060
3.000
10000
191.379
38.042
25.634
19.254
19.191
15.794
12.785
11.527
10.098
9.825
7.069
5.603
4.655
4.131
3.644
2.960
2.333
1.533
1.155
0.675
0.429
0:248
0.166
0.096
0.065
0.049 n
3.500
10000
207.639
56.090
35.425
23.486
18.443
15.122
12.312
10.952
9.558
8.722
6.584
5.210
4.303
3.719
3.199
2.552
2.006
1.313
0.987
0.575
0.364
0.211
0.140
0.081
0.055
0.041
4.000
10000
189.364
72.278
39.821
25.241
17.612
14.234
11.737
10.251
8.922
7.800
6.015
4.803
3.951
3.324
2.834
2.242
1.759
1.147
0.861
0.500
0.316
0.182
0.121
0.070
0.048
0.036
4.500
10000
169.678
70.661
38.229
24.092
16.927
13.035
10.939
9.365
8.142
7.031
5.471
4.360
3.581
2.998
2.533
2.000
1.566
1.018
0.763
0.442
0.279
0.161
0.107
0.062
0.042
0.031
5.000
10000
151.220
66.922
36.170
22.830
16.031
12.312
10.096
8.634
7.498
6.405 ,'
5.013 --
3.996
3.277
2.714
2.290
1.805
1.411
0.915
0.684
0.396
0.249
0.144
0.095
0.055
0.037
0.028
Volume VII
Appendix VII-4
-51-
External Review Draft
Do not cite or quote
-------
TABLE 15
Summary of ISC-COMPDEP Screening Results for
the Off-Site Fire Scenario
One-hour Average Concentrations (pg/m3)
Emission Rate (1 g/s)
X
Downwind
Distance
(m)
Mixing
Height
100
200
300
400
500
600
700
800
900
1000
1250
1500
1750
2000
2250
2500
3000
4000
5000
7500
10000
15000
20000
30000
40000
50000
Stability Class F
Wind Speed (m/s)
1.000
10000
17.673
10.718
22.115
32.516
34.857
28.975
23.247
21.615
19.160
20.693
14.095
11.294
9.602
9.110
8.585
7.888
6.390
4.437
3.457
2.156
1.445
0.886
0.624
0.378
0.267
0.204
1.500
10000
57.570
12.139
25.155
34.118
33.458
27.673
22.609
. 20.432
18.022
16.874
12.861
10.328
8.684
7.755
6.771
5.487
4.422
3.042
2.357
1.454
0.965
0.586
0.411
0.248
0.174
0.133
2.000
10000
135.075
24.989
27.031
33.357
28.702
23.681
20.081
17.400
15.311
13.365
10.651
8.663
7.248
6.162
5.285
4.230
3.395
2.320
1.790
1.097
0.723
0.437
0.305
0.183
0.129
0.098
2.500
10000
218.080
47.283
31.287
30.851
24.205
19.946
17.023
14.618
12.847
11.078
8.861
7.221
6.027
5.057
4.329
3.451
2.761
1.877
1.444
0.880
0.577
0.347
0.242
0.145
0.102
0.077
3.000
10000
193.674
71.261
41.282
27.038
20.871
17.179
14.646
12.561
11.029
9.495
7.580
6.164
5.133
4.298
3.672
2.919
2.329
1.577
1.210
0.734
0.480
0.288
0.200
0.120
0.084
0.064
3.500
10000
167.072
72.022
39.381
24.942
18.405
15.133
12.890
11.044
9.687
8.329
6.638
5.387
4.479
3.743
3.193
2.531
2.016
1.360
1.041
0.629
0.410
0.245
0.171
0.102
0.071
0.054
4.000
10000
141.859
66.840
36.889
23.471
16.553
13.554
11.534
9.873
8.653
7.431
5.913
4.791
3.976
3.318
2.827
2.236
1. 777
1.195
0.914
0.551
0.358
0.214
0.148
0.088
0.062
0.047
Volume VII
Appendix VII-4
-52-
External Review Oral
Do not cite or quot
-------
TABLE 16 '
Maximum and Typical Phosgene and HCI Concentrations for the Conservative
Unmitigated On-Site Fire Scenario
Meteorology
Downwind
(m)
100
200
300
400
500
600
700
800
900
1000
1250
1500
17SO
2000
2250
2500
3000
4000
5000
7500
10000
15000
20000
30000
40000
50000
Concentration Factors
Conservative
Concentration
(ug/m3)/(g/«)
0
o •
0.045
1.257
2.7
3.052
2.839
63.414
54.02
46.921
34.352
26.604
21.724
17.9
14.796
12.892
9.424
6.233
4.733
2.827
1.826
1.088
0.753
0.448
,0.313
0.237
Typical
Concentration
(ug/mj)/(g/s)
0
0
0
0
0
0.001
0.002
2.5295
1.6285
1.543
1.5885
1.594
1.4675
1.465
1.503
1.3885
1.294
0.9795
0.7715
0.476
0.327
0.1875
0.1245
0.0685
0.045
0.0325
Phosgene1-1
Conservative
Concentration
(ppm)
0.00
o.oo.
1.33e-04
3.72e-03
7.99e-03
9.03e-03
8.40e-03
1.88e-01
1.60e-01
1.39e-01
1.02e-01
7.87e-02
6.43e-02
5.30e-02
4.38e-02
3.82e-02
2.79e-02
1.84e-02
1.40e-02
8.37e-03
5.40e-03
3.22e-03
2.23e-03
1.33e-03
9.26e-04
• 7.01e-04
Typical
Concentration
(ppm)
0.00 .
0.00
0.00
0.00
0.00
2.96e-06
5.92e-06
7.49e-03
4.82e-03
4.57e-03
4.70e-03
4.72e-03
4.34e-03
4.34e-03
4.45e-03
4.11e-03
3.83e-03
2.90e-03
2.28e-03
1.41e-03
9.68e-04
5.55e-04
3.68e-04
2.03e-Q4
1.33e-04
9.62e-05
HCI"
Conservative
Concentration
(ppm)
0.00
0.00
1.23e-02
3.43e-01
7.24e-01
8.32e-01
7.74e-01
1.73e-K)l
1.47e+01
1.28e+01
9.37e-K)0
7.25e-K)0
5.92e-K)0
4.88e+00
4.03e-K)0
3.52e+00
2.57e-KM3
1.70e400
1.29e-K)0
7.71e-01
4.98e-01
2.97e-01
2.05e-01
1.22e-01
8.53e-02
6.46e-02
Typical
Concentration
(ppm)
0.00
0.00
0.00
0.00
0.00
2.73e-04
5.45e-04
6.90e-01
4.44e-01
4.21e-01
4.33e-01
4.35e-01
4.00e-01 /""
3.99e-01 v
4.10e-01
3.79e-01
3.53e-01
2.67e-01
2-lOe-Ol
1.30e-01
8.92e-02
5.11e-02
3.39e-02
1.87e-02
1.23e-02
8.86e-03
Notes:
1 Phosgene emission rate = 10.6 g/s.
2 HCI emission rate = 360 g/s. _ „.
3 Concentration = emission rate x concentration factor x 1.15 x _I
MW
Volume VII
Appendix VII-4
-53-
External Review Draft
Do not cite or quote
-------
TABLE 17
Maximum and Typical Phosgene and HCI Concentrations for the
Conservative Off-Site Fire Scenario
Meteorology
Downwind
(m)
100
200
300
400
500
600
700
800
900
1000
1250
1500
1750
2000
2250
2500
3000
4000
5000
7500
10000
15000
20000
30000
40000
50000
Concentration Factors
Conservative
Concentration
(ug/m3)/(g/s)
218.080
72.278
41.282
34.118
34.857
28.975
23.247
21.615
19.160
20.693
14.095
11.294
9.602
9.110
8.585
7.888
6.390
4.437
3.457
2.156
1.445
0.886
0.708
0.563
0.463
0.390
Typical
Concentration
(ug/mj)/(g/s)
0.927
0.635
0.731
0.666
0.510
0.317
0.202
0.156
0.118
0.113
0.057
0.051
0.050
0.053
0.057
0.086
0.085
0.093
0.087
0.098
0.112
0.118
0.113
0.095
0.077
0.064
Phosgene1-3
Conservative
Concentration
(ppm)
2.63e-K)0 .
8.71e-01
4.98e-01
4.11e-01
4.20e-01
3.49e-01
2.80e-01
2.61e-01
2.31e-01
2.49e-01
1.70e-01
1.36e-01
1.16e-01
1.10e-01
1.03e-01
9.51e-02
7.70e-02
5.35e-02
4.17e-02
2.60e-02
1.74e-02
1.07e-02
8.53e-03
6.79e-03
5.58e-03
4.70e-03
Typical
Concentration
(ppm)
1.12e-02
7.65e-03
8.81e-03
8.02e-03
6.15e-03
3.82e-03
2.43e-03
1.88e-03
1.42e-03
1.36e-03
6.81e-04
6.15e-04
5.97e-04
6.33e-04
6.81e-04
1.04e-03
1.02e-03
1.12e-03
1.05e-03
1.18e-03
1.35e-03
1.42e-03
1.36e-03
1.14e-03
9.28e-04
7.71e-04
HC1W
Conservative
Concentration
(ppm)
2.43e-K)2
8.04e+01
4.59e+OJ
3.80e+01
3.88e+01
3.22e+01
2.59e-K)l
2.40e+01
2.13e-K)l
2.30e-K)l
1.57e-K)l
1.26e-K)l
1.07e-K)l
l.Ole+01
9.55e-K)0
8.78+00
7.11e-K)0
4.94e-K)0
3.85e-K)0
2.40e+00
1.61e-K)0
9.86e-01
7.88e-01
6.26e-01
5.15e-01
4.34e-01
Typical
Concentration
(ppm)
1.03e+00
7.06e-01
8.13e-01
7.40e-01
5.67e-01
3.53e-01
2.25e-01
1.74e-01
1.31e-01
1.26e-01
6.29e-02
5.67e-02
5.51e-02
5.84e-02
6.29e-02
9.57e-02
9.40e-02
1.03e-01
9.68e-02
1.09e-01
1.25e-01 '
1.31e-01
1.26e-01
1.05e-01
8.57e-02
7.12e-02
Notes:
1 Phosgene emission rate = 43.2 g/s.
2 HCI emission rate = 1470 g/s.
3 Concentration = emission rate x concentration factor x 1.15 x —
MW
Volume VII
Appendix VIM
-54-
External Review Draft
Do not cite or quote
-------
TABLE 18 /--J
Maximum and Typical Phosgene and HC1 Concentrations for the Conservative
Mitigated On-Site Fire Scenario |
Meteorology
Downwind
(m)
100
200
300
400
500
600
700
800
900
1000
1250
1500
1750
2000
2250
2500
3000
4000
5000
7500
10000
15000
20000
30000
40000
50000
Concentration Factors
Conservative
Concentration
(ug/m3)/(g/s)
0
0
0.045
1.257
2.7
3.052
2.839
63.414
54.02
46.921
34.352
26.604
21.724
17.9
14.796
12.892
9.424
6.233
4.733
2.827
1.826
1.088 .
0.753
0.448
0.313
0.237
Typical
Concentration
(ug/m3)/(g/s)
0
0
0
0
0
0.001
0.002
2.5295
1.6285
1,543
1.5885
1.594
1.4675
1.465
1.503
1.3885
1.294
0.9795
0.7715
0.476
0.327
0.1875
0.1245
0.0685
0.045
0.0325
Phosgene1"1
Conservative
Concentration
(ppm)
0.00
0.00
2.22e-05
6.20e-04
1.33e-03
1.51e-03
1.40e-03
3.13e-02
2.66e-02
2.31e-02
1.69e-02
1.31e-02
1.07e-02
8.83e-03
7.30e-03
6.36e-03
4.65e-03
3.07e-03
2.33e-03
1.39e-03
9.01e-04
5.37e-04
3.71e-04
2.21e-04
1.54e-04
1.17e-04
Typical
Concentration
(ppm)
0.00
0.00
0.00
0.00
0.00
4.93e-07
9.86e-07
1.25e-03
8.03e-04
7.61e-04
7.84e-04
7.86e-04
7.24e-04
7.23e-04
7.41e-04
6.85e-04
6.38e-04
4.83e-04
3.81e-04
2.35e-04
1.61e-04
9.25e-05
6.14e-05
3.38e-05
2.22e-05
1.60e-05
HCP
Conservative
Concentration
(ppm)
0.00
0.00
2.04e-03
5.71e-02
1.23e-01
• 1.39e-01
1.29e-01
2.88e+00
2.45e+00
2.13e+00
1.56e-K)0
1.21e+00
9.87e-01
8.13e-01
6.72e-01
5.86e-01
4.28e-01
2.83e-01
2.15e-01
1.28e-01
8.30e-02
4.94e-02
3.42e-02
2.04e-02
1.42e-02
1.08e-02
Typical
Concentration
(ppm)
0.00
0.00
0.00
0.00
0.00
4.54e-05
9.09e-05
1.15e-01
7.40e-02
7.01e-02
7.22e-02
7.24e-02
6.67e-02
6.66e-02
6.83e-02 f
6.31e-02
5.88e-02
4.45e-02
3.51e-02
2.16e-02
1.49e-02
8.52e-03
5.66e-03
3.11e-03
2.04e-03
1.48e-03
Notes:
1 Phosgene emission rate = 10.6 g/s.
2 HC1 emission rate = 360 g/s.
3 Concentration = emission rate x concentration factor x 1.15 x —I x
MW 60
Volume VII
Appendix \Il-4
-55-
External Review Draft
Do not cite or quote
-------
TABLE 19
Average Emission Rates and Emission Durations
for the Release Scenarios
Scenario
On-Site Spill
• Fonnaldehyde/Methanol
• Acetone/Toluene
On-Site Fire
• HC1
• Phosgene
On-Site Mixing of Incompatible Wastes
• HC1
Off-Site Spill
• Formaldehyde/Methanol
• Acetone/Toluene
Off-Site Fire
• HC1
• Phosgene
Conservative
Emission
Rate
(g/s)
1,040
465
360
11
1,790
1,840
820
1,470
43
Emission
Duration
(sec)
3,120
18,240
7,030
7,030
1,200
1,740
10,320
430
430
Typical
Emission
Rate
(g/s)
94
42
150
4.5
71
94
42
76
2.2
Emission
Duration
(sec)
680
3,960
167
167
600
680
3,960
167
167
Volume VII
Appendix VII-4
-56-
Extemal Review Draf
Do not cite or quofe
-------
TABLE 20
Air Dispersion Modeling Results Based on Various Concentration Averaging Time
Chemical of
Concern
Formaldehyde
HC1
Emission
Scenario
Typical
Conservative
Meteorology
Typical
Conservative
Calm/Inversion
Typical
Conservative
Calm/Inversion
Release
Duration
(sec)
680
680
0
1200
1200
0
Concentration
Averaging
Time (sec)
680
1800
680
1800
305
1800
1200
1800
1200
1800
759
1800
LOC
(ppm)
9.6
9.6
9.6
9.6
9.6
9.6
9.9
9.9
9.9
9.9
9.9
9.9
IDLH
(ppm)
19.6
19.6
19.6
19.6
19.6
19.6
49.1
49.1
49.1
. 49.1
49.1
49.1
Max. Dist. to
LOC(m)'
240
100
1270
910
1950
1600
2230
1780
9110
8790
12840
12200
Max. Dist.
to
IDLH (m)1
140
40
850
550
1300
1000
870
680
3480
3190
4800
4620
Note:
1 All distances are measured from the property line to the east or west, across the Ohio river to the south, or from the existing railroad to the north,
whichever is closer to the spill.
Volume VII
External Review Draft
Do not cite r -^>te
-------
PROPOSED BUILDINGS
EXISTING FACILITIES
CONCRETE PAVEMENT
V%NX\S> BITUMINOUS PAVEMENT
LEGEND
NEw SECURITY FENCE
EXISTING FENCE
PROPERTY LIKE L CORNER
SIDE SLOPE
OBD
( PERSDMJEL GATE
EMERGENCY VEHICLE GATE
MAINTENANCE VEHICLE GATE
VEHICLE GATE
FIRE DEPARTMENT GATE
I/r (T C
I.,,I...I I
GRAPHIC SCALE
NOTES:
Figure 1: Source Area for On-Site Spill
-58-
-------
OH 1C
-------
O
I
Total
F ii i §
OrTnaKienyoe
Methanol
Steady-state
I
s
o>
s a
•* «>
I
Ul
s
I
5
csi
Time, sec
Figure 3: Rate of Evaporation of the 10% Formaldehyde/ 90% Methanol Liquid Pool
for the On-Site Spill Sce---*p (Conservative Emissions)
-------
a\
M
I
0.8
07
0.6
0.5
0.4
0.3
0.2
0.1
CO
Total
Acetone
• • — • Toluene
Steady-state
I
I
I
I
I
ui
f-
I
(O
CO
Time, sec
Figure 4: Rate of Evaporation of 10% Acetone/ 90% Toluene Liquid Pool
for the On-Site Spill Scenario (Conservative Emissions)
-------
H. REFERENCES
Briggs, G.A. 1975. Plume rise predictions. In Lectures on air pollution and
environmental impact analyses. American Meteorological Society.
Britter, R.E., and J. McQuaid. 1988. Workbook on the dispersion of dense gases. HSE
Contract Research Report No. 17/1988, Health and Safety Executive, Sheffield,
England.
Duttenhoeffer, R. et al. 1983. Highway Engineering, in Standard Handbook for Civil
Engineers, ed. by F.S. Merritt. McGraw-Hill Book Company, New York, NY.
Ermak, D.L. 1990. User's manual for the SLAB model, an atmospheric dispersion model
for denser-than-air releases, Lawrence Livermore National Laboratory UCRL-MA-
105607.
New Jersey Department of Environmental Protection (NJDEP). 1993. Toxic catastrophe
prevention act program. N.JA.C 7:31-3.9
Randerson, D. 1984. Atmospheric boundary layer in Atmospheric science and power
production, ed. by D. Randerson, United Sates Department of Energy. DOE/TIC-
27601. Washington, D.C.
Turner, D.B. 1967. Workbook of Atmospheric Dispersion Estimates. U.S. Department
of Health, Education, and Welfare, Publication No. 999-A1-26. Cincinnati, Ohio.
Tennekes, H. and Lumley, J.L. 1972. A first course in Turbulence, MIT Press,
Cambridge, Mass.
United States Department of Commerce (U.S. DOC). 1993. Statistical Abstract of the
United States: 1993 (113th Ed,). U.S. Bureau of the Census. Washington, D.C.
United States Environmental Protection Agency (U.S. EPA). Office of Health and
Environmental Assessment. 1985. Rapid assessment of exposure to paniculate
emissions from surface contamination sites. Washington, D.C. U.S. EPA/600/8-
85/002.
Volume VII External Review Draft
Appendix VII-4 Do not cite or quote
-62-
-------
U.S. Environmental Protection Agency (U.S.EPA), Management Agency (FEMA), and
United States Department of Transportation (USDOT). 1987. Technical guidance
for hazards analysis: (NTIS PB93-206910). December.
United States Environmental Protection Agency (U.S. EPA). 1988. Office of Air
Quality Planning and Standards. A workbook of screening techniques of assessing
impacts of toxic air pollutants. U.S. EPA-450/4-88-009. Research Triangle Park,
NC. September.
United States Environmental Protection Agency (U.S. EPA). 1992. Office of Air
Quality Planning and Standards. Workbook of screening techniques for assessing
impacts of toxic air pollutants (Revised). U.S. EPA-454/R-92-024. Research Triangle
Park, NC. May.
United States Environmental Protection Agency (U.S. EPA). 1993. Office of Air
Quality Planning and Standards. Guidance on the application of refined dispersion
models for hazardous/toxic air releases. U.S. EPA-454/R-93-002. Research Triangle
Park, NC. May.
01-3999CJCCOOB83.WS1
Volume VII External Review Draft
Appendix VII-4 Do not cite or quote
-63-
-------
ATTACHMENT 1
Ohio Department of Public Safety Data
Volume VII External Review Draft
Appendix VII-4 Do Not Cite or Quote
-------
rvcwvrww j^w.
FACSIMILE MESSAGE
OHIO DEPARTMENT OF PUBLIC SAFETY
TRAFFIC CRASH RECORDS SECTION
1952 NEST BROAD STREET
COLUMBUS, OHIO 43223
PHONE: €14/752-1575
FAX: 614/752-1363
•ft*****************************************************
THE DirORMATIOB COHTAIMBD IN THIS FACSIMILE MESSAGE IS CONFIDENTIAL BELONGING TO
THE SENDER. THE INFORMATION IS INTENDED ONLY FOR USE OF THE INDIVIDUAL OR ENTITY.
NAKED ABOVE. IF ANT PAGES ARE UNCLEAR OR THERE IS ANY PROBLEM WITH THIS
TRANSMISSION, PLEASE CALL IMMEDIATELY.
Volume YE External Review Draft
Appendix VIM °° Not Cite or
-------
V»
O
er-
ro
c-/
ris
*><•*
11
hi
2 *
u m
I!
** ^t
i!
^ i
«
M-g
h
* * 0*
a o e
o H a M
• e « o
1
:i!
Dun
I
i
g « 8*«P fi
^
I
Volume VH
Appendix VD-4
External Review Draft
Do Not Cite or Quote
-------
j
4 t
If
JS
I I
•j
1 i
• « a
^ I'
l~>\ It
fell1'
iij ^ii
|n
i1!
J 1
i
I
Volume VH
Appendix VH-4
mtt m
WWW
• m M
flH
qjjsS
!"'
H
n n
M
a °
s -
u
•5
1 1"
Hi
1
n HO
e o ••
ft •* M
B
ai
• M.
S | •
i »!f
j
H W«
N -1 «
I
| B||
I.!,
V
«
«
.5
'
M
*
3
n
X
I
&
I
1
External Review Draft
Do Not Cite or Quote
-------
"
•»•)<
8 -
9t *«•
iH
I
S
I I
\\
Volume VH
Appendix VH-4
External Review Draft
Do Not Cite or Quote
-------
1
I
8
5
y <
* I
2 Si
1
II *'
*S"
MM «•
<• rt 0
m H *«
r 2
i
I
,Sa z |jM
s
H
^ S
I I
i *
*
Volume VH
Appendix VD-4
External Review Draft
Do Not Cite or Quote
-------
i
T1
£
I I
46*.
S*o
i?
So
K H V
IP
•toe
e e
*> «» •< tt
i
Volume VH
Appendix VH-4
2
External Review Draft
Do Not Cite or Quote
-------
U O rt
ee e
0 e e
r> e e
Volume VH
Appendix VD-4
9 fc*M
• otttt
H
I S
It M
External Review Draft
Do Not Cite or Quote
-------
o
VJ
o
u
6s
M ve
H •> X
J
l!
*
!
lii
|:1
\i
i 1
.5 .
II
H
I
PSSSS
*!«• ft t>
Mft
* • n M «
r* r* A M e
•*•) •
t-i N « e «
1AM N «
sssss
8*? I
B g I a
i?1 | |
I I I
S 2
;
Volume \H
Appendix VU-4
H
External Review Draft
Do Not Cite or Quote
-------
8!
r-
if«
II:
s
fill
0 1
4J
^> «
ii ^
!i f
i
r*
i
1
Volume VH
Appendix VH-4
S
S
X
3S3
HIMM
S8XX
K >•» >
rj • • fl •
2 tililtlj
•
s
"
1
4i
1
\
3
^^
^
External Review Draft
Do Not Cite or Quote
-------
. if
tl M
« O
!
u B
-rl M
il
v • TC n • i
<««•«•
£ *40 00 rtC
n • •« o H A •>
•H -IHrlH C C 4>
J ! Him &
Volume VH o
Appendix VH-4
External Review Draft
Do Not Cite or Quote
-------
«l
!
I
is
5st
!•«
1
IS
r
8-3°
1
o|J
« O • PI
t- nn *l
M n M
•) •) rt O
SRP
O •» O
8
S"
M
"
lit 1;
Volume VH
Appendix VH-4
iH • • H
I << «
•rt -rt-rlTl 41 -rl-H 1)
H ,:$: £ c H 5
4 4>4l4>4l 1 f 4l4> I
§ *"5* I * " I
External Review Draft
Do Not Cite or Quote.
-------
8
\l
a*
h-
l
m
a n s
a o
3
u
I
I!
'
ns«
•10 w*i o ••
mm • M r- •» e
£ S5*S
10 o n o r< o
•• n «• •< M p<
i» <• r- H
NN O
*«4 M N TC *« n
•i mm •»•»••
a «
Volume
Appendix VH-4
External Review Draft
Do Not Cite or Quote
-------
It
ri e • M e
11 S"*"=8
E;
S*
Si
i
.!• f|
.1* f*
li*
li! I
1
s$J
I
:
Volume
Appendix VD-4
•« o o no
m v n • f
• ft 9
w N n
HUH N ft
•«••••>
Hl'J
H me
I
44 ?
»4wl W
"
il
S
s
External Review Draft
Do Not Cite or Quote
-------
: If
I
P
I «IM rt
> r» SJ N
n t- HI o e
ta WMO *> •
!•<•
I <• M
r< V « 00
I I iilll
Volume VH
Appendix VH-4
H »* H H 8
External Review Draft
Do Not Cite or Quote
-------
1
it
I*
zzz
CM •»
i
Ko8
"?:
a!
ill
"
I
;
"Volume VH
Appendix VIM
no H
M H
000
...
5«
S5
„„.
m *t M
85"
to
•4
* 3
0 *>
0 0
5 °
I s
5 H
3 o
0 P
s
s
•
0
:
•
o
It
5
Ji
e
S
a
•«
•
s
3
•
• j
e 8
.
il
1
External Review Draft
Do Not Cite or Quote
-------
8
w
i|
l!i
if*
V
§
!i
J5SS-5
o eo o«
•» *I4
MM
^ -- •"** K fi>£
* U «* a •
i I Ill^i
!
HHH
i f llill
Volume VD a ti **«8S
Appendix VII-4
5
External Review Draft
Do Not Cite or Quote
-------
•
ll
I
Is*
ji i:
«4
1
Volume VII
Appendix VD-4
ii
ii1
§3*
1*8 3
BS: *
*eJ
1
S
1
eeoe
I M M •
599
O ft
liil
f*fi
iiii
fil
3 l«i
i «**
3
«
5
a M *
hi 1
External Review Draft
Do Not Cite or Quote
-------
ATTACHMENT 2
Ohio Department of Transportation Data
Volume VH External Review Draft
Appendix VH-4 Do Not Cite or Quote
-------
George V. Voinovieh
Governor
25 South Front Street
P.O. Box 899
Columbus, Ohio 43216-0899
August 31, 1995
Ms. Daune Arnsow
ENVIRON
.214 Carnegie Center
Princeton, New Jersey 08540-6284
Re: Travel Data for SR 39 in East Liverpool, Columbiana County
Dear Ms. Arnsow:
We have prepared the attached data sheet in response to the subject request. The information was
extracted from our historic Highway Performance Monitoring System databases.
The traffic data was available for each section of SR 39 at the state, county and incorporated level. The
HPMS truck information, however, was not available on a sufficient number of sections to be
particularly meaningful except, possibly, at the State level. Furthermore, the HPMS sections with the
additional truck data are selected for statistical adequacy upon a basis that is not necessarily sufficient
for projecting a single route, even at the State-wide level.
The SR 39 data is only for those sections of SR 39 that are primary routes. In other words, those
sections of SR 39 "overlapping" with other route(s) with a higher functional class, a higher jurisdictional
level (interstate or US route), or a lower route number at the same jurisdictional level, are not included in
this data. In Columbiana County, such sections would be where SR 39 follows SR 7 and US 30.
Some additional truck data was available in the current State "traffic book" database. The truck data
from that file represents East Liverpool and Columbiana County for approximately 1992-94, and the
State for about 1990-1994. The values computed from the traffic book's data are as follows:
East Liverpool
Columbiana County
State of Ohio
SR 39 traffic is 11.20% trucks
SR 39 traffic is 7.00% trucks
SR 39 traffic is 6.70% trucks
_ s
Volume VH
External Review Draft
Do Not Cite or Quote
-------
August 31, 1995
ENVIRON - page 2
Please note that the HPMS truck data indicates that the proportions of SR 39 truck travel in Columbi
County range from 8% (1990-91) to 5% (1992-94) of the total vehicle travel, and at the State wide lew.,
about 8%.
Please do not hesitate to call Ms. Andrea Goldberg of my staff (614)466-2697 if you have any questions
or require additional information.
Respectfully,
James E. McQuirt, P.E.
Administrator
Office of Technical Services
JEM:db
Attachment
-T . -irrr External Review Draft
Volume Vn Do Not Cite or Quote
Appendix VTJ-4
-------
ATTACHMENT
1) Estimated Daily Vehicle Miles Traveled (DVMT) for Columbiana County
DVMT
2)
1990
1991
1992
1993
1994
SR 39 State-Wide Data
2,480,770
2,550,010
2,695,350
2,671,490
2,724,910
All
DVMT
(projected from 1993)
Truck
DVMT Miles
1990
1991
1992
1993
1994
613,901
624,036
640,018
694,641
705,359
3) SR 39 Columbiana County Data
All
DVMT
53,924
56,251
48,588
56,085
56,950
Truck
DVMT
140.90
140.90
140.74
140.74
140.74
Miles
1990
1991
1992
1993
1994
81,093
82,074
82,168
84,292
86,180
4) SR 39 East Liverpool Urban Area Data
All
DVMT
6,487
6,566
4,108
4,215
4,309
Truck
DVMT
17.11
17.11
17.11
17.08
17.08
Miles
1990
1991
1992
1993
1994
35,178
35,417
31,830
32,496
33,877
3.39
3.39
3.39
3.36
3.36
a) New traffic counts taken for Columbiana County in 1992. 1990 and 1991 counts are projections of the
previous (circa 1988) counts; 1993 and 1994 arc projections of the 1992 counts.
b) Truck information is based upon a sample of approximately 11.5% of the statewide mileage and
approximately 2% of the Columbiana County mileage. No truck breakdowns were available within Easi
Lb*MBftOVlI External Review Draft
.. ,m ., Do Not Cite or Quote
Appendix VII-4
-------
ATTACHMENT 1
Program AIRCONC
Volume VII - External Review Draft
Appendix VII-4 Do Not Cite or Quote
-------
program airconc
integer indexl, indexh,npts,nmet,nblank,iloc
double precision mfrac,loc,idlh
character*80 filenm,fileout,chem
character*80 junk
character*? seen,locat,durat,meteo
double precision xp(54,61), zm(54,61), cvpm(54,61), timp(54,61)
double precision maxconc(24),maxdist
dou'ble precision tcld(54,61) ,conc(54,24)
double precision x(24), rmin, rmax, distl, dist2,xloc(13)
data X/25,50,100,200,300,400,500,600,700,800,900,1000,1250,1500
1 1750,2000,2250,2500,3000,4000,5000,10000,15000,20000
data xloc/0.0001,0.0005,0.001,0.005,0.01,0.05, 0.1,0.5,1.0,5.0,
1 10.0,50.0,100.07
open(unit=5,file='ppm.dat',status='old')
read(5,130) filenm
open(unit=3,file=filenm, status='old')
fileout = 'ppm'// filenm(4:9)
open(unit=7,file=fileout, status='new')
read(5,132) mfrac
•*~~-*JfC 1 *> *> \ 1 r*.r*
,
read (5, 132) loc
• read (5, 132) idlh
. read (5, 130) chem
read (5, 131) seen
read (5, 131) locat
read (5, 131) meteo
read (5, 131) durat
if (meteo . eg . ' WORST ' ) then
nmet = 54
else
nmet = 1
endif
, filenm
locat
npts =24
write (7, 133) 'From Slab output f ile: '
write (7,129)' Scenario : ' , seen
write (7 ,129) 'Accident Location: ' , l
write (7, 12 9) 'Duration: ' , durat
write (7 , 129) 'Meteorology: ' , meteo
write (7, 133) 'Chemical: ', chem
write (7, 134) 'Vapor phase mole fraction: ', mfrac
''
wrte (7 , 134 : ,
if (nmet.eq.l) nblank = 323
if (nmet. eq. 54) nblank = 5
do 10 j =1, nmet
,
do 12 k = 1, nblank
read (3, 130) junk
12 continue
continue
read (3,135) (xp(j,i),
l cvpm(3,i), i * 1,61)
10 continue
find interpolation indeces
if(locat.eq.'ON-SITE') then
write(7,*)'*Output adjusted to be distance from fenceline.'
do 29 1*1,61
do 28 j = l,nmet
xp(},i) = xp(j,i) - (250.73.2808)
28 continue
29 continue
endif
do 30 j = 1, nmet
do 35 k=l, npts
if(xp(j,61).ge.x(k)) then
do 40 i = 1, 61
if(xp(j,i).le.x(k)) then
indexl = i
-------
indexh = i+1
endif
40 continue
distl - xp(j,indexh) - xp(j,indexl)
dist2 - x(k) - xp(j,indexl)
rmax - cvpm(j,indexh)
rmin = cvpm(},indexl)
cone(j,k)=mfrac*le+06*((dist2*(rmax-rmin)/distl)+rmin)
else
npts = k-l
goto 30
endif
35 continue
30 continue
if (nmet.ne.l) then
write(7,145)'X,m',(i,i=i,27)
write(7,140) (x(i),(conc(j,i), j=l,27), i=l,npts)
write(7,145)'X/m',(i,i=28,nmet)
write(7/140) (x(i),(conc(j,i), j=28,nmet), i=l,npts)
endif
do 45 k = 1, npts
maxconc(k) - 0.0
45 . continue
write(7,147) 'X,m', 'Max concentration, ppm'
do 50 k=l,npts
do 60 j - l, nmet
maxconc(k) = max(naxconc(k),cone(j,k))
60 continue
write(7,150) x(k), maxconc(k)
50 continue
c find distances to fractions of LOG
write(7,*)
write(7,*)
write(7,155)'Concentration (ppn)', 'Distance to (m)'
c do 80 iloc = 1/13
do 80 iloc = 9,9
maxdist - 0.0
indexl=l
indexh=l
do 70 k=npts,l,-l
if (maxconc(k).le.(xloc(iloc)*loc)) then
indexl=k
indexh=k-l
endif
70 continue
if (maxconc(1).ge.(xloc(iloc)*loc).and.
1 maxconc(npts).le.(xloc(iloc)*loc)) then
distl = maxconc(indexh)-maxconc(index1)
dist2 - maxconc(indexh)-(xloc(iloc)*loc)
rmax = x(indexh)
rmin - x(indexl)
maxdist=rmax - (dist2*(rmax-rmin)/distl)
write(7,160) loc*xloc(iloc), maxdist
endif
if (maxconc(1).le.(loc*xloc(iloc))) then
write(7,165) loc*xloc(iloc),' less than', x(l)
endif
if (maxconc(npts).ge.(loc*xloc(iloc))) then
write(7,165) loc*xloc(iloc),' greater than', x(npts)
endif
80 continue
c find distance to the IDLH
maxdist =0.0
indexl=l
indexh=l
do 95 k=npts,l,-l
-------
if(maxconc(k).le.idlh) then
indexl=k
indexh=k-l
endif
>5 continue
if(maxconc(1).ge.idlh.and.
1 maxconc(npts).le.idlh) then
distl - maxconc(indexh)-maxconc(indexl)
dist2 = maxconc(indexh)-idlh
rmax - x(indexh)
rmin = x(indexl)
maxdist=rmax - (dist2*(rmax-rmin)/distl)
write(7,l61) idlh, maxdist
endif
if (maxconc(1).le.idlh) then
write(7,166) idlh,' less than', x(l)
endif
if (maxconc(npts).ge.idlh) then
write(7,i66) idlh,' greater than', x(npts)
endif
130 format (A80)
131 format (A7)
132 format (f!2.3)
129 format (A26,T40,A7)
133 format (A26,T40,A80)
134 format (A26,T40,fl2.3)
135 format (e!2.2,42xrell.2)
136 format (2el2.2)
140 format (28fl2.2)
145 format (A12,27112)
147 format(/,A12,3x,A22 /, 40('-'))
150 format (F12'.2,3x,F12.2)
155 format (//,A19,8x,A15 /,40('='))
156 format (2F12.2)
160 format ('LOG',5x,F12.4,8x,F12.2)
161 format ('IDLH',4x,F12.4,8x,F12.2)
165 format ('LOG',3x,F12.4,A15, F12.2)
166 format ('IDLH',2x,F12.4,A15, F12.2)
end
-------
ATTACHMENT 2
SLAB Output for the On-Site Spill Scenario
Volume VH External Review Draft
Appendix VH-4 Do Not Cite or Quote
-------
RUN01.0UT
problem input
idspl >
ncalc *
urns *
cps =
tbp =
cmedO *
dhe •
cpsl •
rhosl *
spb =
spc s
ts =
qs =
as =
tsd =
qtis =
hs
t8V =
xffin =
zp(1) -
zp<2) =
zpC3) =
zp(4> *
zO
za =
ua =
ta =
rh
stab «
1
1
.031880
909.80
309.35
.00
1070000.
2716.00
793.70
-1.00
.00
293.00
1.04
418.00
3120.
.00
.00
1800.00
20000.00
.00
.00
.00
.00
.300000
10.00
3.20
293.00
68.00
4.00
release gas properties
molecular weight of source gas (kg)
vapor heat capacity, const, p. (j/kg-k)
temperature of source gas (k)
density of source gas {kg/m3)
boiling point temperature
liquid mass fraction
liquid heat capacity (j/kg-k)
heat of vaporization (j/kg)
liquid source density (kg/mS)
saturation pressure constant
saturation pressure constant (k)
saturation pressure constant (k)
spill characteristics
spill type
mass source rate (kg/s)
continuous source duration (s)
continuous source mass (kg)
instantaneous source mss (kg)
source area (m2)
vertical vapor velocity (*/s)
source half width (n)
source height (m)
horizontal vapor velocity (m/s)
field parameters
concentration averaging time (s)
mixing layer height (m)
maximum downwind distrace (n)
concentration measurement height (n)
urns *
cps *
ts *
rhos *
tbp «
cmedO*
cpsl *
dhe *
rhosl*
spa «
spb *
spc «
idspl
q*
tsd
qtcs
qtis
as
MS
bs
hs
us
tav *
hmx >
xf fn *
z*X1>-
zp(2)«
zp(3)«
zp(4)«
3.1880E-02
9.09806*02
3.0935E+02
1.25596*00
3.09356*02
0.00006*00
2.71606*03
1.07006*06
7.93706*02
1.32636*01
4.10286*03
O.OOOOE+00
1
1.04006*00
3.12006*03
3.24486*03
0.00006*00
4.18006*02
1.98116-03
1.02236*01
0.00006*00
0.00006*00
1.80006*03
1.04006*03
2.00006*04
0.00006*00
0.00006*00
0.00006*00
0.00006*00
-------
anbient meteorological properties
molecular weight of ambient air (kg)
heat capacity of anbient air at const p. (j/kg-k)- cpaa
density of anbient air (kg/m3) - rhoa
anbient measurement height (m) - za
anbient atmospheric pressure (pa*n/m2*j/m3) - pa
anbient wind speed (m/s) - ua
anbient temperature (k) - ta
relative humidity (percent) - rh
ambient friction velocity (m/s) - uastr
atmospheric stability class value - stab
inverse monin-obukhov length (1/m) - ala
surface roughness height (m) - zO
2.8783E-02
1.0144E+03
1.1972E+00
1.0000E+01
1.0133E+05
3.2000E+00
2.9300E+02
6.8000E+01
3.7515E-01
4.0000E+00
O.OOOOE+00
3.0000E-01
additional parameters
sub-step multiplier
number of calculations! sub-steps
acceleration of gravity (m/s2)
gas constant (j/mol- k)
von karman constant
1
- ncalc
- nssm
- grav
• rr
- xk
1
3
9.8067E+00
8.3U3E+00
4.1000E-01
instantaneous spatially averaged cloud parameters
X
1.02E+01
8.18E+00
6.13E+00
4.09E+00
2.04E+00
1.55E-06
2.04E+00
4.09E+00
6.13E+00
8.18E+00
1.02E+01
1 .04E+01
1.07E+01
1.10E+01
1.15E+01
1.19E+01
1.25E+01
1 .33E+01
1.42E+01
1.53E+01
1 .666+01
1.82E+01
2.02E+01
2.25E+01
2.55E+01
2.90E+01
3.33E+01
3.86E+01
4.50E+01
5.29E+01
6.24E+01
7.40E+01
8.82E+01
1 .05E+02
1 .27E+02
1.52E+02
1.B3E+02
2.21E+02
2.68E+02
3.24E+02
3.93E+02
4.77E+02
5.79E+02
7.04E+02
zc
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
h
O.OOE+00
1.75E+00
2.37E+00
2.86E+00
3.29E+00
3.67E+00
4.03E+00
4.36E+00
4.67E+00
4.97E+00
5.25E+00
5.28E+00
5.32E+00
5.36E+00
5.42E+00
5.48E+00
5.56E+00
5.65E+00
5.77E+00
S.90E+00
6.06E+00
6.26E+00
6.49E+00
6.77E+00
7.09E+00
7.48E+00
7.93E+00
8.46E+00
9.08E+00
9.80E+00
1.06E+01
1.16E+01
1.27E+01
1.40E+01
1.55E+01
1.72E+01
1.92E+01 i
2.15E+01 i
2.42E+01 i
2.72E+01 !
3.08E+01 :
3.48E+01 :
3.95E+01 t
4.50E+01 '
bb
.02E+01
.04E+01
.OSE+01
.06E+01
.07E+01
.08E+01
.09E+01
.10E+01
.12E+01
.13E+01
.14E+01
.14E+01
.14E+01
.14E+01
.15E+01
.1SE+01
.15E+01
.16E+01
I.16E+01
I.17E+01
I.18E+01
I.18E+01
I.20E+01
I.21E+01
I.23E+01
I.25E+01
I.27E+01
I.30E+01
I.34E+01
I.38E+01
I.44E+01
I.51E+01
I.59E+01
I.69E+01
I.81E+01
I.95E+01
2.12E+01
2.34E+01
2.59E+01
2.90E+01
S.26E+01
S.70E+01
I.23E+01
I.85E+01
b
9.20E+00
9.20E+00
9.20E+00
9.20E+00
9.20E+00
9.20E+00
9.21E+00
9.21E+00
9.21E+00
9.22E+00
.22E+00
-22E+00
.22E+00
.22E+00
.22E+00
.22E+00
9.22E+00
9.23E+00
9.23E+00
9.23E+00
9.23E+00
9.24E+00
9.24E+00
9.25E+00
9.25E+00
9.26E+00
9.27E+00-
9.29E+00
9.30E+00
9.33E+00
9.35E+00
9.38E+00
9.41E+00
9.45E+00
9.49E+00
9.54E+00
9.59E+00
9.64E+00
9.69E+00
9.75E+00
9.80E+00
9.85E+00
9.90E+00
9.94E+00
be*
.02E+01
.13E+01
.24E+01
.35E+01
.45E+01
.S6E+01
.67E+01
.78E+01
.89E+01
2.00E+01
2.10E+01
2.13E+01
2.16E+01
2.19E+01
2.23E+01
2.29E+01
2.35E+01
2.43E+01
2.52E+01
2.64E+01
2.78E+01
2.95E+01
3.15E+01
3.41E+01
3.72E+01
4.09E+01
4.5SE+01
5.11E+01
5.79E+01
6.61E+01
7.62E+01
8.8SE+01
1.04E+02
1.22E+02
1.44E+02
1.71E+02
2.04E+02
2.44E+02
2.93E+02
3.53E+02
4.26E+02
5.15E+02
6.23E+02
7.55E+02
bx
1.02E+01
1.13E+01
1.24E+01
1.35E+01
1.45E+01
1.56E+01
1 .67E+01
1.78E+01
1.89E+01
2.00E+01
2.10E+01
2.13E+01
2.16E+01
2.19E+01
2.23E+01
2.29E+01
2.35E+01
2.43E+01
2.52E+01
2.64E+01
2.78E+01
2.95E+01
3.1SE+01
3.41E+01
3.71E+01
4.09E+01
4.55E+01
5.11E+01
5.79E+01
6.61E+01
7.62E+01
8.8SE+01
1.04E+02
1.22E+02
1 .44E+02
1.71E+02
2.04E+02
2.44E+02
2.93E+02
3.53E+02
4.26E+02
5.15E+02
6.23E+02
7.55E+02
cv
O.OOE+00
2.39E-03
2.80E-03
3.05E-03
3.22E-03
3.35E-03
3.46E-03
3.54E-03
3.61E-03
3.67E-03
3.71E-03
3.68E-03
3.64E-03
3.59E-03
3.53E-03
3.46E-03
3.38E-03
3.28E-03
3.17E-03
3.05E-03
2.91E-03
2.76E-03
2.59E-03
2.42E-03
2.23E-03
2.03E-03
1.83E-03
1.64E-03
1.44E-03
1.26E-03
1.08E-03
9.1SE-04
7.66E-04
6.33E-04
5.17E-04
4.16E-04
3.31E-04
2.60E-04
2.02E-04
1.55E-04
1.18E-04
8.87E-05
6.63E-05
4.91E-05
rho
1.20E+00
1 .20E+00
1.20E+00
1.20E+00
1.20E+00
1.20E+00
1 .20E+00
1 .20E+00
1.20E+00
1.20E+00
1.20E+00
1.20E+00
1.20E+00
1.20E+00
1.20E+00
1.20E+00
1 .20E+00
1.20E+00
1.20E+00
1 .20E+00
1 .20E+00
1.20E+00
1 .20E+00
1.20E+00
1.20E+00
1 .20E+00
1.20E+00
1.20E+00
1.20E+00
1.20E+00
1.20E+00
1.20E+00
1.20E+00
1.20E+00
1.20E+00
1.20E+00
1.20E+00
1.20E+00
1.20E+00
1.20E+00
1.20E+00
1.20E+00
1.20E+00
1.20E+00
t
2.93E+02
2.93E+02
2.93E+02
2.93E+02
2.93E+02
2.93E+02
2.93E+02
2.93E+02
2.93E+02
2.93E+02
2.93E+02
2.93E+02
2.93E+02
2.93E+02
2.93E+02
2.93E+02
2.93E+02
2.93E+02
2.93E+02
2.93E+02
2.93E+02
2.93E+02
2.93E+02
2.93E+02
2.93E+02
2.93E+02
2.93E+02
2.93E+02
2.93E+02
2.93E+02
2.93E+02
2.93E+02
2.93E+02
2.93E+02
2.93E+02
2.93E+02
2.93E+02
2.93E+02
2.93E+02
2.93E+02
2.93E+02
2.93E+02
2.93E+02
2.93E+02
u
O.OOE+00
9.05E-01
.13E+00
.27E+00
.38E+00
.47E+00
.5SE+00
1 .61E+00
1.67E+00
1.72E+00
1.77E+00
1.77E+00
1.78E+00
1.78E+00
1.79E+00
1 .80E+00
1 .81E+00
1 .83E+00
1 .85E+00
1.87E+00
1.89E+00
1.92E+00
1.95E+00
1.98E+00
2.02E+00
2.07E+00
2.12E+00
2.18E+00
2.24E+00
2.30E+00
2.38E+00
2.45E+00
2.53E+00
2.62E+00
2.71E+00
2.80E+00
2.90E+00
3.00E+00
3.10E+00
3.21E+00
3.32E+00
3.43E+00
3.54E+00
3.66E+00
ua
O.OOE+00
9.08E-01
1.13E+00
1.28E+00
1 .39E+00
1.48E+00
1.55E+00
1 .62E+00
1 .67E+00
1.73E+00
1.77E+00
.78E+00
.78E+00
.79E+00
.BOE+00
.81E+00
.82E+00
1.83E+00
1 .85E+00
1 .87E+00
1 .89E+00
1.92E+00
1 .95E+00
1.99E+00
2.03E+00
2.07E+00
2.12E+00
2.18E+00
2.24E+00
2.31E+00
2.38E+00
2.46E+00
2.54E+00
2.62E+00
2.71E+00
2.81E+00
2.90E+OC
3.00E+00
3.11E+00
3.21E+00
3.32E+00
3.43E+00
3.54E+00
3.66E+00
-------
8.56E+02
1.04E+03
1.27E+03
1.54E+03
1.8BE+03
2.28E+03
2.78E+03
3.39E+03
4.12E+03
5.02E+03
6.12E+03
7.45E+03
9.10E+03
1.12E+04
1 .37E+04
1 .69E+04
2.08E+04
1
X
-1.02E+01
-8.18E+00
-6.13E+00
-4.09E+00
-2.04E+00
-1-.55E-06
2.04E+00
4.09E+00
6.13E+00
8.18E+00
1 .02E+01
1.04E+01
1.07E+01
1.10E+01
1.15E+01
1.19E+01
1.25E+01
1.33E+01
1.42E+01
1 -53E+01
1 .66E+01
1 .82E+01
2.02E+01
2.25E+01
2.55E+01
2.90E+01
3.33E*01
3.86E+01
4.50E+01
5.29E+01
6.24E+01
7.40E+01
8.82E+01
1.05E+02
1.27E+02
1 .52E+02
1 .83E+02
2.21E+02
2.68E+02
3.24E+02
3.93E+02
4.77E+02
5.79E*02
7.04E+02
8.56E+02
1.04E+03
1.27E+03
1.54E4-03
1.88E+03
2.28E+03
2.78E+03
3.39E+03
4.12E+03
5.02E+03
6.12E+03
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
on
O.OOE+00
2.65E-03
3.10E-03
3.37E-03
3.57E-03
3.71E-03
3.83E-03
3.92E-03
4.00E-03
4.06E-03
4.11E-03
4.07E-03
4.03E-03
3.97E-03
3.90E-03
3.83E-03
3.74E-03
3.63E-03
3.51E-03
3.3BE-03
3.23E-03
3.06E-03
2.87E-03
2.68E-03
2.47E-03
2.25E-03
2.03E-03
1.81E-03
1.60E-03
1.39E-03
1.19E-03
1.01E-03
8.49E-04
7.02E-04
5.72E-04
4.61E-04
3.67E-04
2.88E-04
2.24E-04
1.72E-04
1.30E-04
9.82E-OS
7.34E-05
5.44E-05
4.01E-05
2.95E-05
2.15E-05
1.57E-05
1.14E-05
8.34E-06
6.07E-06
4.43E-06
3.24E-06
2.38E-06
1.75E-06
5.13E+01
5.86E+01
6.69E+01
7.66E+01
8.78E+01
1.01E+02
1.16E+02
1.33E+02
1 .52E+02
1.75E+02
2.00E+02
2.30E+02
2.68E+02
3.13E+02
3.62E+02
4.17E+02
4.78E+02
cmv
O.OOE+00
2.65E-03
3.10E-03
3.37E-03
3.57E-03
3.71E-03
3.83E-03
3.92E-03
4.00E-03
4.06E-03
4.11E-03
4.07E-03
4.03E-03
3.97E-03
3.90E-03
3.83E-03
3.74E-03
3.63E-03
3.51E-03
3.38E-03
3.23E-03
3.06E-03
2.87E-03
2.68E-03
2.47E-03
2.25E-03
2.03E-03
.81E-03
.60E-03
.39E-03
.196-03
.01E-03
8.49E-04
7.02E-04
5.72E-04
4.61E-04
3.67E-04
2.88E-04
2.24E-04
1.72E-04
1.30E-04
9.82E-05
7.34E-05
5.44E-05
4.01E-05
2.95E-05
2.15E-05
1.57E-05
1. 14E-05
8.34E-06
6.07E-06
4.43E-06
3.24E-06
2.38E-06
1.75E-06
5.59E+01
6.47E+01
7.52E+01
8.74E+01
1.02E+02
1.19E+02
1.38E+02
1.61E+02
1.87E+02
2.16E+02
2.50E+02
2.89E+02
3.34E+02
3.85E+02
4.43E+02
5.10E+02
5.86E+02
cfflda
9.90E-01
9.87E-01
9.87E-01
9.87E-01
9.86E-01
9.86E-01
9.86E-01
9.86E-01
9.86E-01
9.86E-01
9.86E-01
9.86E-01
9.86E-01
9.86E-01
9.86E-01
9.86E-01
9.86E-01
9.86E-01
9.86E-01
9.87E-01
9.87E-01
9.87E-01
9.87E-01
9.87E-01
9.87E-01
9.88E-01
9.88E-01
9.8BE-01
9.88E-01
9.89E-01
9.89E-01
9.89E-01
9.89E-01
9.89E-01
9.89E-01
9.89E-01
9.90E-01
9.90E-01
9.90E-01
9.90E-01
9.90E-01
9.90E-01
9.90E-01
9.90E-01
9.90E-01
9.90E-01
9.90E-01
9.90E-01
9.90E-01
9.90E-01
9.90E-01
9.90E-01
9.90E-01
9.90E-01
9.90E-01
9.99E+00
1 .OOE+01
1.01E+01
1.01E+01
.01E+01
.01E+01
.02E+01
.02E+01
.02E+01
-02E+01
.02E+01
.02E+01
.02E+01
.02E+01
1.02E+01
1.02E+01
1.02E+01
COM
1.01E-02
1.01E-02
1.01E-02
1.01E-02
1.01E-02
1.01E-02
1.01E-02
1.01E-02
1.01E-02
1.01E-02
1.01E-02
1.01E-02
1.01E-02
1.01E-02
1.01E-02
1.01E-02
1.01E-02
1.01E-02
1.01E-02
1.01E-02
1.01E-02
1.01E-02
1.01E-02
1.01E-02
1.01E-02
1.01E-02
1.01E-02
1.01E-02
1.01E-02
1.01E-02
1.01E-02
1.01E-02
1.01E-02
1.01E-02
1.01E-02
1.01E-02
1.01E-02
1.01E-02
1.01E-02
1.01E-02
1.01E-02
1.01E-02
1.01E-02
1.01E-02
1.01E-02
1.01E-02
1.01E-02
1.01E-02
1.01E-02
1.01E-02
1.01E-02
1.01E-02
1.01E-02
1.01E-02
1.01E-02
9.15E+02
1.11E+03
1.35E+03
1.64E+03
1.99E+03
2.42E+03
2.9SE+03
3.59E+03
4.37E+03
S.32E+03
6.48E+03
7.89E+03
8.18E+03
8.S2E+03
8.93E+03
9.42E+03
1.00E+04
cnwv
1.01E-02
1.01E-02
1.01E-02
1.01E-02
1.01E-02
1.01E-02
1.01E-02
1.01E-02
1.01E-02
1.01E-02
1.01E-02
1.01E-02
1.01E-02
1.01E-02
1.01E-02
1.01E-02
1.01E-02
1.01E-02
; 1.01E-02
1.01E-02
1.01E-02
1.01E-02
1.01E-02
1.01E-02
1.01E-02
1.01E-02
1.01E-02
1.01E-02
1.01E-02
1.01E-02
1.01E-02
1.01E-02
1.01E-02
1.01E-02
1.01E-02
1.01E-02
1.01E-02
1.01E-02
1.01E-02
1.01E-02
1. 016-02
1.01E-02
1.01E-02
1.01E-02
1.01E-02
1.01E-02
1.01E-02
1.01E-02
1.01E-02
1.01E-02
1.01E-02
1.01E-02
1.01E-02
1.01E-02
1.01E-02
9.15E+02
1.11E+03
1.3SE+03
1.64E+03
1.99E+03
2.42E+03
2.9SE+03
3.S9E+03
4.37E+03
5.32E+03
6.48E+03
7.89E+03
7.89E+03
7.89E+03
7.89E+03
7.89E+03
7.89E+03
we
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
3.62E-05
2.66E-05
1.94E-05
1.42E-05
1.03E-05
7.53E-06
5.48E-06
4.00E-06
2.93E-06
2.15E-06
1.58E-06
1.17E-06
8.36E-07
S.98E-07
4.27E-07
3.05E-07
2.18E-07
vg
O.OOE+00
1.84E-04
4.71E-04
8.16E-04
1.20E-03
1.62E-03
2.07E-03
2.54E-03
3.02E-03
3.S3E-03
4.04E-03
4.10E-03
4.171-03
4.25E-03
4.3SE-03
4.46E-03
4.60E-03
4.76E-03
4.95E-03
S.16E-03
5.41E-03
5.69E-03
6.00f-03
6.35E-03
6.73E-03
7.13E-03
7.56E-03
7.99E-03
8.42E-03
8.83E-03
9.20E-03
9.52E-03
9.75E-03
9.88E-03
9.91E-03
9.80E-03
9.57E-03
9.22E-03
8.75E-03
8.19E-03
7.57E-03
6.91E-03
6.24E-03
S.57E-03
4.92E-03
4.31E-03
3.72E-03
3.19E-03
2.72E-03
2.33E-03
2.03E-03
1.79E-03
1.5BE-03
1.35E-03
1.17E-03
1.20E+00
1.20E+00
1.20E+00
1.20E+00
1.20E+00
1.20E+00
1.20E+00
1.20E+00
1.20E+00
1.20E+00
1.20E+00
1.20E+00
1.20E+00
1.20E+00
1.20E+00
1.20E+00
1 .20E+00
ug
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
2.93E+02
2.93E+02
2.93E+02
2.93E+02
2.93E+02
2.93E+02
2.93E+02
2.93E+02
2.93E+02
2.93E+02
2.93E+02
2.93E+02
2.93E+02
2.93E+02
2.93E+02
2.93E+02
2.93E+02
w
4.12E-01
3.37E-01
2.87E-01
2.62E-01
2.47E-01
2.36E-01
2.27E-01
2.20E-01
2.UE-01
2.09E-01
2.05E-01
2.05E-01
2.04E-01
2.04E-01
2.03E-01
2.02E-01
2.01E-01
2.00E-01
1.99E-01
1.97E-01
1.95E-01
1.93E-01
1.91E-01
1.88E-01
1.86E-01
1.S3E-01
1.79E-01
1.76E-01
1.72E-01
1.69E-01
1.65E-01
1.61E-01
1.57E-01
1.53E-01
1.49E-01
1.4SE-01
1.41E-01
1.37E-01
1.33E-01
.29E-01
.26E-01
.22E-01
.18E-01
.15E-01
.11E-01
.08E-01
1.04E-01
1.01E-01
9.75E-02
9.41E-02
9.07E-02
8.72E-02
8.37E-02
8.00E-02
7.63E-02
3.77E+00
3.89E+00
4.01E+00
4.13E+00
4.24E+00
4.36E+00
4.48E+00
4.60E+00
4.72E+00
4.83E+00
4.95E+00
5.06E+00
5.19E+00
5.31E+00
S.42E+00
S.52E+Ot)
5.62E+00
V
1.04E-01
2.85E-02
3.55E-02
4.00E-02
4.35E-02
4.62E-02
4.86E-02
5.06E-02
S.24E-02
5.40E-02
5.S4E-02
5.56E-02
5.57E-02
5.60E-02
5.62E-02
5.65E-02
S.69E-02
S.73E-02
5.78E-02
5.84E-02
5.92E-02
6.00E-02
6.09E-02
6.20E-02
6.32E-02
6.46E-02
6.61E-02
6.78E-02
6.96E-02
7.16E-02
7.37E-02
7.59E-02
7.81E-02
8.05E-02
8.29E-02
8.54E-02
8.78E-02
9.02E-02
9.25E-02
9.47E-02
9.68E-02
9.86E-02
1.00E-01
1.02E-01
1.02E-01
1.03E-01
1.03E-01
1.02E-01
1.01E-01
1.00E-01
9.79E-02
9.54E-02
9.24E-02
8.90E-02
8.52E-02
3.77E+00
3.89E+00
4.01E+00
4.13E+00
4.25E+00
4.37E+00
4.49E+00
4.60E+00
4.72E+00
4.84E+00
4.9SE+00
5.06E+00
5.19E+00
5.31E+00
5.42E+00
5.53E+00
5.62E+00
vx
O.OOE+00
3.45E-01
3.83E-01
4.05E-01
4.19E-01
4.30E-01
4.39E-01
4.46E-01
4.52E-01
4.57E-01
4.61E-01
4.62E-01
4.62E-01
4.63E-01
4.64E-01
4.6SE-01
4.66E-01
4.67E-01
4.68E-01
4.70E-01
4.72E-01
4.74E-01
4.77E-01
4.79E-01
4.82E-01
4.86E-01
4.89E-01
4.93E-01
4.97E-01
5.01E-01
5.05E-01
5.09E-01
5.12E-01
S.16E-01
5.20E-01
5.23E-01
5.27E-01
5.30E-01
5.33E-01
5.35E-01
5.37E-01
5.40E-01
5.41E-01
5.43E-01
5.44E-01
5.46E-01
5.46E-01
5.47E-01
5.47E-01
5.47E-01
5.46E-01
5.46E-01
5.44E-01
5.43E-01
5.40E-01
-------
7.45E+03
9.106+03
1.12E+04
1.37E+04
1.69E+04
2.08E+04
1.29E-06
9.26E-07
6.62E-07
4.73E-07
3.38E-07
2.42E-07
1.29E-06
9.26E-07
6.62E-07
4.73E-07
3.386-07
2.42E-07
9.90E-01
9.906-01
9.90E-01
9.90E-01
9.90E-01
9.90E-01
1.01E-02
1.01E-02
1.01E-02
1.01E-02
1.01E-02
1.01E-02
1.01E-02
1.01E-02
1.01E-02
1.01E-02
1.01E-02
1.01E-02
O.OOE+00
O.OOE+00
-1.03E-04
-3.39E-04
-1.53E-04
O.OOE+00
9.85E-04
8.52E-04
O.OOE+00
O.OOE+00
O.OOE+00
4. 176-04
3.61E-05
3.16E-05
0.006*00
O.OOE+00
O.OOE+00
2.39E-05
7.23E-02
6.77E-02
6.28E-02
5.76E-02
5.23E-02
4.67E-02
8.13E-02
7.73E-02
7.30E-02
6.85E-02
6.40E-02
5.94E-02
5.386-01
5.066-01
5.00E-01
4.926-01
4.84E-01
4.75E-01
1
time averaged (tav * 1800. s) volume concentration: concentration contour parameters
c(x.y,z,t> « cc(x) * (erf(xa)-erf(xb)) * (erf
xb (x-xc-bx)/(sr2*betax)
ya /
yb
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
sig(x)
O.OOE+00
1.01E+00
1.37E+00
1.65E+00
1.90E+00
2.12E+00
2.32E+00
2.52E+00
2.70E+00
2.87E+00
3.03E+00
3.05E+00
3.07E+00
3.10E+00
3.13E+00
3.16E+00
3.21E+00
3.26E+00
3.33E+00
3.41E+00
3.50E+00
3.61E+00
3.7SE+00
3.91E+00
4.09E+00
4.32E+00
4.58E+00
4.88E+00
5.24E+00
5.66E+00
6.14E+00
6.70E+00
7.35E+00
8.09E+00
8.96E+00
9.95E+00
1.11E+01
1.24E+01
1.40E+01
1.57E+01
1.78E+01
2.01E+01
2.28E+01
2.60E+01
2.96E+01
3.38E+01
t
4.08E+00
4.82E+00
5.57E+00
6.41E+00
7.25E+00
8.18E+00
9.12E+00
1.01E+01
1.12E+01
1.23E+01
1.34E+01
1.36E+01
1.40E+01
1.43E+01
1.48E+01
1.53E+01
1.60E+01
1.68E+01
1.78E+01
1.89E+01
2.03E+01
2.20E+01
2.41E+01
2.6SE+01
2.94E+01
3.29E+01
3.70E+01
4.19E+01
4.78E+01
5.46E+01
6.28E+01
7.24E+01
8.38E+01
9.72E+01
1.13E+02
1.32E+02
1.53E+02
1.79E+02
2.10E+02
2.45E+02
2.88E+02
3.37E+02
3.96E+02
4.65E+02
5.47E+02
6.43E+02
xc(t)
O.OOE+00
1.02E+00
2.04E+00
3.07E+00
4.09E+00
5.11E+00
6.13E+00
7.16E+00
8. 186+00
9.20E+00
.02E+01
.04E+01
.07E+01
.10E+01
.15E+01
.196+01
.2SE+01
1.33E+01
1.42E+01
1.S3E+01
1 .666+01
1.82E+01
2.02E+01
2.25E+01
2.55E+01
2.906+01
3.33E+01
3.86E+01
4.50E+01
S.29E+01
6.24E+01
7.40E+01
8.82E+01
1.0SE+02
1.27E+02
1.52E+02
1.83E+02
2.21E+02
2.68E+02
3.24E+02
3.93E+02
4.77E+02
5.79E+02
7.04E+02
8.56E+02
1.04E+03
bx(t)
1.02E+01
1.13E+01
1.24E+01
1.35E+01
1.4SE+01
1.56E+01
1.67E+01
1.78E+01
1.89E+01
2.00E+01
2.10E+01
2.13E+01
2.166+01
2.19E+01
2.23E+01
2.29E+01
2.3SE+01
2.43E+01
2.52E+01
2.64E+01
2.78E+01
2.95E+01
3.15E+01
3.41E+01
3. 71 E+01
4.09E+01
4.55E+01
5.11E+01
5.79E+01
6.61E+01
7.62E+01
8.85E+01
1.04E+02
1.22E+02
1.44E+02
1.71E+02
2.04E+02
2.44E+02
2.93E+02
3.53E+02
4.26E+02
5.15E+02
6.23E+02
7.55E+02
9.15E+02
1.11E+03
betax(t)
8.35E-02
9.23E-02
1.01E-01
1.10E-01
1.19E-01
1.28E-01
1.36E-01
1.4SE-01
1.546-01
1.63E-01
1.72E-01
1.74E-01
1.76E-01
1.79E-01
1.82E-01
1.87E-01
1.92E-01
1.98E-01
2.06E-01
2.15E-01
2.27E-01
2.41E-01
2.58E-01
2.786-01
3.03E-01
3.34E-01
3.71E-01
4.17E-01
4.72E-01
5.406-01
6.22E-01
7.23E-01
8.45E-01
9.95E-01
1.18E+00
1.40E+00
1 .67E+00
2.00E+00
2.40E+00
2.886+00
3.486+00
4.206+00
5.096+00
6.16E+00
7.476+00
9.076+00
-------
1.27E+03
1.54E+03
1.88E+03
2.28E+03
2.78E+03
3.396+03
4.12E+03
5.02E+03
6.12E+03
7.45E+03
9.10E+03
1.12E+04
1 .376+04
1.69E+04
2.08E+04
6.23E-05
5.386-05
4.63E-05
3.98E-05
3.41E-05
2.92E-OS
2.50E-05
2.UE-05
1.83E-05
1.57E-05
1.3SE-05
1.16E-05
1.01E-05 1
8.75E-06 1
7.66E-06 1
.01E+01
.016+01
.01E+01
.01E+01
.02E+01
.02E+01
.026+01
.02E+01
.026+01
.02E+01
.02E+01
.02E+01
.026+01
.02E+01
.02E+01
1.07E+02
1.28E+02
1.51E+02
1.79E+02
2.11E+02
2.486+02
2.916+02
3.406+02
3.96E+02
4.596+02
5.32E+02
6. 166+02
7.13E+02
8.22E+02
9.46E+02
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
3.87E+01
4.436+01
5.07E+01
5.82E+01
6.67E+01
7.66E+01
8.79E+01
1.016+02
1.166+02
1.33E+02
1.556+02
1.80E+02
2.09E+02
2.41E+02
2.76E+02
7.586+02
8.936+02
1.05E+03
1.24E+03
1.47E+03
1.73E+03
2.05E+03
2.43E+03
2.876+03
3.416+03
3.446+03
3.836+03
4.316+03
4.896+03
5.606+03
1.276+03
1.54E+03
1.88E+03
2.286+03
2.78E+03
3.39E+03
4.12E+03
5.026+03
6.12E+03
7.456+03
9.10E+03
1.12E+04
1.37E+04
1.696+04
2.086+04
1.35E+03
1.646+03
1.99E+03
2.426+03
2.956+03
3.596+03
4. 376+03
5.32E+03
6.48E+03
7.89E+03
7.89E+03
7.89E+03
7.89E+03
7.89E+03
7.896+03
1.10E+01
1.34E+01
1 .63E+01
1.98E+01
2.41E+01
2.93E+01
3.57E+01
4.35E+01
5.29E+01
6.UE+01
1 ..24E+03
1 .85E+03
2.41E+03
2.97E+03
3.55E+03
time averaged (tav = 1800. s) volume concentration: concentration in the z * .00 plane.
downwind
distance
x (m)
-1.02E+01
-8.18E+00
-6.13E+00
-4.09E+00
-2.04E+00
-1.55E-06
2.04E+00
4.09E+00
6.13E+00
8.18E+00
1.02E+01
1.04E+01
1.07E+01
1.10E+01
1.15E+01
1.19E+01
1.25E+01
1 .33E+01
1.42E+01
1 .53E+01
1 .66E+01
1.82E+01
2.02E+01
2.25E+01
2.55E+01
2.90E+01
3.33E+01
3.86E+01
4.50E+01
5.29E+01
6.24E+01
7.40E+01
8.82E+01
1.05E+02
1.27E+02
1.52E+02
1 .83E+02
2.21E+02
2.68E+02
3.24E+02
3.93E+02
4.77E+02
5.79E+02
7.04E+02
8.56E+02
1.04E+03
1 .27E+03
1.54E+03
1 .88E+03
2.28E+03
2.78E+03
3.39E+03
time of
max cone
(s)
1 .566+03
1.56E+03
1.56E+03
1.56E+03
1 .56E+03
1.56E+03
1.56E+03
1.56E+03
1.56E+03
1.56E+03
1 .56E+03
1.56E+03
1.56E+03
1 .56E+03
1.56E+03
1.56E+03
1.56E+03
1.56E+03
1 .56E+03
1 .566+03
1.56E+03
1 .56E+03
1.56E+03
1.56E+03
1 .57E+03
1.57E+03
1.57E+03
1.57E+03
1 .57E+03
1 .57E+03
1.57E+03
1.58E+03
1.58E+03
1.58E+03
1.59E+03
1.59E+03
1.60E+03
1 .61E+03
1.62E+03
1.63E+03
1.64E+03
1.66E+03
1.68E+03
1.71E+03
1.74E+03
1.78E+03
1 .83E+03
1.88E+03
1. 956+03
2.04E+03
2.14E+03
2.27E+03
cloud
duration
(s)
3.12E+03
3.12E+03
3.12E+03
3.12E+03
3.12E+03
3.12E+03
3.12E+03
3.12E+03
3.12E+03
3.12E+03
3.126+03
3.12E+03
3.12E+03
3.12E+03
3.12E+03
3.12E+03
3.12E+03
3.12E+03
3.12E+03
3.12E+03
3.12E+03
3.12E+03
3.12E+03
3.126+03
3.12E+03
3.12E+03
3.12E+03
3.12E+03
3.12E+03
3.12E+03
3.12E+03
3.12E+03
3.12E+03
3.12E+03
3.12E+03
3.126+03
3.12E+03
3.126+03
3.126+03
3.12E+03
3.12E+03
3.126+03
3.12E+03
3.12E+03
3.12E+03
3.12E+03
3.12E+03
3.12E+03
3.12E+03
3.126+03
3.12E+03
3.12E+03
effective
half width
bbc (m)
1 .02E+01
1.04E+01
1.05E+01
1.06E+01
1.08E+01
1.09E+01
1.116+01
1.126+01
1.146+01
1.166+01
1.186+01
1.186+01
1.18E+01
1.19E+01
1.19E+01
1.20E+01
1.20E+01
1.21E+01
1.22E+01
1.23E+01
1.24E+01
1.266+01
1.28E+01
1 .30E+01
1 .34E+01
1 .386+01
1.43E+01
1 .49E+01
1.57E+01
1.67E+01
1 .80E+01
1.95E+01
2.15E+01
2.40E+01
2.706+01
3.086+01
3.546+01
4.10E+01
4.796+01
5.636+01
6.64E+01
7.866+01
9.32E+01
1.11E+02
1 .32E+02
1.57E+02
1 .86E+02
2.21E+02
2.62E+02
3.10E+02
3.65E+02
4.30E+02
average concentration (volume fraction) at (x,y,z)
y/bbc=
0.0
O.OOE+00
3.72E-03
4.40E-03
4.83E-03
5.16E-03
5.41E-03
5.62E-03
5.796-03
5.93E-03
6.05E-03
6.15E-03
6.106-03
6.03E-03
5.95E-03
5.85E-03
5.74E-03,
5.61E-03
5.456-03
5.286-03
5.08E-03
4.85E-03
4.606-03
4.32E-03
4.01E-03
3.69E-03
3.35E-03
3.00E-03
2.64E-03
2.29E-03
1.95E-03
1.63E-03
1.33E-03
1.07E-03
8.48E-04
6.58E-04
5.03E-04
3.79E-04
2.83E-04
2.08E-04
1.52E-04
1.11E-04
7.98E-05
5.736-05
4.11E-05
2.94E-05
2.10E-05
1.50E-05
1.07E-05
7.66E-06
5.50E-06
3.96E-06
2.85E-06
y/bbc«
0.5
O.OOE+00
3.45E-03
4.02E-03
4.356-03
4.566-03
4.716-03
4.816-03
4.886-03
4.93E-03
4.956-03
4.976-03
4.916-03
4.856-03
4.786-03
4.69E-03
4.58E-03
4.46E-03
4.32E-03
4.16E-03
3.98E-Q3
3.77E-03
3.55E-03
3.30E-03
3.046-03
2.766-03
2.48E-03
2.19E-03
1.91E-03
1.63E-03
1. 386-03
1.14E-03
9.30E-04
7.44E-04
5.86E-04
4.54E-04
3.46E-04
2.61E-04
1.94E-04
1.436-04
1.056-04
7.606-05
5.486-05
3.946-05
2.826-05
2.026-05
1.446-05
1.03E-05
7.366-06
5.27E-06
3.78E-06
2.72E-06
1.966-06
y/bbc*
1.0
O.OOE+00
1.256-03
1.456-03
.566-03
.626-03
.676-03
.706-03
.726-03
.736-03
.736-03
.736-03
.716-03
.696-03
.666-03
.636-03
1.59E-03
1.55E-03
1.50E-03
1 .44E-03
1. 376-03
1.30E-03
1.22E-03
1.13E-03
1.04E-03
9.406-04
8.40E-04
7.39E-04
6.40E-04
5.46E-04
4.58E-04
3.77E-04
3.06E-04
2.44E-04
1.91E-04
1.48E-04
1.136-04
8.496-05
6.316-05
4.656-05
3.406-05
2.476-05
1.786-05
1.286-05
9.17E-06
6.55E-06
4.686-06
3.346-06
2.39E-06
1.71E-06
1.236-06
8.82E-07
6.376-07
y/bbc-
1.5
O.OOE+00
4.00E-05
5.48E-05
6.84E-05
8.14E-05
9.39E-05
1.066-04
1.17E-04
1.27E-04
1.37E-04
1.46E-04
1.45E-04
1.44E-04
1.436-04
1.426-04
1.416-04
1.396-04
1.376-04
1.356-04
1.326-04
1.286-04
1.246-04
1.196-04
1.146-04
1.076-04
9.986-05
9.166-05
8.276-05
7.326-05
6.356-05
5.38E-05
4.466-05
3.626-05
2.876-05
2.24E-05
1.72E-05
1.306-05
9.666-06
7.136-06
5.216-06
3.786-06
2.736-06
1.966-06
1.41E-06
1.01E-06
7.18E-07
5.13E-07
3.66E-07
2.626-07
1.886-07
1.35E-07
9.77E-08
y/bbcs
2.0
O.OOE+00
5.53E-08
1.16E-07
2.11E-07
3.49E-07
5.37E-07
7.78E-07
1.07E-06
1.42E-06
1.82E-06
2.26E-06
2.28E-06
2.31E-06
2.35E-06
2.39E-06
2.45E-06
2.51E-06
2.59E-06
2.67E-06
2.78E-06
2.89E-06
3.03E-06
3.17E-06
3.316-06
3.45E-06
3.566-06
3.636-06
3.63E-06
3.55E-06
3.36E-06
3.09E-06
2.73E-06
2.33E-06
1.93E-06
1.55E-06
1.21E-06
9.22E-07
6.93E-07
5.13E-07
3.76E-07
2.74E-07
1. 986-07
1.42E-07
1.02E-07
7.28E-08
5.20E-08
3.71E-08
2.65E-08
1.90E-08
1.36E-08
9.80E-09
7.08E-09
y/bbc=
2.5
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
1.54E-10
3.25E-10
5.07E-10
1.22E-09
2.16E-09
3.51E-09
5.67E-09
6.00E-09
6.12E-09
6.59E-09
7.04E-09
7.45E-09
8. 16E-09
8.98E-09
1.02E-OB
1.16E-08
1 .36E-08
1.60E-08
1.94E-08
2.36E-08
2.89E-08
3.54E-08
4.30E-08
5.10E-08
5.87E-08
6.48E-08
6.80E-08
6.76E-08
6.35E-08
5.64E-08
4.77E-08
3.87E-08
3.04E-08
2.32E-08
1 .736-08
1 .286-06
9.33E-09
6.74E-09
4.85E-09
3.49E-09
2.49E-09
1.78E-09
1.27E-09
9.12E-10
6.51E-10
4.68E-10
3.35E-10
2.42E-10
-------
4.12E+03
5.02E+03
6.12E+03
7.45E+03
9.10E+03
1.12E+04
1.37E+04
1.69E+04
2.08E+04
2.42E+03
2.61E+03
2.84E+03
3.12E+03
3.44E+03
3.83E+03
4.31E+03
4.89E+03
5.60E+03
3.12E+03
3.12E+03
3.12E+03
3.12E+03
3.15E+03
3.21E+03
3.29E+03
3.41E+Q3
3.56E+03
5.04E+02
5.89E+02
6.86E+02
7.96E+02
9.22E+02
1.07E+03
1.23E+03
1.42E+03
1.64E+03
2.07E-06
1.51E-06
1.10E-06
8.10E-07
5.98E-07
4.40E-07
3.23E-07
2.36E-07
1.73E-07
1.42E-06
1.03E-06
7.57E-07
5.57E-07
4.11E-07
3.03E-07
2.22E-07
1.62E-07
1.19E-07
4.62E-07
3.36E-07
2.46E-07
1.81E-07
1.33E-07
9.83E-08
7.21E-08
5.27E-08
3.86E-08
7.08E-08
5.15E-08
3.77E-08
2.77E-08
2.05E-08
1.51E-08
1.11E-08
8.09E-09
5.92E-09
5.13E-09
3.73E-09
2.73E-09
2.01E-09
1.48E-09
1.09E-09
8.00E-10
5.86E-10
4.29E-10
1.77E-10
1.29€-10
9.25E-11
6.80E-11
5.00E-11
3.67E-11
2.77E-11
1.98E-11
1.43E-11
1
time averaged (tav « 1800. s) volune concentration: mximum concentration (volune fraction) along centerline.
downwind
distance
x (m>
-1.02E*01
-8.18E+00
-6.13E+00
-4.096+00
-2.04E+00
-1.55E-06
2.04E+00
4.09E+00
6.13E+00
8.18E+00
1.02E+01
1.04E+01
1.07E+01
1.10E+01
1.15E+01
1.19E+01
1 .25E+01
1.33E*01
1.42E+01
1 .53E+01
1.66E+01
1 .82E+01
2.02E+01
2.25E+01
2.55E+01
2.90E+01
3.33E+01
3.86E+01
4.50E+01
5.29E*01
6.24E+01
7.40E+01
8.82E+01
1.05E+02
1.27E+02
1.52E+02
1.83E+02
2.21E+02
2.68E+02
3.24E+02
3.93E+02
4.77E+02
5.79E+02
7.WE+02
8.56E+02
1 .04E+03
1 .27E+03
1 .54E+03
1.88E+03
2.28E+03
2.78E+03
3.39E+03
4.12E+03
5.02E+03
6.12E+03
7.45E+03
9.10E+03
1.12E+04
height
z (m)
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
mximjn
concentration
c(x,0,z)
O.OOE+00
3.72E-03
4.40E-03
4.83E-03
5.16E-03
5.41E-03
5.62E-03
5.79E-03
5.93E-03
6.05E-03
6.1SE-03
6.10E-03
6.03E-03
S.9SE-03
5.85E-03
5.74E-03
5.61E-03
5.45E-03
5.28E-03
5.08E-03
4.85E-03
4.60E-03
4.32E-03
4.01E-03
3.69E-03
3.3SE-03
3.00E-03
2.64E-03
2.29E-03
1.95E-03
1.63E-03
1.33E-03
1.07E-03
8.48E-04
6.58E-04
5.03E-04
3.79E-04
2.83E-04
2.08E-04
1.52E-04
1.11E-04
7.98E-05
5.73E-05
4.11E-05
2.94E-05
2.10E-05
1.50E-05
1.07E-05
7.66E-06
5.SOE-06
3.96E-06
2.85E-06
2.07E-06
1.51E-06
1.10E-06
8.10E-07
5.98E-07
4.40E-07
time of
max cone
(s)
1.56E+03
1.56E+03
1.56E+03
1.56E+03
1.56E+03
1.56E+03
1.56E+03
1.56E+03
1.56E+03
1.56E+03
1.56E+03
1.56E+03
1.S6E+03
1.56E+03
1.56E+03
1.56E+03
1.56E+03
1.S6E+03
1.56E+03
1.56E+03
1.56E+03
1.56E+03
1.56E+03
1.56E+03
1.57E+03
1.57E+03
1.57E+03
1.57E+03
1.57E+03
1.57E+03
1.57E+03
1.S8E+03
1.58E+03
1.58E+03
1.59E+03
1.59E+03
1.60E+03
1 .616+03
1.62E+03
1.63E+03
1.64E+03
1.66E+03
1.68E+03
1.71E+03
1.74E+03
1.78E+03
1.83E+03
1.88E+03
1.95E+03
2.04E+03
2.14E+03
2.27E+03
2.42E+03
2.61E+03
2.84E+03
3.12E+03
3.44E+03
3.83E+03
cloud
duration
(s)
3.12E+03
3.12E+03
3.12E+03
3.12E+03
3.12E+03
3.12E+03
3.12E+03
3.12E+03
3.12E+03
3.12E+03
3.12E+03
3.12E+03
3.12E+03
3.12E+03
3.12E+03
3.12E+03
3.12E+03
3.12E+03
3.12E+03
3.12E+03
3.12E+03
3.12E+03
3.12E+03
3.12E+03
3.12E+03
3.12E+03
3.12E+03
3.12E+03
3.12E+03
3.12E+03
3.12E+03
3.12E+03
3.12E+03
3.12E+03
3.12E+03
3.12E+03
3.12E+03
3.12E+03
3.12E+03
3.12E+03
3.12E+03
3.12E+03
3.12E+03
3.12E+03
3.12E+03
3.12E+03
3.12E+03
3.12E+03
3.12E+03
3.12E+03
3.12E+03
3.12E+03
3.12E+03
3.12E+03
3.12E+03
3.12E+03
3.15E+03
3.21E+03
-------
1.37E+04 O.OOE+00 3.23E-07 4.31E+03 3.29E+03
1.69E+04 O.OOE+00 2.36E-07 4.89E*03 3.41E+03
2.08E+04 O.OOE+00 1.73E-07 5.60E+03 3.56E+03
-------
RUN13.0UT
problem input
idspl *
ncale «
urns -
cps *
tbp =
cmedO *
dhe «
cpsl *
rhosl «
spb =
spc «
ts =
qs «
as *
tsd =
qtis =
hs -
tav »
xffro *
zp<1> *•
zp(2) =
zp(3) -
zp(«) =
zO =
za =
ua «
ta =
rh =
stab =
1
1
.031880
909.80
309.35
.00
1070000.
2716.00
793.70
-1.00
.00
293.00
.09
37.85
680.
.00
.00
1800.00
5000.00
.00
.00
.00
.00
.300000
10.00
3.20
293.00
68.00
4.00
release gas properties
molecular weight of source gas (kg)
vapor heat capacity, const, p. (j/kg-k)
temperature of source gas (k)
density of source gas (kg/m3)
boiling point temperature
liquid mass fraction
liquid heat capacity (j/kg-k)
heat of vaporization (j/kg)
liquid source density (kg/m3)
saturation pressure constant
saturation pressure constant (k)
saturation pressure constant (k)
spill characteristics
spill type
mass source rate (kg/s)
continuous source duration (s)
continuous source mass (kg)
instantaneous source mass (kg)
source area (m2)
vertical vapor velocity (n/s)
source half width (m)
source height (m)
horizontal vapor velocity (m/s)
field parameters
concentration averaging time *
zp(3)-
zp(4)=
3.1880E-02
9.0980E+02
3.093SE+02
1.2559E+00
3.0935E+02
O.OOOOE+00
2.7160E+03
1.0700E+06
7.9370E+02
1.3263E+01
4.1028E+03
O.OOOOE+00
1
9.4000E-02
6.8000E+02
6.3920E+01
O.OOOOE+00
3.7854E+01
1.9772E-03
3.0763E+00
O.OOOOE+00
O.OOOOE+00
1.8000E+03
1.0400E+03
5.0000E+03
O.OOOOE+00
O.OOOOE+00
O.OOOOE+00
O.OOOOE+00
-------
ant lent meteorological properties
molecular weight of ambient air (kg)
heat capacity of ambient air at const p. (j/kg-k>-
density of ambient air (kg/m3)
ambient measurement height (m)
ambient atmospheric pressure (pa=n/m2=j/in3)
ambient wind speed (n/s)
ambient temperature (k)
relative humidity (percent)
ambient friction velocity
von karman constant
1 '
- ncalc
- nssm
• grav
- rr
- xk
1
3
9.8067E+00
8.3143E+00
4.1000E-01
instantaneous spatially averaged cloud parameters
X
-3.08E+00
•2.46E+00
•1.85E+00
-1.23E+00
-6.15E-01
3.87E-07
6.15E-01
1.23E+00
1 .856+00
2.46E+00
3.08E+00
3.14E+00
3.22E+00
3.32E+00
3.44E+00
3.58E+00
3.75E+00
3.96E+00
4.22E+00
4.53E+00
4.91E+00
5.37E+00
5.92E+00
6.60E+00
7.41E+00
8.41E+00
9.62E+00
1.11E+01
1 .29E+01
1.50E+01
1.76E+01
2.08E+01
2.47E+01
2.94E+01
3.51E+01
4.20E+01
5.04E+01
6.06E+01
7.29E+01
8.79E+01
1.06E+02
1.28E+02
1.55E+02
1.8BE+02
zc
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
h
O.OOE+00
1.11E+00
1.44E+00
1.70E+00
1.91E+00
2.10E+00
2.28E+00
2.44E+00
2.60E+00
2.74E+00
2.88E+00
2.90E+00
2.91E+00
2.93E+00
2.96E+00
2.99E+00
3.03E+00
3.07E+00
3.12E+00
3. 186+00
3.26E+00
3.35E+00
3.4SE+00
3.58E+00
3.72E+00
3.89E+00
4.09E+00
4.33E+00
4.60E+00
4.91E+00
5.27E+00
S.69E+00
6.16E+00
6.71E+00
7.34E+00
8.06E+00
8.89E+00
9.83E+00
.09E+01
.21E+01
.36E+01
.52E+01
.70E+01
.92E+01
bb
3.08E+00
3.13E+00
3.16E+00
3.20E+00
3.23E+00
3.27E+00
3.30E+00
3.34E+00
3.37E+00
3.41E+00
3.44E+00
3.45E+00
3.45E+00
3.46E+00
3.46E+00
3.47E+00
3.48E+00
3.49E+00
3.51E+00
3.53E+00
3.55E+00
3.58E+00
3.61E+00
3.65E+00
3.70E+00
3.75E+00
3.82E+00
3.91E+00
4.01E+00
4.14E+00
4.29E+00
4.48E+00
4.70E+00
4.986+00
5.31E+00
5.71E+00
6.19E+00
6.77E+00
7.48E+00
8.33E+00
9.35E+00
1.06E+01
1.21E+01
1 .39E+01
b
2.77E+00
2.77E+00
2.77E+00
2.77E+00
2.77E+00
2.77E+00
2.77E+00
2.77E+00
2.77E+00
2.77E+00
2.77E+00
2.77E+00
2.77E+00
2.77E+00
2.77E+00
2.77E+00
2.77E+00
2.77E+00
2.78E+00
2.78E+00
2.78E+00
2.78E+00
2.78E+00
2.78E+00
2.78E+00
2.78E+00
2.79E+00
2.79E+00
2.79E+00
2.80E+00
2.BOE+00
2.81E+00
2.81E+00
2.82E+00
2.83E+00
2.84E+00
2.85E+00
2.866+00
2.87E+00
2.88E+00
2.89E+00
2.90E+00
2.90E+00
2.91E+00
bbx
3.08E+00
3.40E+00
3.73E+00
4.05E+00
4.38E+00
4.71E+00
5.03E+00
5.36E+00
5.69E+00
6.01E+00
6.34E+00
6.41E+00
6.49E+00
6.59E+00
6.72E+00
6.87E+00
7.06E+00
7.286+00
7.55E+00
7.88E+00
8.28E+00
8.76E+00
9.35E+00
1.01E+01
1.09E+01
1.20E+01
1.33E+01
1.48E+01
1.67B+01
1.90E+01
2.18E+01
2.51E+01
2.92E+01
3.42E+01
4.02E+01
4.76E+01
5.65E+01
6.73E+01
8.04E+01
9.63E+01
1.16E+02
1.39E+02
1.686+02
2.02E+02
bx
3.08E+00
3.40E+00
3.73E+00
4.05E+00
4.38E+00
4.71E+00
5.03E+00
5.36E+00
5.68E+00
6.01E+00
6.34E+00
6.41E+00
6.49E+00
6.S9E+00
6.72E+00
6.87E+00
7.05E+00
7.28E+00
7.5SE+00
7.88E+00
8.28E+00
8.76E+00
9.35E+00
1.01E+01
1.09E+01
1.20E+01
1.33E+01
1.48E+01
1.67E+01
1.90E+01
2.18E+01
2.51E+01
2.92E+01
3.42E+01
4.02E+01
4.766+01
5.65E+01
6.73E+01
8.04E+01
9.63E+01
1.16E+02
1.39E+02
1.68E+02
2.02E+02
cv
O.OOE+00
1.66E-03
2.00E-03
2.21E-03
2.36E-03
2.47E-03
2.566-03
2.64E-03
2.70E-03
2.75E-03
2.79E-03
2.77E-03
2.74E-03
2.70E-03
2.66E-03
2.61E-03
2.55E-03
2.49E-03
2.41E-03
2.32E-03
2.22E-03
2.12E-03
2.00E-03
.87E-03
.74E-03
.59E-03
.45E-03
.30E-03
.16E-03
.02E-03
8.83E-04
7.57E-04
6.41E-04
5.366-04
4.42E-04
3.606-04
2.906-04
2.30E-04
1.816-04
1.40E-04
1.08E-04
8.19E-05
6.166-05
4.606-05
rho
1.20E+00
1.20E+00
1.20E+00
.20E+00
.20E+00
.206+00
.206+00
.20E+00
.20E+00
.206+00
.206+00
1.20E+00
1.20E+00
1.20E+00
1.206+00
1.206+00
1.20E+00
1.20E+00
1.20E+00
1.20E+00
1.20E+00
1.20E+00
1.206+00
1.206+00
1.20E+00
1.20E+00
1 .206+00
1 .206+00
1.20E+00
1.20E+00
1.20E+00
1.20E+00
1.20E+00
1 .206+00
1.20E+00
1.206+00
1.20E+00
1.20E+00
1.20E+00
1.20E+00
1.20E+00
1.20E+00
1.20E+00
1.206+00
t
2.93E+02
2.93E+02
2.93E+02
2.93E+02
2.93E+02
2.93E+02
2.93E+02
2.93E+02
2.936+02
2.93E+02
2.93E+02
2.93E+02
2.93E+02
2.93E+02
2.93E+02
2.93E+02
2.93E+02
2.93E+02
2.93E+02
2.93E+02
2.93E+02
2.93E+02
2.93E+02
2.93E+02
2.93E+02
2.93E+02
2.93E+02
2.93E+02
2.93E+02
2.93E+02
2.93E+02
2.93E+02
2.93E+02
2.93E+02
2.93E+02
2.93E+02
2.93E+02
2.93E+02
2. 936+02
2.93E+02
2.93E+02
2.93E+02
2.93E+02
2.93E+02
u
O.OOE+00
6.16E-01
7.78E-01
8.886-01
9.72E-01
1.046+00
1.106+00
1.15E+00
1.20E+00
1.24E+00
1.286+00
1 .286+00
1.29E+00
1.29E+00
1 .306+00
1.31E+00
1.32E+00
1 .33E+00
1.34E+00
1.36E+00
1.386+00
1 .406+00
1.426+00
.456+00
.49E+00
.526+00
.56E+00
.616+00
1.666+00
1.71E+00
1.77E+00
1 .846+00
1.916+00
1.98E+00
2.06E+00
2.14E+00
2.22E+00
2.31E+00
2.40E+00
2.50E+00
2.59E+00
2.69E+00
2.80E+00
2.906+00
ua
O.OOE+00
6.18E-01
7.80E-01
8.90E-01
9.74E-01
1.04E+00
1.106+00
1.166+00
1 .206+00
1.24E+00
1 .28E+00
1.29E+00
1.29E+00
1.30E+00
1.30E+00
1.31E+00
1.32E+00
1 .336+00
1.35E+00
1 .366+00
1.38E+00
1 .406+00
1.43E+00
1.46E+00
1.49E+00
1.S2E+00
1 .57E+00
1.616+00
1.66E+00
1.72E+00
1.78E+00
1.84E+00
1.91E+00
1.98E+00
2.06E+00
2.146+00
2.22E+00
2.31E+00
2.406+00
2.506+00
2.596+00
2.69E+00
2.806+00
2.906+00
-------
2.27E+02
2.75E+02
3.34E+02
4.05E+02
4.90E+02
5.95E+02
7.22E+02
8.7SE+02
1.06E+03
1.29E+03
1.57E+03
1.92E+03
2.36E+03
2.91E+03
3.61E+03
4.47E+03
5.54E+03
1
X
-3.08E+00
-2.46E+00
-1.85E+00
-1.23E+00
-6.15E-01
3.87E-07
6.15E-01
1.23E+00
1 .85E+00
2.46E+00
3.08E+00
3.14E+00
3.22E+00
3.32E+00
3.44E+00
3.58E+00
3.75E+00
3.96E+00
4.22E+00
4.53E+00
4.91E+00
5.37E+00
5..92E+00
6.60E+00
7.41E+00
8.41E+00
9.62E+00
1.11E+01
1.29E+01
1.50E+01
1.76E+01
2.08E+01
2.47E+01
2.94E+01
3.51E+01
4.20E+01
5.04E+01
6.06E+01
7.29E+01
8.79E+01
1.06E+02
1.28E+02
1.55E+02
1.88E+02
2.27E+02
2.75E+02
3.34E+02
4.05E+02
4.90E+02
5.95E+02
7.22E+02
8.75E+02
1 .06E+03
. 1.29E+03
1.57E+03
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
cm
O.OOE+00
1.84E-03
2.21E-03
2.45E-03
2.61E-03
2.74E-03
2.84E-03
2.92E-03
2.99E-03
3.04E-03
3.09E-03
3.06E-03
3.03E-03
2.99E-03
2.94E-03
2.89E-03
2.83E-03
2.75E-03
2.67E-03
2.57E-03
2.46E-03
2.34E-03
2.21E-03
2.07E-03
1.92E-03
.77E-03
.60E-03
.44E-03
.28E-03
.13E-03
9.78E-04
8.38E-04
7.10E-04
5.93E-04
4.90E-04
3.99E-04
3.21E-04
2.55E-04
2.00E-04
1.S6E-04
1.19E-04
9.07E-05
6.82E-05
5.09E-05
3.77E-05
2.77E-05
2.03E-05
1.48E-05
1.07E-05
7.73E-06
5.58E-06
4.02E-06
2.89E-06
2.08E-06
1.43E-06
2.16E+01
2.44E+01
2.77E+01
3.14E+01
3.56E+01
4.05E+01
4.61E+01
5.25E+01
6.00E+01
6.85E+01
8.05E+01
9.45E+01
1.11E+02
1.30E+02
1.52E+02
1.77E+02
2.07E+02
cmv
O.OOE+00
1.84E-03
2.21E-03
2.45E-03
2.61E-03
2.74E-03
2.84E-03
2.92E-03
2.99E-03
3.04E-03
3.09E-03
3.06E-03
3.03E-03
2.99E-03
2.94E-03
2.89E-03
2.83E-03
2.75E-03
2.67E-03
2.57E-03
2.46E-03
2.34E-03
2.21E-03
2.07E-03
1.92E-03
1.77E-03
1.60E-03
1.44E-03
1.28E-03
1.13E-03
9.78E-04
8.38E-04
7.10E-04
5.93E-04
4.90E-04
3.99E-04
3.21E-04
2.55E-04
2.00E-04
1.56E-04
1.19E-04
9.07E-05
6.82E-05
5.09E-05
3.77E-05
2.77E-05
2.03E-05
1 .48E-05
1.07E-05
7.73E-06
5.58E-06
4.02E-06
2.89E-06
2.08E-06
1.43E-06
1 .60E+01
1.86E+01
2.17E+01
2.54E+01
2.99E+01
3.52E+01
4.15E+01
4.90E+01
5.79E+01
6.84E+01
8.09E+01
9.60E+01
1.14E+02
1.36E+02
1.61E+02
1.91E+02
2.26E+02
crate
9.90E-01
9.88E-01
9.88E-01
9.87E-01
9.87E-01
9.87E-01
9.B7E-01
9.87E-01
9.87E-01
9.87E-01
9.87E-01
9.87E-01
9.87E-01
9.87E-01
9.87E-01
9.87E-01
9.87E-01
9.87E-01
9.87E-01
9.87E-01
9.87E-01
9.88E-01
9.88E-01
9.88E-01
9.88E-01
9.88E-01
9.88E-01
9.88E-01
9.89E-01
9.89E-01
9.89E-01
9.89E-01
9.89E-01
9.89E-01
9.89E-01
9.89E-01
9.90E-01
9.90E-01
9.90E-01
9.90E-01
9.90E-01
9.90E-01
9.90E-01
9.90E-01
9.90E-01
9.90E-01
9.90E-01
9.90E-01
9.90E-01
9.90E-01
9.90E-01
9.90E-01
9.90E-01
9.90E-01
9.90E-01
2.92E+00
2.93E+00
2.93E+00
2.94E+00
2.94E+00
2.94E+00
2.9SE+00
2.95E+00
2.95E+00
2.95E+00
2.95E+00
2.95E+00
2.95E+00
2.95E+00
2.95E+00
2.95E+00
2.95E+00
emu
1.01E-02
1.01E-02
1.01E-02
1.01E-02
1.01E-02
1.01E-02
1.01E-02
1.01E-02
1.01E-02
1.01E-02
1.01E-02
1.01E-02
1.01E-02
1.01E-02
1.01E-02
1.01E-02
1.01E-02
1.01E-02
1.01E-02
1.01E-02
1.01E-02
1.01E-02
1.01E-02
1.01E-02
1.01E-02
1.01E-02
1.01E-02
1.01E-02
1.01E-02
1.01E-02
1.01E-02
1.01E-02
1.01E-02
1.01E-02
1.01E-02
1.01E-02
1.01E-02
1.01E-02
1.01E-02
1.01E-02
1.01E-02
1.01E-02
1.01E-02
1.01E-02
1.01E-02
1.01E-02
1.01E-02
1.01E-02
1.01E-02
1.01E-02
1.01E-02
1.01E-02
1.01E-02
1.01E-02
1.01E-02
2.44E+02
2.9SE+02
3.57E+02
4.32E+02
5.23E+02
6.34E+02
7.68E+02
9.31E+02
1.13E+03
1.37E+03
1.43E+03
1.51E+03
1.60E+03
1.71E+03
1 .85E+03
2.01E+03
2.21E+03
cmuv
1.01E-02
1.01E-02
1.01E-02
1.01E-02
1.01E-02
1.01E-02
1.01E-02
1.01E-02
1.01E-02
1.01E-02
1.01E-02
1.01E-02
1.01E-02
1.01E-02
1.01E-02
1.01E-02
1.01E-02
1.01E-02
1.01E-02
1.01E-02
1.01E-02
1.01E-02
1.01E-02
1.01E-02
1.01E-02
1.01E-02
1.01E-02
1.01E-02
1.01E-02
1.01E-02
1.01E-02
1.01E-02
1.01E-02
1.01E-02
1.01E-02
1.01E-02
1.01E-02
1.01E-02
1.01E-02
1.01E-02
1.01E-02
1.01E-02
1.01E-02
1.01E-02
1.01E-02
1.01E-02
1.01E-02
1.01E-02
1.01E-02
1.01E-02
1.01E-02
1.01E-02
1.01E-02
1.01E-02
1.01E-02
2.44E+02
2.95E+02
3.57E+02
4.32E+02
S.23E+02
6.34E+02
7.68E+02
9.31E+02
.13E+03
.37E+03
.37E+03
.37E+03
.37E+03
.37E+03
.37E+03
.37E+03
.37E+03
HC
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
3.40E-05
2.SOE-OS
1.83E-05
1.33E-05
9.66E-06
6.98E-06
5.04E-06
3.63E-06
2.61E-06
1.88E-06
1.29E-06
8.81E-07
5.95E-07
4.00E-07
2.67E-07
1.77E-07
1.17E-07
vg
O.OOE+00
1.21E-04
3.07E-04
5.23E-04
7.S9E-04
1.01E-03
1.27E-03
1.55E-03
1.83E-03
2.12E-03
2.41E-03
2.44E-03
2.48E-03
2.52E-03
2.57E-03
2.64E-03
2.71E-03
2.80E-03
2.90E-03
3.01E-03
3.14E-03
3.29E-03
3.45E-03
3.63E-03
3.83E-03
4.03E-03
4.25E-03
4.46E-03
4.67E-03
4.86E-03
5.04E-03
5.18E-03
5.27E-03
5.32E-03
5.30E-03
5.22E-03
5.07E-03
4.86E-03
4.59E-03
4.27E-03
3.92E-03
3.55E-03
3.18E-03
2.81E-03
2.45E-03
2.13E-03
1.84E-03
1.58E-03
1.34E-03
1.13E-03
9.43E-04
7.92E-04
6.63E-04
5.50E-04
4.30E-04
1.20E+00
1.20E+00
1.20E+00
1.20E+00
1.20E+00
1.20E+00
1.20E+00
1 .20E+00
1.20E+00
1 .20E+00
1.20E+00
1.20E+00
1.20E+00
1.20E+00
1.20E+00
1 .20E+00
1.20E+00
ug
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
2.75E-05
2.16E-05
2.93E+02
2.93E+02
2.93E+02
2.93E+02
2.93E+02
2.93E+02
2.93E+02
2.93E+02
2.93E+02
2.93E+02
2.93E+02
2.93E+02
2.93E+02
2.93E+02
2.93E+02
2.93E+02
2.93E+02
H
4.80E-01
4.55E-01
3.79E-01
3.43E-01
3.20E-01
3.05E-01
2.92E-01
2.83E-01
2.75E-01
2.68E-01
2.62E-01
2.61E-01
2.60E-01
2.60E-01
2.59E-01
2.57E-01
2.S6E-01
2.55E-01
2.53E-01
2.51E-01
2.48E-01
2.45E-01
2.42E-01
2.39E-01
2.35E-01
2.31E-01
2.27E-01
2.22E-01
2.17E-01
2.12E-01
2.07E-01
2.01E-01
1.96E-01
1.91E-01
1.85E-01
1.80E-01
1.75E-01
1.69E-01
1.64E-01
1.60E-01
1.55E-01
1.50E-01
1.46E-01
1.41E-01
1.37E-01
1 .33E-01
1.29E-01
1.25E-01
1.21E-01
1.18E-01
1.14E-01
1.11E-01
1.07E-01
1.04E-01
9.98E-02
3.01E+00
3.11E+00
3.22E+00
3.34E+00
3.45E+00
3.56E+00
3.68E+00
3.79E+00
3.91E+00
4.03E+00
4.17E+00
4.31E+00
4.45E+00
4.58E+00
•4.72E+00
4.85E+00
4.98E+00
V
1.04E-01
1.99E-02
2.51E-02
2.86E-02
3.13E-02
3.36E-02
3.55E-02
3.72E-02
3.87E-02
4.00E-02
4.12E-02
4.14E-02
4.15E-02
4.17E-02
4.19E-02
4.22E-02
4.25E-02
4.28E-02
4.33E-02
4.38E-02
4.44E-02
4.50E-02
4.58E-02
4.67E-02
4.78E-02
4.89E-02
5.02E-02
5.17E-02
5.33E-02
5.50E-02
5.69E-02
5.89E-02
6.11E-02
6.33E-02
6.57E-02
6.82E-02
7.08E-02
7.34E-02
7.61E-02
7.89E-02
8.17E-02
8.44E-02
8.72E-02
8.99E-02
9.25E-02
9.51E-02
9.74E-02
9.96E-02
1.01E-01
1.03E-01
1.04E-01
1.05E-01
1.06E-01
1.05E-01
1.05E-01
3.01E+00
3.12E+00
3.23E+00
3.34E+00
3.4SE+00
3.56E+00
3.68E+00
3.80E+00
3.91E+00
4.03E+00
4.17E+00
4.31E+00
4.45E+00
4.S9E+00
4.72E+00
4.8SE+00
4.98E+00
vx
O.OOE+00
2.84E-01
3.20E-01
3.42E-01
3.57E-01
3.69E-01
3.79E-01
3.87E-01
3.94E-01
4.00E-01
4.05E-01
4.06E-01
4.06E-01
4.07E-01
4.08E-01
4.09E-01
4.11E-01
4.12E-01
4.14E-01
4.16E-01
4.18E-01
4.21E-01
4.24E-01
4.28E-01
4.31E-01
4.36E-01
4.40E-01
4.45E-01
4.50E-01
4.56E-01
4.62E-01
4.67E-01
4.73E-01
4.79E-01
4.85E-01
4.90E-01
4.96E-01
5.01E-01
5.06E-01
5.11E-01
5.15E-01
5.19E-01
5.23E-01
5.27E-01
5.30E-01
5.33E-01
5.35E-OV
5.38E-0'
5.40E-01
5.42E-01
5.43E-01
5.45E-01
5.46E-01
5.46E-01
5.30E-01
-------
1.926+03
2.36E+03
2.91E+03
3.61E+03
4.47E+03
5.54E+03
9.75E-07
6.59E-07
4.43E-07
2.95E-07
1.96E-07
1.30E-07
9.75E-07
6.59E-07
4.436-07
2.95E-07
1.96E-07
1.30E-07
9.90E-01
9.90E-01
9.90E-01
9.90E-01
9.90E-01
9.90E-01
1.01E-02
1.01E-02
1.01E-02
1.01E-02
1.01E-02
1.01E-02
1.01E-02 O.OOE+00 3.34E-04 1.726-05 9.586-02 1.05E-01 5.29E-01
1.01E-02 -2.69E-05
1.01E-02 -1.81E-05
1.01E-02 O.OOE+00
1.01E-02 -9.08E-06
1.01E-02 -4.76E-05
O.OOE+00
O.OOE+00
8.65E-05
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
7.33E-06
O.OOE+00
O.OOE+00
9.18E-02
8.78E-02
8.38E-02
7.97E-02
7.55E-02
1.03E-01
1.01E-01
9.76E-02
9.40E-02
8.98E-02
1
time averaged (tav * 1800. s) volune concentration: concentration contour parameters
c(x,y,z,t> « cc(x) • +exp(-zb*zb»
c(x,y,z,t) « concentration (volume fraction) at (x,y,z,t)
x * downwind distance (m)
y * crosswind horizontal distance (m)
z = height (m)
t = time (s)
erf = error fincton
xa * (x-xc+bx)/(sr2*betax)
xb =
yb = (y-b)/(sr2*betac)
exp - exponential function
za = (z-zc)/(sr2*sig>
zb =
-------
3.34E+02
4.05E+02
4.90E+02
5.95E+02
7.22E+02
8.75E+02
1.06E+03
1.29E+03
1.57E+03
1.92E+03
2.36E+03
2.91E+03
3.61E+03
4.47E+03
5.54E+03
4.78E-05
4.15E-05
3.59E-05
3.10E-05
2.67E-05
2.29E-05
1.97E-05
1.68E-05
1.45E-05
1.24E-05
1.07E-05
9.24E-06
8.00E-06
6.9SE-06
6.05E-06
2.93E+00
2.94E+00
2.94E+00
2.94E+00
2.95E+00
2.95E+00
2.95E+00
2.95E+00
2.95E+00
2.95E+00
2.95E+00
2.95E+00
2.95E+00
2.95E+00
2.95E+00
2.55E+01
3.05E+01
3.65E+01
4.366*01
5.21E+01
6.23E+01
7.42E+01
8.84E+01
1 .05E+02
1.26E+02
1. 526+02
1.83E1-02
2. 206+02
2.646+02
3.17E+02
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
1.60E+01
1 .81E+01
2.06E+01
2.34E+01
2.66E+01
3.03E+01
3.46E+01
3.9SE+01
4.65E+01
5.46E+01
6.40E+01
7.50E+01
a.77E+01
1.02E+02
1.19E+02
2.57E+02
3.00E+02
3.51E+02
4.10E+02
4.80E+02
5.63E+02
6.60E+02
7.74E+02
7.48E+02
8.31E+02
9.32E+02
1.05E+03
1.20E+03
1 .38E+03
1.60E+03
3.34E+02
4.05E+02
4.90E+02
5.95E+02
7.22E+02
8.75E+02
1.06E+03
1.29E+03
1.57E+03
1.92E+03
2.36E+03
2.91E+03
3.61E+03
4.47E+03
5.54E+03
3.57E+02
4.32E+02
S.23E+02
6.34E+02
7.68E+02
9.31E+02
1.13E+03
1.37E+03
1.37E+03
1.37E+03
1.37E+03
1 .37E+03
1.37E+03
1 .37E+03
1 .37E+03
2.91E+00
3.53E+00
4.27E+00
5.17E+00
6.27E+00
7.60E+00
9.22E+00
1.12E+01
2.43E+02
3.6SE+02
4.79E+02
5.93E+02
7.15E+02
8.49E+02
9.98E+02
time averaged (tav = 1800. s) volume concentration: concentration in the z « .00 plane.
downwind
distance
x (m)
-3.08E+00
•2.46E+00
-1.85E+00
-1.23E+00
-6.15E-01
3.87E-07
6.15E-01
1 .23E+00
1.85E+00
2.46E+00
3.08E+00
3.14E+00
3.22E+00
3.32E+00
3.44E+00
3.58E+00
3.75E+00
3.96E+00
4.22E+00
4.53E+00
4.91E+00
5.37E+00
5.92E+00
6.60E+00
7.41E+00
8.41E+00
9.62E+00
1.11E+01
1.29E+01
1.50E+01
1.76E+01
2.08E+01
2.47E+01
2.94E+01
3.51E+01
4.20E+01
5.04E+01
6.06E+01
7.29E+01
8.79E+01
1.06E+02
1.28E+02
1 .55E+02
1 .88E+02
2.27E+02
2.75E+02
3.34E+02
4.05E+02
4.90E+02
5.95E+02
7.22E+02
8.75E+02
time of
max cone
(8)
3.41E+02
3.41E+02
3.40E+02
3.40E+02
3.40E+02
3.40E+02
3.40E+02
3.40E+02
3.40E+02
3.41E+02
3.41E+02
3.41E+02
3.41E+02
3.41E+02
3.41E+02
3.41E+02
3.41E+02
3.41E+02
3.41E+02
3.41E+02
3.41E+02
3.41E+02
3.42E+02
3.42E+02
3.42E+02
3.42E+02
3.43E+02
3.43E+02
3.43E+02
3.44E+02
3.45E+02
3.45E+02
3.47E+02
3.48E+02
3.49E+02
3.51E+02
3.53E+02
3.56E+02
3.59E+02
3.63E+02
3.68E+02
3.74E+02
3.81E+02
3.90E+02
4.00E+02
4.13E+02
4.28E+02
4.47E+02
4.69E+02
4.97E+02
5.30E+02
5.71E+02
cloud
duration
(s)
6.80E+02
6.80E+02
6.80E+02
6.80E+02
6.80E+02
6.80E+02
6.80E+02
6.80E+02
6.80E+02
6.80E+02
6.80E+02
6.80E+02
6.80E+02
6.80E+02
6.80E+02
6.80E+02
o.BOE+02
6.80E+02
6.80E+02
6.80E+02
6.80E+02
6.80E+02
6.80E+02
6.80E+02
6.80E+02
6.80E+02
6.80E+02
6.80E+02
6.80E+02
6.80E+02
6.80E+02
6.80E+02
6.80E+02
6.80E+02
6.80E+02
6.80E+02
6.80E+02
6.80E+02
6.80E+02
6.80E+02
6.80E+02
6.80E+02
6.80E+02
6.80E+02
6.80E+02
6.80E+02
6.80E+02
6.80E+02
6.80E+02
6.80E+02
6.80E+02
6.80E+02
effective
half width
bbc (m)
3.08E+00
3.13E+00
3.17E+00
3.21E+00
3.25E+00
3.29E+00
3.33E+00
3.38E+00
3.42E+00
3.47E+00
3.52E+00
3.52E+00
3.53E+00
3.S4E+00
3.SSE+00
3.56E+00
3.57E+00
3.59E+00
3.61E+00
3.64E+00
3.67E+00
3.71E+00
3.76E+00
3.82E+00
3.90E+00
3.99E+00
4.11E+00
4.25E+00
4.43E+00
4.66E+00
4.94E+00
5.29E+00
5.73E+00
6.28E+00
6.95E+00
7.79E+00
8.82E+00
1.01E+01
1.16E+01
1.35E+01
1.58E+01
1.86E+01
2.20E+01
2.61E+01
3.11E+01
3.71E+01
4.43E+01
5.29E+01
6.33E+01
7.56E+01
9.04E+01
1.08E+02
average concentration (volume fraction) at (x,y,z)
y/bbc*
0.0
O.OOE+00
9.77E-04
1.19E-03
1.33E-03
1.43E-03
1.51E-03
1.58E-03
1.64E-03
1.69E-03
1.73E-03
1.76E-03
1.75E-03
1.73E-03
1. TIE-OS
1.68E-03
1.65E-03
1.62E-03
1.58E-03
1.53E-03
1.48E-03
1.42E-03
1.35E-03
1.28E-03
1.20E-03
1.11E-03
1.02E-03
9.24E-04
8.27E-04
7.30E-04
6.34E-04
5.42E-04
4.55E-04
3.75E-04
3.04E-04
2.42E-04
1.90E-04
1.46E-04
1.11E-04
8.38E-05
6.23E-05
4.59E-05
3.36E-05
2.44E-05
1.76E-05
1.27E-05
9.07E-06
6.48E-06
4.62E-06
3.29E-06
2.34E-06
1.67E-06
1.19E-06
y/bbc-
0.5
O.OOE+00
9.03E-04
1.08E-03
1.19E-03
1.26E-03
1.32E-03
1.36E-03
1.38E-03
1.41E-03
1.42E-03
1.43E-03
1.42E-03
1.40E-03
1.38E-03
1.36E-03
1.33E-03
1.30E-03
1.26E-03
1.22E-03
1.17E-03
1.11E-03
1.05E-03
9.88E-04
9.17E-04
8.42E-04
7.65E-04
6.B5E-04
6.06E-04
5.28E-04
4.S4E-04
3.84E-04
3.20E-04
2.62E-04
2.11E-04
1.68E-04
1.31E-04
1.01E-04
7.67E-05
5.76E-05
4.28E-05
3.16E-05
2.31E-05
1.67E-05
1.21E-05
8.70E-06
6.23E-06
4.45E-06
3.18E-06
2.26E-06
1.61E-06
1.15E-06
8.17E-07
y/bbc«
1.0
O.OOE+00
3.27E-04
3.89E-04
4.26E-04
4.50E-04
4.67E-04
4.78E-04
4.87E-04
4.93E-04
4.96E-04
4.99E-04
4.94E-04
4.87E-04
4.80E-04
4.72E-04
4.62E-04
4.50E-04
4.37E-04
4.22E-04
4.04E-04
3.85E-04
3.63E-04
3.40E-04
3.15E-04
2.88E-04
2.61E-04
2.33E-04
2.05E-04
1.78E-04
1.52E-04
1.28E-04
1.06E-04
8.63E-05
6.93E-05
5.48E-05
4.27E-05
3.29E-05
2.SOE-05
1.87E-OS
1.39E-05
1.02E-05
7.49E-06
5.44E-06
3.93E-06
2.82E-06
2.02E-06
1.45E-06
1.03E-06
7.35E-07
5.23E-07
3.72E-07
2.65E-07
y/bbc«
1.5
O.OOE+00
1.09E-05
1.52E-05
1.91E-05
2.28E-05
2.63E-05
2.96E-05
3.27E-05
3.56E-05
3.84E-05
4.09E-05
4.07E-05
4JJ5E-05
4.02E-05
3.99E-05
3.96E-05
3.91E-05
3.86E-05
3.80E-05
3.72E-05
3.64E-05
3.54E-05
3.42E-05
3.28E-05
3.12E-05
2.94E-05
2.74E-05
2.52E-05
2.27E-05
2.02E-05
1.76E-05
1.50E-05
1.25E-05
1.02E-05
8.21E-06
6.46E-06
4.99E-06
3.81E-06
2.86E-06
2.13E-06
1.57E-06
1.15E-06
8.34E-07
6.02E-07
4.33E-07
3.10E-07
2.22E-07
1.58E-07
1.13E-07
8.02E-08
5.71Er08
4.07E-08
y/bbc=
2.0
O.OOE+00
1.67E-08
3.49E-08
6.22E-08
1.00E-07
1.51E-07
2.14E-07
2.90E-07
3.78E-07
4.7BE-07
5.88E-07
5.94E-07
6.01E-07
6.10E-07
6.20E-07
6.33E-07
6.48E-07
6.66E-07
6.86E-07
7.11E-07
7.39E-07
7.71E-07
8.07E-07
8.46E-07
8.85E-07
9.22E-07
9.54E-07
9.74E-07
9.76E-07
9.57E-07
9.13E-07
8.44E-07
7.54E-07
6.52E-07
5.45E-07
4.42E-07
3.49E-07
2.70E-07
2.05E-07
1.53E-07
1.13E-07
8.30E-08
6.03E-08
4.36E-08
3.14E-08
2.25E-08
1.61E-08
1.15E-08
8.16E-09
5.81E-09
4.14E-09
2.95E-09
y/bbc=
2.5
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
4.28E-11
9.08E-11
1.43E-10
2.97E-10
5.11E-10
8.41E-10
1.29E-09
1.39E-09
1.43E-09
1.47E-09
1.60E-09
1.68E-09
1.84E-09
2.00E-09
2.23E-09
2.53E-09
2.92E-09
3.43E-09
4.08E-09
4.93E-09
6.03E-09
7.42E-09
9.10E-09
1.11E-08
1.32E-08
1.53E-08
1.70E-08
1.80E-08
1.82E-08
1.73E-08
1.56E-08
1.34E-08
1.11E-08
6.83E-09
6.83E-09
5.17E-09
3.85E-09
2.83E-09
2.06E-09
1.49E-09/
1.07E-0'
7.68E-10
5.49E-10
3.92E-10
2.80E-10
1.99E-10
1.41E-10
1.00E-10
-------
1.06E+03
1.29E+03
1.57E+03
1.92E+03
2.36E+03
2.91E+03
3.61E+03
4.47E+03
5.54E+03
6.20E+02
6.80E+02
7.48E+02
8.31E+02
9.32E+02
1 .05E+03
1 .20E+03
1 .38E+03
1 .60E+03
6.80E+02
6.80E+02
6.87E+02
7.00E+02
7.20E+02
7.47E+02
7.83E+02
8.29E+02
8.86E+02
1.29E+02
1.53E+02
1.B3E+02
2.19E+02
2.63E+02
3.16E+02
3.80E+02
4.57E+02
5.49E+02
S.48E-07
6.06E-07
4.17E-07
2.87E-07
1.97E-07
1.36E-07
9.38E-08
6.50E-08
4.53E-08
5.83E-07
4.17E-07
2.87E-07
1.97E-07
1.36E-07
9.34E-08
6.45E-08
4.47E-08
3.11E-08
1.89E-07
I.35E-07
9.31E-08
6.40E-08
4.40E-08
3.03E-08
2.09E-08
1.45E-08
1.01E-08
2.90E-08
2.07E-08
1.43E-08
9.82E-09
6.75E-09
4.65E-09
3.21E-09
2.22E-09
1.55E-09
2.10E-09
1.50E-09
1.03E-09
7.11E-10
4.89E-10
3.37E-10
2.33E-10
1.61E-10
1.12E-10
7.18E-11
5.15E-11
3.51E-11
2.43E-11
1.67E-11
1.16E-11
8.08E-12
5.43E-12
3.81E-12
time averaged (tav * 1800. s) volune concentration: inaxinun concentration (voltne fraction) along center I inc.
downwind
distance
x (m)
-3.08E+00
-2.46E+00
-1.85E*00
-1.23E+00
-6.15E-01
3.87E-07
6.15E-01
1.23E+00
1.85E+00
2.46E+00
3.08E+00
3.14E+00
3.22E+00
3.32E+00
3.44E4-00
3.58E+00
3.75E+00
3.96E+00
4.22E+00
4.53E+00
4.91E+00
5.37E+00
5.92E+00
6.60E+00
7.41E+00
8.41E+00
9.62E+00
1.11E+01
1.29E+01
1.50E+01
1.76E+01
2.08E+01
2.47E+01
2.94E+01
3.51E+01
4.20E+01
5.04E+01
6.06E*01
7.29E+01
8.79E+01
1.06E+02
1.28E*02
1.55E+02
1 .88E+02
2.27E+02
2.75E+02
3.34E*02
4.05E+02
4.90E+02
5.95E+02
7.22E+02
8.75E+02
1.06E+03
1.29E+03
1.57E+03
1.92E+03
2.36E+03
2.91E+03
height
z (m)
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
O.OOE+00
naxinin
time of
concentration max cone
c(x,0,z)
O.OOE+00
9.77E-04
1.19E-03
1.33E-03
1.43E-03
1.51E-03
1.58E-03
1.64E-03
1.69E-03
1.73E-03
1.76E-03
1.75E-03
1.73E-03
1.71E-03
1.68E-03
1.65E-03
1 .62E-03
1.58E-03
1 -53E-03
1.48E-03
1.42E-03
1.35E-03
1.28E-03
1.20E-03
1.11E-03
1.02E-03
9.24E-04
8.27E-04
7.30E-04
6.34E-04
5.42E-04
4.5SE-04
3.75E-04
3.04E-04
2.42E-04
1.90E-04
1.46E-04
1.11E-04
6.38E-05
6.23E-05
4.59E-05
3.36E-05
2.44E-05
1. 766-05
1.27E-05
9.07E-06
6.48E-06
4.62E-06
3.29E-06
2.34E-06
1.67E-06
1.19E-06
8.48E-07
6.06E-07
4.17E-07
2.87E-07
1.97E-07
1.36E-07
(S)
3.41E+02
3.41E+02
3.40E+02
3.40E+02
3.40E+02
3.40E+02
3.40E+02
3.40E+02
3.40E+02
3.41E+02
3.41E+02
3.41E+02
3.41E+02
3.41E+02
3.41E+02
3.41E+02
3.41E+02
3.41E+02
3.41E+02
3.41E+02
3.41E+02
3.41E+02 :
3.42E+02
3.42E+02
3.42E+02
3.42E+02
3.43E+02
3.43E+02
3.43E+02
3.44E+02
3.45E+02
3.45E+02
3.47E+02
3.48E+02
3.49E+02
3.51E+02
3.53E+02
3.56E+02
3.59E+02
3.63E+02
3.68E+02
3.74E+02 '
3.81E+02
3.90E+02
4.00E+02
4.13E+02
4.28E+02
4.47E+02
4.69E+02
4.97E+02
5.30E+02
5.71E+02
6.20E+02
6.80E+02
7.48E+02
8.31E+02
9.32E+02
1.05E+03
cloud
duration
(s)
6.80E+02
6.80E+02
6.80E+02
6.80E+02
6.80E+02
6.80E+02
6.80E+02
6.80E+02
6.80E+02
6.80E+02
6.80E+02
6.80E+02
6.80E+02
6.80E+02
6.80E+02
6.80E+02
6.80E+02
6.80E+02
6.80E+02
6.80E+02
6.80E+02
6.80E+02
6.80E+02
6.80E+02
6.80E+02
6.80E+02
6.80E+02
6.80E+02
6.80E+02
6.80E+02
6.80E+02
6.80E+02
6.80E+02
6.80E+02
6.80E+02
6.80E+02
6.80E+02
6.80E+02
6.80E+02
6.80E+02
6.80E+02
6.80E+02
6.80E+02
6.80E+02
6.80E+02
6.80E+02
6.80E+02
6.80E+02
6.80E+02
6.80E+02
6.80E+02
6.80E+02
6.80E+02
6.80E+02
6.87E+02
7.00E+02
7.20E+02
7.47E+02
-------
3.61E+03 O.OOE+00 9.38E-08 1.20E+03 7.B3E+02
4.47E+03 O.OOE+00 6.50E-08 1.38E+03 8.29E+02
5.546+03 O.OOE+00 4.53E-08 1.60E+03 8.86E+02
-------
ATTACHMENT 3
Summary of Exposure Concentrations at'
Specific Receptor Locations
v
Volume YD External Review Draft
Appendix ¥11-4 Do Not Cite or Quote
-------
From Slab output file:
Scenario:
Accident Location:
Duration:
Meteorology:
Chemical:
Vapor phase mole fraction:
LOG:
IDLH:
RUN01.OOT
CONSERV
ON-SITE
UNMITIG
TYPICAL
FORMALDEHYDE
0.478
9.600
19.600
*0utput adjusted to be distance from fenceline.
X,m Max concentration, ppm
25.00
50.00
100.00
200.00
300.00
400.00
500.00
600.00
700.00
. 800.00
900.00
1000.00
1250.00
1500.00
1750.00
2000.00
2250.00
2500.00
3000.00
4000.00
5000.00
10000.00
15000.00
20000.00
429.34
.317.82
194.16
95.50
57.83
38.29
27.68
21.37
16.99
13.61
11.43
9.59
6.74
4.96
3.89
3.16
2.56
2.19
1.64
1.01
0.71
0.25
0.14
0.09
Concentration (ppm)
LOG
IDLH
9.6000
19.6000
Distance to (m)
999.27
640.38
Volume VH
Appendix VII-4
External Review Draft
Do Not Cite or Quote
-------
From Slab output file:
Scenario:
^---^ Accident Location:
f Duration:
V_x Meteorology:
Chemical:
Vapor phase mole fraction:
LOG:
• IDLH:
RUN02.OUT
CONSERV
ON-SITE
MITIGAT
TYPICAL
FORMALDEHYDE
0.742
9.600
19.600
*0utput adjusted to be distance from fenceline.
X,m Max concentration, ppm
25.00
50.00
100.00
200.00
300.00
400.00
' 500.00
600.00
700.00
800.00
900.00
1000.00
1250.00
1500.00
,-^ 1750.00
2000.00
, y 2250.00
2500.00
3000.00
4000.00
5000.00
10000.00
15000.00
20000.00
476.47
358.89
224.89
113.41
69.36
46.47
33.82
26.14
20.83
16.75
14.09
11.77
7.95
5.73
4.48
3.56
2.88
2.43
1.76
1.10
0.76
0.25
0.13
0.08
Concentration (ppm)
LOC
IDLH
9.6000
19.6000
Distance to (m)
1141.92
730.21
Volume VH
Appendix VII-4
External Review Draft
Do Not Cite or Quote
-------
From Slab output file:
Scenario :
Accident Location:
Duration:
Meteorology:
r phase mole
1
put adjusted
X,m
25.00
50.00
100.00
200.00
300.00
400.00
500.00
600.00
700.00
800.00
900.00
1000.00
1250.00
1500.00
1750.00
2000.00
2250.00
2500.00
3000.00
4000.00
5000.00
10000.00
15000.00
X,m
25.00
50.00
100.00
200.00
300.00
400.00
500.00'
600.00
700.00
800.00
900.00
1000.00
1250.00
1500.00
1750.00
2000.00
2250.00
2500.00
3000.00
4000.00
5000.00
10000.00
15000.00
Chemical :
fraction:
LOG:
IDLH:
— •- --
to be distance from
1
69.02
48.11
27.25
12.26
7.01
4.48
3.16
2.39
1.87
1.47
1.23
1.02
0.70
0.50
0.39
0.32
0.25
0.22
0.16
0.10
0.07
0.02
0.01
28
796.32
603.23
381.34
195.52
120.67
81.54
59. 8S
46.52
37.22
30.02
25.32
21.34
15.17
11.27
8.88
7.24
5.91
5.07
3.80
2.37
1.67
0.59
0.32
2
166.11
117.10
67.17
30.91
17.98
11.61
8.27
6.28
4.93
3.92
3.26
2.72
1.89
1.38
1.07
0.86
0.69
0.59
0.44
0.27
0.19
0.06
0.03
29
2262.62
1792.22
1211.15
674.08
438.08
306.88
230.61
182.77
148.57
121.61
103.69
88.34
63.72
48.28
38.37
31.47
25.87
22.31
16.90
10.69
7.64
2.59
1.30
RUN03.OUT
CONSERV
ON-SITE
UNMITIG
WORST
- -FORMALDEHYDE
0.478
9.600
19.600
fenceline.
3
466.75
339.75
203.44
98.16
58.18
38.24
27.45
21.02
16.61
13.23
11.05
9.21
6.43
4.72
3.67
2.96
2.39
2.04
1.51
0.93
0.64
0.21
0.11
30
61.47
43.13
24.71
11.31
6.57
4.25
3.03
2.30
1.81
1.44
1.20
1.00
0.70
0.51
0.40 *
0.32
0.26
0.22
0.16
0.10
0.07
0.02
0.01
4
971.81
724.29
446.33
222.32
134.61
89.71
64.75
49.93
39.64
31.71
26.59
22.27
15.59
11.45
8.95
7.24
5.86
5.01
3.73
2.31
1.59 .
0.51
0.25
31
169.07
122.31
72.54
34.63
20.53
13.43
9.66
7.40
5.86
4.67
3.91
3.27
2.28
1.67
1.31
1.06
0.86
0.73
0.54
0.33
0.23
0.08
0.04
5
1914.76
1457.10
926.57
483.21
300.86
204.33
150.63
117.54
94.20
76.03
64.34
54.36
38.49
28.57
22.52
18.32
14.91
12.80
9.58
5.94
4.07
1.24
0.61
32
342.11
253.09
154.26
75.79
45.76
30.32
21.93
16.91
13.45
10.79
9.05
7.58
5.35
3.94
3.09
2.51
2.03
1.74
1.30
0.81
0.57
0.20
0.11
Volume VII
Appendix VII-4
External Review Draft
Do Not Cite or Quote
-------
6
3951.19
3038.31
2016.25
1147.64
771.82
560.81
432.81
350.82
291.38
243.81
210.81
182.39
135.56
104.68
84.88
70.33
57.59
49.66
36.53
-^ 22.78
15.41
y 4.32
^ 1.99
33
695.31
526.05
331.94
169.73
104.94
70.52
51.67
40.26
32.24
26.00
21.94
18.51
13.15
9.79
7.71
6.28
5.12
4.40
3.30
2.06
1.46
0.52
7
51.95.
36.12
20.42
9.19
.5.27
3.36
2.37
1.79
1.40
1.10
0.92
0.76
0.52
0.38
0.29
0.24
0.19
0.16
0.12
0.07
0.05
0.02
0.01
34
1983.05
1570.61
1055.63
586.27
379.75
265.64
199.26
157.64
128.10
104.88
89.29
76.04
55.06
41.46
33.03
27.11
22.29
19.25
14.60
9.23
6.60
2.33
8
123.63
87.10
49.81
22.89
13.29
8.59
6.09
4.65
3.66
2.90
2.42
2.01
1.40
1.02
0.79
0.64
0.52
0.44
0.33
0.20
0.14
0.05
0.03
35
54.45
38.32
21.93
10.07
5.84
3.78
2.69
2.05
1.61
1.28
1.07
0.89
0.62
0.45
0.35
0.28
23 .
0.29
1.19
0.
0.19
0.14
0.09
0.06
0.02
0.01
9
343.03
248.93
148.63
71.08
42.22
27.73
19.91
15.27
12.08
9.62
8.04
6.70
4.67
3.43
2.68
2.17
1.75
1.49
1.11
0.68
0.47
0.16
0.09
36
150.20
108.77
64.36
30.72
18.22
11.95
8.56
6.56
5.19
4.14
3.47
2.90
2.03
1.49
1.16
0.94
0.76
0.65
0.48
0.30
0.21
0.07
0.04
10
704.41
521.62
321.94
159.83
96.58
64.28
46.48
35.84
28.46
22.78
19.11
16.02
11.23
8.25
6.46
5.23
4.24
3.63
2.70
1.66
1.17 •
0.39
0.20
37
303.62
224.60
136.85
67.06
40.51
26.87
19.42
14.98
11.90
9.54
8.00
6.71
4.72
3.49
2.74
2.22
1.80
1.54
1.15
0.71
0.50
0.18
0.10
11
1429.94
1090.35
696.79
. 361.30
224.78
152.05
111.55
87.00
69.63
56.07
47.31
39.89
28.27
20.96
16.50
13.40
10.90
9.34
6.99
4.37
3.04
0.98
0.49
38
615.59
466.16
293.78
150.36
92.53
62.36
45.73
35.57
28.48
22.98
19.40
16.36
11.62
8.63
6.80
5.54
4.52
3.89
2.92
1.82
1.29
0.46
0.26
Volume VH
Appendix VII-4
External Review Draft
Do Not Cite or Quote
-------
12
3608.06
2819.74
1884.63
1053.44
693.01
493.80
375.65
300.62
246.73
203.96
174.87
149.99
109.89
83.65
67.13
55.44
45.87
39.80
30.11
18.74
12.91
3.83
1.82
39
49.09
34.46
19.75
9.07
5.26
3.40
2.42
1.84
1.45
1.15
0.96
0.80
0.56
0.41
0.32
0.25
0.21
0.18
0.13
0.08
0.06
0.02
0.01
13
41.53
28.90
16.36
7.37
4.22
2.69
1.90
1.44
1.12
0.88
0.73
0.61
0.42
0.30
0.24
0.19
0.15
0.13
0.10
0.06
0.04
0.01
0.01
40
134.99
97.65
58.10
27.65
16.38
10.75
7.69
5.89
4.66
3.73
3.12
2.61
1.82
1.34
1.05
0.85
0.68
0.58
0.43
0.27
0.19
0,07
0.04
14
98.48
69.20
39.67
18.23
10.57
6.81
4.88
3.71
2.91
2.31
1.93
1.61
1.12
0.82
0.64
0.51
0.41
0.35
0.26
0.16
0.11
0.04
0.02
41
272.73
201.89
123.00
60.58
36.39
24.13
17.44
13.46
10.70
8.56
7.19
6.03
4.25
3.13
2.46
2.00
1.62
1.39
1.03
0.64
0.45
0.16
0.09
15
272.38
197.23
117.64
55.97
33.30
21.83
15.66
11.99
9.50
7.59
6.34
5.29
3.70
2.71
2.12
1.71
1.38
1.18
0.88
0.54
0.38
0.13
0.07
42
553.90
418.93
263.69
134.73
83.11
56.12
40.96
31.87
25.51
20.57
17.35
14.63
10.41
7.74
6.09
4.96
4.06
3.49
2.62
1.64
1.16
0.41
0.23
16
557.15
411.56
252.32
124.50
75.23
49.89
36.18
27.89
22.15
17.74
14.90
12.50
8.76
6.44
5.06
4.10
3.32
2.84
2.12
1.31
0.92
0.32
0.17
43
84.06
60.91
36.21
17.24
10.22
6.67
4.80
3.68
2.91
2.32
1.94
1.62
1.14
0.83
0.65
0.53
0.43
0.36
0.27
0.17
0.12
0.04
0.02
17
1129.09
858.83
545.01
282.50
175.05
118.48
86.92
67.46
54.01
43.65
36.82
31.03
22.01
16.32
12.84
10.45
8.52
7.30
5.47
3.40
2.40
0.82
0.42
44
170.23
125.60
76.84
37.60
22.65
15.02
10.87
8.38
6.65
5.33
4.48
3.76
2.65
1.95
1.53
1.24
1.01
0.86
0.65
0.40
0.28
0.10
0.06
Volume VII
Appendix VII-4
External Review Draft
Do Not Cite or Quote
-------
18
3084.38
2437.95
1641.56
919.02
601.16
422.91
319.32
253.99
207.30
170.39
145.45
124.20
90.33
68.28
54.57
44.89
36.97
31.93
24.25
N 15.45
10.76
3.28
1.64
45
67.20
48.82
28.96
13.80
8.17
.37
.84
2.95
2.33
1.86
1.55
1.30
0.91
0.67
0.52
0.42
0.34
0.29
0.22
0.13
0.09
0.03
0.02
5
3
19
34.54
24.11
13.63
6.13
3.51
2.24
1.58
1.20
0.93
0.73
0.61
0.51
0.35
0.25
0.20
0.16
0.13
0.11
0.08
0.05
0.03
0.01
0.01
46
135.89
100.47
61.45
30.07
18.11
11.99
8.70
6.71
5.33
4.26
3.58
3.00
2.12
1.56
1.22
0.99
0.81
0.69
0.52
0.32
0.22
0.08
0.04
20
81.99
57.59
32.99
15.12
8.79
5.66
4.04
3.08
2.42
1.92
1.60
1.34
0.93
0.68
0.53
0.43
0.34
0.29
0.22
0.13
0.09
0.03
0.02
47
90.64
66.68
40.82
20.01
12.05
8.01
5.80
4.46
3.55
2.84
2.39
2.00
1.41
1.04
0.82
0.66
0.54
0.46
0.34
0.21
0.15
0.05
0.03
21
226.07
163.86
97.26
46.33
27.54
18.04
12.95
9.95
7.86
6.25
5.24
4.38
3.06
2.24
1.75
1.42
1.14
0.98
0.73
0.45
0.31
0.11
0.06
48
67.84
50.23
30.58
15.01
9.04
6.00
4.33
3.34
2.66
2.13
1.79
1.50
1.06
0.78
0.61
0.50
0.40
0.35
0.26
0.16
0.11
0.04
0.02
22
459.44
340.02
207.91
102.39
61.64
41.02
29.67
22.88
18.19
14.58
12.25
10.27
7.20
5.33
4.17
3.38
2.74
2.34
1.75
1.08
0.76
0.27
0.15
49
105.19
72.18
40.62
18.34
10.49
6.72
4.73
3.58
2.80
2.21
1.84
1.52
1.05
0.76
0.59
0.47
0.38
0.32
0.24
0.14
0.10
0.03
0.02
23
932.94
709.26
449.32
230.93
142.85
96.41
70.97
55.03
44.02
35.54
29.98
25.27
17.96
13.31
10.50
8.53
6.94
5.96
4.48
2.79
1.97
0.69
0.37
50
256.66
181.44
104.79
48.11
28.07
18.14
12.86
9.78
7.69
6.10
5.08
4.22
2.92
2.13
1.65
1.33
1.07
0.91
0.68
0.41
0.28
0.09
0.04
Volume VII
Appendix VII-4
External Review Draft
Do Not Cite or Quote
-------
24
2626.70
2081.28
1407.01
785.30
511.91
359.14
270.62
214.63
174.58
142.97
121.93
103.99
75.35
56.67
45.28
37.20
30.58
26.40
20.02
12.69
9.02
2.90
1.45
51
737.42
536.48
322.04
155.05
92.16
60.46
43.45
33.27
26.27
20.91
17.45
14.55
10.15
7.41
5.76
4.64
3.75
3.21
2.37
1.45
0.99
0.29
0.14
25
70.24
49.36
28.24
12.96
7.52
4.85
3.46
2.63
2.07
1.65
1.37
1.14
0.79
0.58
0.45
0.36
0.29
0.25
0.19
0.11
0.08
0.03
0.02
52
1506.13
1111.03
680.82
338.09
205.32
136.73
99.50
76.91
61.21
49.07
41.14
34.46
24.23
17.84
13.98
11.34
9.18
7.87
5.81
3.54
2.41
0.70
0.33
26
193.42
140.18
83.31
39.67
23.51
15.40
11.07
8.49
6.70
5.32
4.47
3.74
2.61
1.92
1.50
1.21
0.98
0.84
0.62
0.38
0.27
0.09
0.05
53
2522.04
1882.95
1190.86
626.98
399.04
276.22
206.53
162.95
131.98
107.64
91.54
77.80
56.04
42.25
33.52
27.19
22.07
18.82
13.69
8.42
5.67
1.61
0.74
27
391.76
289.80
177.23
87.25
52.70
34.83
25.22
19.45
15.45
12.36
10.39
8.72
6.12
4.52
3.55
2.87
2.33
2.00
1.49
0.92
0.65
0.23
0.13
54
3842.79
2965.40
2004.13
1187.28
826.85
618.17
491.10
405.04
341.94
291.15
255.92
223.56
165.38
128.80
103.52
82.37
70.21
58.04
43.68
26.34
17.85
4.90
2.16
Volume VH
Appendix VII-4
External Review Draft
Do Not Cite or Quote
-------
X,m Max concentration, ppm
25.00
50.00
100.00
^ 200.00
300.00
400.00
500.00
600.00
700.00
800.00
900,00
1000.00
1250.00
1500.00
1750.00
2000.00
2250.00
2500.00
3000.00
4000.00
5000.00
10000.00
15000.00
3951.19
3038.31
2016.25
1187.28
826.85
618.17
491.10
405.04
341.94
291.15
255.92
223.56
165.38
128.80
103.52
82.37
70.21
58.04
43.68
26.34
17.85
4.90
2.16
Concentration (ppm)
Distance to (m)
9.6000
19.6000
8185.01
4793.62
Volume Vn
Appendix VH-4
External Review Draft
Do Not Cite or Quote
-------
From Slab output file:
Scenario:
Accident Location:
Duration:
Meteorology:
Vapor phase mole
*Output adjusted
X,m
25.00
50.00
100.00
200.00
300.00
400.00
500.00
600.00
700.00
800.00
900.00
1000.00
1250.00
1500.00
1750.00
2000.00
2250.00
2500.00
3000.00
4000.00
5000.00
10000.00
15000.00
20000.00
X,ffi
25.00
50.00
100.00
200.00
300.00
400.00
500.00
600.00
700.00
800.00
900.00
1000.00
1250.00
1500.00
1750.00
2000.00
2250.00
2500.00
3000.00
4000.00
5000.00
10000.00
15000.00
20000.00
Chemical :
fraction:
LOG:
IDLH:
** — —
to be distance from
1
81.56
56.95
32.47
14.77
8.49
5.44
3.84
2.86
2.20
1.70
1.41
1.15
0.78
0.56
0.44
0.34
0.28
0.23
0.16
0.10
0.07
0.02
0.01
0.01
28
871.31
670.87
435.13
230.12
144.02
98.28
72.61
56.73
45.58
36.91
31.18
26.16
17.72
12.77
10.01
7.95
6.47
5.42
3.91
2.47
1.70
0.55
0.28
0.18
2
192.89
137.40
80.06
37.55
21.99
14.30
10.21
7.63
5.90
4.59
3.82
3.11
2.12
1.55
1.21
0.94
0.78
0.64
0.46
0.28
0.19
0.06
0.03
0.02
29
2329.06
1861.59
1280.35
732.06
484.38
344.57
262.00
200.89
158.62
125.26
107.26
89.55
62.73
47.28
36.37
29.82
24.33
20.86
15.35
9.62
6.63
2.00
1.01
0.60
RUN04.OUT
CONSERV
ON-SITE
MITIGAT
WORST
FORMALDEHYDE
0.742
9.600
19.600
fenceline.
3
524.21
387.63
236.90
116.91
70.29
46.47
32.50
24.55
19.09
14.88
12.54
10.26
6.99
5.19
3.98
3.10
2.59
2.11
1.56
0.92
0.63
0.19
0.10
0.06
30
70.97
50.46
29.32
13.65
7.97
5.18
3.69
2.82
2.22
1.76
1.47
1.22
0.85
0.62
0.49
0.39
0.31
0.26
0.19
0.12
0.08
0.03
0.01
0.01
4
1058.75
794.34
499.03
254.05
155.85
100.85
71.89
54.58
42.37
33.91
28.15
23.55
16.35
12.04
9.03
7.31
5.90
5.00
3.65
2.22
1.51
0.44
0.22
0.13
31
189.90
139.49
84.51
41.18
24.67
16.24
11.70
9.04
7.16
5.70
4.78
4.00
2.80
2.05
1.57
1.26
1.00
0.85
0.62
0.38
0.26
0.09
0.05
0.03
5
1894.64
1438.12
' 921.84
486.75
290.03
195.90
144.13
110.24
85.97
71.78
58.93
50.73
35.31
26.04
20.77
16.26
13.74
11.22
8.42
5.06
3.43
0.99
0.47
0.27
32
379.26
285.48
178.34
89.88
54.82
36.64
26.69
20.65
16.46
13.22
11.08
9.29
6.55
4.70
3.62
2.89
2.30
1.97
1.43
0.89
0.62
0.20
0.11
0.07
/*'"
Volume VU
Appendix VII-4
Exteraal Review Draft
Do Not Cite or Quote
-------
6
3112.56
2402.57
1549.78
825.48
556.15
412.97
323.93
266.98
218.98
189.30
159.62
142.68
105.15
81.08
65.18
52.08
44.01
37.00
27.41
16.72
11.17
2.89
1.32
0.73
33
758.38
585.39
378.46
199.41
124.77
85.61
62.89
49.10
39.41
31.88
26.96
22.64
15.36
11.14
8.74
6.94
5.65
4.74
3.43
2.16
1.50
0.49
0.26
7
61.16
42.82
24.41
11.09
6.38
4.08
2.88
2.19
1.71
1.35
1.10
0.90
0.61
0.43
0.34
0.27
0.21
0.18
0.13
0.08
0.05
0.02
0.01
0.01
34
2072.46
1659.64
1140.28
653.79
431.97
306.62
232.82
185.76
148.32
116.71
98.60
81.00
55.81
42.64
33.22
26.34
22.05
18.46
13.79
8.59
5.98
1.88
0.91
7,
4,
3,
0.16
0.57
8
142.96
102.10
59.36
27.67
16.21
10.50
7.49
5.71
4.50
3.57
2.93
2.41
1.64
1.17
0.92
0.73
0.58
0.49
0.36
0.22
0.15
0.05
0.03
0.02
35
63.04
44.83
26.04
12.09
,08
,60
,28
2.50
1.97
1.57
1.31
1.09
0.76
0.55
0.43
0.35
0.28
0.23
0.17
0.10
0.07
0.02
0.01
0.01
9
386.47
284.95
174.05
85.49
51.25
33.89
24.38
18.75
14.67
11.44
9.47
7.75
5.32
3.90
3.02
2.36
1.94
1.60
1.16
0.72
0.50
0.16
0.08
0.05
36
168.52
123.75
75.13
36.54
21.89
14.45
10.43
8.00
6.33
5.06
4.24
3.55
2.48
1.83 »
1.43
1.14
0.91
0.77
0.56
0.34
0.23
0.08
0.04
0.03
10
783.37
591.10
.371.43
189.13
116.24
78.19
56.69
42.80
33.29
25.92
21.74
17.67
12.10
9.09
7.01
5.40
4.56
3.72
2.77
1.66
1.14
0.35
0.18
0.11
37
336.27
253.25
157.75
79.22
48.51
32.39
23.55
18.22
14.51
11.65
9.79
8.23
5.81
4.28
3.27
2.62
2.09
1.79
1.30
0.80
0.55
0.18
0.10
0.06
1 11
1514.99
1167.76
756.84
402.64
254.54
174.95
123.90
94.73
74.17
58.82
49.28
40.84
28.64
21.31
16.19
13.15
10.66
9.06
6.63
4.09
2.80
0.83
0.40
0.25
38
673.40
518.79
335.20
176.54
110.33
75.20
55.46
43.31
34.78
28.13
23.78
20.09
14.26
10.22
7.92
6.31
5.05
4.30
3.13
1.96
1.36
0.45
0.24
0.15
Volume VII
Appendix VII-4
External Review Draft
Do Not Cite or Quote
-------
12
3146.31
2439.67
1629.61
927.88
578.29
407.86
310.63
244.48
200.38
168.14
143.40
122.70
88.69
69.43
54.65
44.78
36.86
31.59
23.22
14.30
9.59
2.64
1.26
0.71
39
56.78
40.33
23.47
10.89
6.38
4.13
2.95
2.25
1.77
1.41
1.17
0.98
0.68
0.50
0.39
0.31
0.25
0.21
0.16
0.09
0.06
0.02
0.01
0.01
13
48.93
34.26
19.53
8.88
5.10
3.26
2.30
1.75
1.37
1.08
0.89
0.74
0.50
0.35
0.27
0.22
0.17
0.15
0.11
0.06
0.04
0.01
0.01
0.00
40
151.36
111.72
67.51
32.85
19.65
12.96
9.37
7.19
5.69
4.55
81
19
2.23
1.64
1.29
1.03
0.82
0.70
0.51
0.31
0.21
0.07
0.04
0.02
3
3
14
114.23
81.11
47.19
21.97
12.86
8.34
5.94
4.54
3.57
2.84
2.37
1.97
1.33
0.95
0.74
0.59
0.47
0.40
0.29
0.18
0.12
0.04
0.02
0.01
41
302.52
227.06
141.93
71.34
43.51
29.12
21.15
16.37
13.05
10.49
8.80
7.37
5.22
3.85
3.03
2.4-3
1.93
1.64
1.19
0.73
0.50
0.16
0.09
0.06
15
306.26
225.71
136.90
67.11
40.24
26.59
19.13
14.71
11.67
9.31
7.66
6.29
4.29
3.10
2.42
1.91
1.56
1.30
0.94
0.59
0.40
0.13
0.07
0.04
42
604.99
466.39
301.18
158.01
99.03
67.31
49.61
38.73
31.11
25.18
21.27
17.96
12.79
9.47
7.24
5.82
4.63
3.96
2.89
1.79
1.24
0.41
0.22
0.14
16
617.25
465,28
292.19
148.36
90.51
60.84
44.24
34.26
26.94
21.08
17.64
14.45
9.75
7.24
5.63
4.40
3.65
3.00
2.21
1.36
0.94
0.30
0.15
0.10
43
94.58
69.52
42.12
20.45
12.25
8.04
5.82
4.48
3.55
2.83
2.38
1.99
1.39
1.02
0.80
0.65
0.52
0.45
0.33
0.20
0.14
0.05
0.02
0.02
17
1223.67
943.27
614.56
326.82
205.85
141.45
104.18
78.91
61.77
48.36
40.79
33.23
23.13
17.30
13.32
10.54
8.79
7.31
5.43
3.32
2.30
0.72
0.36
0.22
44
188.15
141.61
88.06
44.37
27.02
18.02
13.12
10.16
8.09
6.49
5.46
4.59
3.24
2.39
1.88
1.52
1.24
1.06
0.80
0.48
0.33
0.11
0.06
0.04
Volume VII
Appendix VTI-4
External Review Draft
Do Not Cite or Quote
-------
18
2944.74
2311.65
1559.58
890.09
568.43
386.74
290.27
227.37
179.24
152.39
125.53
110.13
78.63
58.91
47.42
37.34
32.02
26.70
20.17
12.44
8.50
2.48
1.15
0.67
45
75.54
55.57
33.68
16.38
9.81
6.46
4.65
3.58
2.84
2.26
1.90
1.59
1.12
0.82
0.64
0.52
0.42
0.36
0.27
0.16
0.11
0.04
0.02
0.01
19
40.78
28.55
16.30
7.39
4.25
2.72
1.92
1.46
1.14
0.90
0.75
0.62
0.43
0.30
0.23
0.18
0.14
0.12
0.09
0.05
0.04
0.01
0.01
0.00
46
150.52
113.15
70.54
35.45
21.60
14.45
10.50
8.14
6.48
5.19
4.36
3.67
2.59
1.91
1.51
1.22
0.99
0.85
0.63
0.39
0.27
0.09
0.05
0.03
20
94.67
67.49
39.24
18.28
10.68
6.92
4.94
3.77
2.97
2.36
1.97
1.64
1.14
0.81
0.62
0.50
0.39
0.34
0.25
0.15
0.10
0.03
0.02
0.01
47
100.35
74.95
46.94
23.60
14.38
9.61
6.98
5.40
4.31
3.46
2.91
2.45
1.72
1.27
1.00
0.81
0.66
0.57
0.42
0.26
0.18
0.06
0.03
0.02
21
254.26
186.75
113.75
55.42
33.18
21.90
15.83
12.14
9.61
7.69
6.44
5.37
3.64
2.62
2.04
1.62
1.30
1.10
0.80
0.50
0.34
0.11
0.06
0.04
48
75.09
56.42
35.19
17.70
10.77
7.20
5.23
4.05
3.22
2.59
2.18
1.83
1.29
0.9^6
0.75
0.61
0.50
0.42
0.32
0.20
0.14
0.05
0.03
0.02
22
510.06
383.65
240.12
121.99
74.41
49.82
36.22
28.05
22.33
17.91
15.08
12.63
8.56
6.13
4.79
3.81
3.07
2.59
1.88
1.17
0.81
0.26
0.14
0.09
49
125.22
87.18
49.07
22.09
12.68
7.94
5.52
4.11
3.16
2.45
2.05
1.67
1.13
0.83
0.63
0.49
0.40
0.33
0.24
0.14
0.10
0.03
0.01
23
1020.68
786.11
510.60
271.00
170.49
116.15
86.16
67.21
53.07
41.57
34.78
28.48
19.42
14.53
11.29
8.76
7.40
6.03
4.53
2.75
1.91
0.62
0.32
0.20
50
295.73
211.70
123.96
58.26
33.56
21.18
14.95
11.22
8.62
6.84
5.63
4.66
3.17
2.32
1.75
1.39
1.14
0.94
0.69
0.41
0.28
0.08
0.04
0.01
0.02
Volume VU
Appendix VII-4
External Review Draft
Do Not Cite or Quote
-------
24
2633.54
2093;77
1423.67
811.51
540.49
386.23
278.16
215.61
171.01
138.80
117.14
. 99.53
71.01
53.26
40.88
33.77
27.23
23.44
17.04
10.75
7.28
2.22
1.10
0.65
51
798.08
584.24
353.53
172.65
99.61
64.70
46.37
34.98
26.78
21.99
17.83
15.29
10.44
7.54
5.73
4.64
3.66
3.14
2.26
1.37
0.92
0.26
0.12
0.07
25
81.05
57.74
33.56
15.58
9.12
5.92
4.22
3.23
2.54
2.02
1.68
1.40
0.98
0.71
0.54
0.43
0.35
0.29
0.21
0.13
0.09
0.03
0.02
0.01
52
1467.37
1079.80
665.01
321.70
194.14
130.91
95.52
72.34
56.96
46.65
38.29
32.57
22.59
16.75
13.17
10.22
8.58
6.95
5.17
3.00
2.01
0.56
0.26
0.14
26
217.38
159.74
97.03
47.24
28.32
18.69
13.43
10.34
8.20
6.55
5.48
4.59
3.20
2.28
1.75
1.40
1.12
0.96
0.70
0.43
0.30
0.10
0.05
0.03
53
2098.59
1573.56
979.43
491.31
316.19
224.55
167.55
134.74
109.27
90.81
76.44
66.13
47.34
35.23
27.90
22.39
18.40
15.14
10.94
6.47
4.32
1.16
0.52
0.29
27
434.80
327.43
204.46
103.46
63.11
42.22
30.67
23.77
18.93
15.17
12.75
10.70
7.51
5.40
4.16
3.31
2.63
2.25
1.64
1.02
0.70
0.23
0.12
0.08
54
3067.89
2255.16
1473.71
856.81
604.88
460.12
364.07
303.81
255.79
219.90
189.51
168.39
124.50
93.07
76.18
60.68
51.38
42.07
31.53
18.62
12.29
3.11
1.32
0.75
Volume VII
Appendix VII-4
External Review Draft
Do Not Cite or Quote
-------
X,m Max concentration/ ppm
25.00
50.00
-— "•' 100.00
200.00
300.00
400'. 00
500.00
600.00
700.00
800.00
900.00
1000.00
1250.00
1500.00
1750.00
2000.00 .
2250.00
2500.00
3000.00
4000.00
5000.00
10000.00
15000.00
20000.00
3146.31
2439.67
1629.61 — ~--
927.88
604.88
460.12
364.07
303.81
255.79
219.90
189.51
168.39
124.50
93.07
76.18
60.68
51.38
42.07
31.53
18.62
12.29
3.11
1.32
0.75
icentration (ppm)
Distance to (m)
9.6000
19.6000
6464.52
3924.27
Volume VH
Appendix VII-4
External Review Draft
Do Not Cite or Quote
-------
From Slab output file:
Scenario:
Accident Location:
Duration:
Meteorology:
Chemical:
Vapor phase mole fraction:
LOC:
IDLH:
RUN05.OUT
CONSERV
ON-SITE
UNMITIG
INVERSN
FORMALDEHYDE
0.478
9.600
19.600
*Output adjusted to be distance from fenceline.
X,m Max concentration, ppm
25.00
50.00
100.00
200.00
300.00
400.00
500.00
600.00
700.00
800.00
900.00
1000.00
1250.00
1500.00
1750.00
2000.00
2250.00
2500.00
3000.00
4000.00
5000.00
10000.00
15000.00
20000.00
6494.06
5038.76
3464.59
2068.94
1454.11
1101.68
867.51
720.65
607.79
522.51
452.54
403.52
304.94
235.86
194.85
159.25
135.99
113.41
87.83
54.79
38.15
11.23
5.33
3.08
Concentration (ppm)
LOC
IDLH
9.6000
19.6000
Distance to (m)
11380.26
8445.13
Volume Vn
Appendix VII-4
External Review Draft
Do Not Cite or Quote
-------
From Slab output file:
Scenario:
x Accident Location:
Duration:
Meteorology:
Chemical:
Vapor phase mole fraction:
LOG:
IDLH:
RUN06.0UT
CONSERV
ON-SITE
MITIGAT
INVERSN
FORMALDEHYDE
0.742
9.600
19.600
*Output adjusted to be distance from fenceline.
X,m May: concentration, ppm
25.00
50.00
100.00
200.00
300.00
400.00
500.00
600.00
700.00
800.00
900.00
1000.00
1250.00
1500.00
^-^ 1750.00
2000.00
v ^ 2250.00
2500.00
3000.00
4000.00
5000.00
10000.00
15000.00
20000.00
4450
3473
2427
1473
1060
813
646
544
454
396
338
303
227
177
144
116
99
82
62
38
26
7
3
1
.17
.82
.27
.06
.50
.60
.51
.01
.30
.47
.65
.76
.17
.19
.82-
.19
.41
.81
.75
.46
.09
.18
.27
.86
Concentration (ppm)
LOG
IDLH
9.6000
19.6000
Distance to (m)
9360.84
6716.09
Volume VH
Appendix VII-4
External Review Draft
Do Not Cite or Quote
-------
From Slab output file: RUN07.0UT
Scenario: CONSERV
Accident Location: ON-SITE
Duration: UNMITIG
Meteorology: — -- TYPICAL
Chemical: ACETONE
Vapor phase mole fraction: 0.273
LOC: 1960.000
IDLH: - 2442.000
*0utput adjusted to be distance from fenceline.
X,m Max concentration, ppm
25.00
50.00
100.00
200.00
300.00
400.00
500.00
'600.00
700.00
800.00
900.00
1000.00
1250.00
1500.00
1750.00
2000.00
2250.00
2500.00
3000.00
4000.00
5000.00
10000.00
15000.00
41.05
30.35
18.68
9.26
5.60
3.73
2.69
2.07
1.65
1.32
1.11
0.93
0.65
0.48
0.37
0.30
0.25
0.21
0.16
0.10
0.07
0.02
0.01
Concentration (ppm) Distance to (m)
LOC 1960.0000 less than 25.00
IDLH 2442.0000 less than 25.00
Volume VH . External Review Draft
Appendix VH^ Do Not Cite or Quote
-------
From Slab output file: RUN08.OUT
Scenario: CONSERV
Accident Location: ON-SITE
Duration: MITIGAT
_,/ Meteorology: _ _ TYPICAL
Chemical: ACETONE
Vapor phase mole fraction: 0.585
LOC: 1960.000
IDLH: 2442.000
*0utput adjusted to be distance from fenceline.
'X,m Max concentration, ppm
25.00
50.00
100.00
200.00
300.00
400.00
500.00
• 600.00
700.00
800.00
900.00
1000.00
1250.00
1500.00
1750.00
2000.00
^ 2250.00
2500.00
3000.00
4000.00
5000.00
' 10000.00
15000.00
20000.00
50.03
37.74
23.72
12.04
7.38
4.94
3.60
2.78
2.22
1.78
1.50
1.25
0.85
0.61
0.47
0.38
0.30
0.26
0.19
0.12
0.08
0.03
0.01
0.01
Concentration (ppm) Distance to (m)
LOC 1960.0000 less than 25.00
IDLH 2442.0000 less than 25.00
Volume VH External Review Draft
Appendix VH-4 Do Not cite or Quote
-------
From Slab output file:
Scenario:
Accident Location:
Duration:
Meteorology:
Chemical:
Vapor phase mole fraction:
LOG:
IDLH:
*Output adjusted to be distance from
X,m
25.00
50.00
100.00
200.00
300.00
400.00
500.00
600.00
700.00
800.00
900.00
1000.00
1250.00
1500.00
1750.00
2000.00
2250.00
2500.00
3000.00
4000.00
5000.00
10000.00
15000.00
X,m
25.00
50.00
100.00
200.00
300.00
400.00
500.00
600.00
700.00
800.00
900.00
1000.00
1250.00
1500.00
1750.00
2000.00
2250.00
2500.00
3000.00
4000.00
5000.00
10000.00
15000.00
1
6.56
4.51
2.53
1.14
0.66
0.42
0.30
0.22
0.17
0.14
0.11
0.09
0.07
0.05
0.04
0.03
0.02
0.02
0.01
0.01
0.01
0.00
0.00
28
75.63
57.59
36.61
18.97
11.78
7.97
5.85
4.56
3.65
2.94
2.48
09
48
10
0.86
0.70
0.57
0.49
0.37
0.23
0.16
0.06
0.03
2,
1,
1,
*•* — —
e from
2
16.01
11.33
6.52
3.01
1.75
1.13
0.80
0.61
0.48
0.38
0.32
0.26
0.18
0.13
0.10
0.08
0.07
0.06
0.04
0.03
0.02
0.01
0.00
29
202.78
159.89
107.58
60.17
39.37
27.93
21.08
16.77
13.70
11.27
9.64
8.24
5.99
4.54
3.63
2.99
2.47
2.13
1.62
1.03
0.74
0.27
0.15
RUN09 . OUT
CONSERV
ON-SITE
UNMITIG
WORST
ACETONE
0.273
1960.000
2442.000
fenceline.
3
45.91
33.40
20.06
9.67
5.74
3.78
2.71
2.07
1.63
1.30
1.09
0.91
0.63
0.46
0.36
0.29
0.23
0.20
0.15
0.09
0.06
0.02
0.01
30
5.75
4.04
2.32 "
1.06
0.62
0.40
0.28
0.22
0.17
0.13
0.11
0.09
0.07
0.05
O.D4
0.03
0.02
0.02
0.02
0.01
0.01
0.00
0.00
4
93.55
69.24
42.40
21.04
12.78
8.52
6.18
4.78
3.80
3.04
2.56
2.15
1.51
1.11
0.87
0.70
0.57
0.49
0.36
0.22
0.16
0.05
0.03
31
15.88
11.51
6.85
3.27
1.94
1.27
0.91
0.70
0.55
0.44
0.37
0.31
0.22
0.16
0.12
0.10
0.08
0.07
0.05
0.03
0.02
0.01
0.00
5
157.28
117.73
74.44
39.24
24.98
17.28
12.90
10.19
8.25
6.73
5.72
4.86
3.50
2.63
2.08
1.71
1.40
1.20
0.91
0.57
0.40
0.14
0.08
32
32.37
23.95
14.65
7.24
4.38
.90
.10
2
2
1,
62
1.29
1.03
0.86
0.72
0.51
0.38
0.29
0.24
0.19
0.17
0.12
0.08
0.05
0.02
0.01
Volume VH
Appendix VE-4
External Review Draft
Do Not Cite or Quote
-------
6
237.90
184.. 48
125.59
74.71
51.92
38.86
30.80
25.54
21.59
18.35
16.08
14.11
10.76
8.46
6.96
5.87
4.96
4.35
3.40
2.25
1.65
0.63
0.36
33
65.64
49.88
31.73
16.37
10.14
6.85
5.02
3.91
3.13
2.52
2.13
1.80
1.27
0.94
0.74
0.61
0.49
0.42
0.32
0.20
0.14
0.05
0.03
7
4.86
3.37
1.91
0.86
0.49
0.32
0.22
0.17
0.13
0.10
0.09
0.07
0.05
0.04
0.03
0.02
0.02
0.02
0.01
0.01
0.00
0.00
0.00
34
181.74
143.91
97.15
54.36
35.56
24.97
18.82
14.95
12.18
10.00
8.53
7.28
5.28
3.98
3.18
2.61
2.15
1.86
1.41
0.90
0.64
0.23
0.13
8
11.74
8.26
4.75
2.19
1.27
0.82
0.58
0.44
0.35
0.28
0.23
0.19
0.13
0.10
0.08
0.06
0.05
0.04
0.03
0.02
0.01
0.00
0.00
35
5.10
3.59
2.06
0.94
0.55
0.35
0.25
0.19
0.15
0.12
0.10
0.08
0.06
0.04
0.03
0.03
0.02
0.02
0.01
0.01
0.01
0.00
0.00
9
33.10
24.15
14.49
6.97
4.15
2.72
1.95
1.50
1.18
0.94
0.79
0.66
0.46
0.33
0.26
0.21
0.17
0.14
0.11
0.07
0.05
0.02
0.01
36
14.08
10.21
6.08
2.91
1.72
1.12
0.81
0.62
0.49
0.39
0.33
0.27
0.19
0.14
0.11
0.09
0.07
0.06
0.05
0.03
0.02
0.01
0.00
10
69.07
51.30
31.79
15.79
9.56
6.36
4.61
3.54
2.61
2.25
1.89
1.58
1.11
0.81
0.64
0.51
0.41
0.35
0.26
0.16
0.11
0.04
0.02
37
28.59
21.18
12.96
6.37
3.85
2.55
1.85
1.43
1.13
0.91
0.76
0.64
0.45
0.33
0.26
0.21
0.17
0.15
0.11
0.07
0.05
0.02
0.01
.00
.58
.29
.05
11
132.22
100.05
63.68
33.13
20.70
14.13
10.42
8.13
6.53
5.30
4.48
3.79
2.70
2
1
1
1,
0.90
0.67
0.42
0.30
0.10
0.06
38
58.11
44.10
27.97
14.37
8.90
6.00
4.41
3.43
2.75
2.21
1.87
1.57
1.12
0.83
0.65
0.53
0.43
0.37
0.28
0.17
0.12
0.04
0.02
Volume Vn
Appendix VII-4
External Review Draft
Do Not Cite or Quote
-------
7,
5
12
246.28
189.49
126.77
73.03
49.81
36.41
28.34
23.15
19.33
16.25
14.09
12.24
9.18
.12
.80
4.83
4.03
3.52
2.73
1.77
1.28
0.48
0.27
39
4.60
3.23
1.85
0.85
0.49
0.32
0.23
0.17
0.14
0.11
0.09
0.07
0.05
0.04
0.03
0.02
0.02
0.02
0.01
0.01
0.01
0.00
0.00
13
3.88
2.70
1.53
0.69
0.39
0.25
0.18
0.13
0.10
0.08
0.07
0.06
0.04
0.03
0.02
0.02
0.01
0.01
0.01
. 0.01
0.00
0.00
0.00
40
12.65
9.17
5.46
2.60
1
1
54
01
0.72
0.56
0.44
0.35
0.29
0.24
0.17
0.13
0.10
0.08
0.06
0.05
0.04
0.03
0.02
0.01
0.00
14
9.28
6.55
3.75
1.72
1.00
0.65
0.46
0.35
0.27
0.22
0.18
0.15
0.11
0.08
0.06
0.05
0.04
0.03
0.02
0.01
0.01
0.00
0.00
41
25.65
18.98
11.61
5.72
3.45
2.29
1.65
1.27
1.01
0.81
0.68
0.57
0.40
0.30
0.23
0.19
0.15
0.13
0.10
0.06
0.04
0.01
0.01
15
25.97
18.88
11.29
5.42
3.23
2.11
1.52
1.16
0.92
0.73
0.61
0.51
0.36
0.26
0.20
0.16
0.13
0.11
0.08
0.05
0.04
0.01
0.01
42
52.13
39.42
25.01
12.82
7.93
5.34
,92
,05
1.
1.
1.
3,
3,
2.44
1.97
.66
.40
.00
0.74
0.58
0.47
0.39
0.33
0.25
0.16
0.11
0.04
0.02
16
53.74
39.99
24.61
12.25
7.42
4.93
3.56
2.75
2.18
1.75
1.47
1.23
0.86
0.63
0.49
0.40
0.32
0.28
0.21
0.13
0.09.
0.03
0.02
43
7.88
5.71
3.38
1.62
P.96
0.63
0.45
0.35
0.27
0.22
0.18
0.15
0.11
0.08
0.06
0.05
0.04
0.03
0.03
0.02
0.01
0.00
0.00
17
107.32
81.83
52.31
27.09
16.92
11.48
8.44
6.57
5.27
,26
,59
,03
.14
.59
4.
3.
3,
2,
1.
1.
1,
25
,02
0.83
0.71
0.53
0.33
0.23
0.08
0.05
44
15.92
11.78
7.17
3.52
2.12
1.41
1.02
0.79
0.62
0.50
0.42
0.35
0.25
0.18
0.14
0.12
0.09
0.08
0.06
0.04
0.03
0.01
0.01
Volume VII
Appendix VH-4
External Review Draft
Do Not Cite or Quote
-------
18
241.47
186.98
124.64
70.26
46.80
33.68
25.93
20.92
17.28
14.37
12.38
10.67
7.89
6.06
4.89
4.05
3.36
2.92
2.24
1.44
1.03
0.38
0.21
45
6.31
4.56
2.71
1.29
0.77
0.50
0.36
0.28
0.22
0.17
0.15
0.12
0.09
0.06
0.05
0.04
0.03
0.03
0.02
0.01
0.01
0.00
0.00
19
3.23
2.25
1.27
0.57
0.33
0.21
0.15
0.11
0.09
0.07
0.06
0.05
0.03
0.02
0.02
0.01
0.01
0.01
0.01
0.00
0.00
0.00
0.00
46
12.73
9.41
5.73
2.81
1.70
1.12
0.81
0.63
0.50
0.40
0.34
0.28
0.20
0.15
0.11
0.09
0.08
0.06
0.05
0.03
0.02
0.01
0.00
20
7.70
5.42
3.10
1.43
0.83
0.53
0.38
0.29
0.23
0.18
0.15
0.13
0.09
0.06
0.05
0.04
0.03
0.03
0.02
0.01
0.01
0.00
0.00
47
8.46
6.26
3.81
1.87
1.13
0.75
0.54
0.42
0.33
0.27
0.22
0.19
0.13
0.10
0.08
0.06
0.05
0.04
0.03
0.02
0.01
0.00
0.00
21
21.40
15.54
9.27
4.43
2.64
1.73
1.24
0.95
0.75
0.60
0.50
0.42
0.29
0.21
0.17
0.13
0.11
0.09
0.07
0.04
0.03
0.01
0.01
48
6.34
4.69
2.86
1.40
0.85
0.56
0.41
0.31
0.25
0.20
0.17
0.14
0.10
0.07
0.06 *
0.05
0.04
0.03
0.02
0.01
0.01
0.00
0.00
22
43.97
32.55
20.05
9.94
6.02
4.00
2.90
2.23
1.77
1.42
1.19
1.00
0.70
0.51
0.40
0.33
0.26
0.23
0.17
0.10
0.07
0.03
0.01
49
10.24
7.05
3.94
1.76
1.00
0.64
0.45
0.34
0.26
0.21
0.17
0.14
0.10
0.07
0.06
0.04
0.04
0.03
0.02
0.01
0.01
0.00
0.00
1,
1,
' 23
88.86
67.78
43.31
22.47
13.97
9.48
6.95
5.41
4.33
3.49
2.94
2.48
1.76
,30
,03
0.83
0.68
0.58
0.43
0.27
0.19
0.07
0.04
50
25.10
17.77
10.27
4.73
2.75
1.78
1.26
0.96
0.75
0.60
0.50
0.41
0.28
0.21
0.16
0.13
0.10
0.09
0.07
0.04
0.03
0.01
0.01
Volume VII
Appendix VII-4
External Review Draft
Do Not Cite or Quote
-------
1
1
24
224.61
175.63
117.46
65.97
43.39
30.94
23.47
18.78
15.41
12.74
10.91
9.35
6.85
5.23
4.18
3.45
2.85
2.47
89
.20
0.86
0.32
0.18
51
70.82
50.28
29.67
14.18
8.48
5.59
4.03
3.12
2.47
1.97
1.65
1.38
0.97
0.71
0.56
0.45
0.36
0.31
0.23
0.14
0.10
0.03
0.02
25
6,59
4.64
2.65
1.22
0.71
0.46
0.33
0.25
0.19
0.15
0.13
0.11
0.07
0.05
0.04
0.03
0.03
0.02
0.02
0.01
0.01
0.00
0.00
52
120.70
88.04
54.04
27.59
17.12
11.67
8.60
6.73
5.42
4.39
3.71
3.13
2.23
1.66
1.31
1.07
0.87
0.74
0.56
0.35
0.24
0.08
6.05
0
0
26
18.23
13.22
7.87
3.77
2.23
1.46
1.05
0.81
0.64
0.51
0.42
0.35
0.25
0.18
0.14
.11
.09
0.08
0.06
0.04
0.03
0.01
0.00
53
166.17
125.14
81.11
44.85
29.57
21.16
16.16
12.99
10.69
8.87
7.62
6.55
4.81
3.66
2.94
2.43
2.01
1.74
1.33
0.85
0.61
0.22
0.12
27
37.32
27.59
16.93
8.37
5.07
3.37
2.43
1.87
1.49
1.19
1.00
0.84
0.59
0.43
0.34
0.28
0.22
0.19
0.14
0.09
0.06
0.02
0.01
54
278.61
212.12
140.44
82.88
57.52
43.49
34.75
28.81
24.42
20.94
18.52
16.39
12.72
10.21
8.42V
7.20
6.23
5.40
4.29
2.99
2.22
0.89
0.52
y°lumeVI1
Appendix VH-4
External Review Draft
Do Not Cite or Quote
-------
X,m Max concentration, ppm
25.00
50.00
100.00
200.00
300.00
400.00
500.00
600.00
700.00
800.00
900.00
1000.00
1250.00
1500.00
1750.00
2000.00
2250.00
2500.00
3000.00
4000.00
5000.00
10000.00
15000.00
278.61
212.12
140.44 '
82.88
57.52
43.49
34.75
28.81
24.42
20.94
18.52
16.39
12.72
10.21
8.42
7.20
6.23
5.40
4.29
2.99
2.22
0.89
0.52
Concentration (ppm)
1960.0000
2442.0000
Distance to (m)
less than
less than
25.00
25.00
Volume YE
Appendix VII-4
External Review Draft
Do Not Cite or Quote
-------
From Slab output file:
Scenario:
Accident Location:
Duration:
Meteorology:
Chemical:
Vapor phase mole fraction:
LOG:
IDLH:
*Output adjusted to be distance from
X,m
25.00
50.00
100.00
200.00
300.00
400.00
500.00
600.00
700.00
800.00
900.00
.1000.00
1250.00
1500.00
1750.00
2000.00
2250.00
2500.00
3000.00
4000.00
5000.00
10000.00
15000.00
20000.00
X,m
25.00
50.00
100.00
200.00
300.00
400.00
500.00
600.00
700.00
800.00
900.00
1000.00
1250.00
1500.00
1750.00
2000.00
2250.00
2500.00
3000.00
4000.00
5000.00
10000.00
15000.00
20000.00
1
8.56
5.98
3.36
1.51
0.88
0.56
0.40
0.30
0.23
0.18
0.15
0.12
0.08
0.06
0.05
0.04
0.03
0.02
0.02
0.01
0.01
0.00
0.00
0.00
28
90.23
69.65
45.28
24.07
15.19
10.39
7.68
6.01
4.83
90
25
67
81
33
04
82
0.68
0.56
0.41
0.26
0.18
0.06
0.03
0.02
3.
3,
2.
1,
1.
1.
0.
— ~ - - _ -
:e from
2
20.32
14.56
8.51
3.99
2.34
1.52
1.08
0.81
0.63
0.49
0.41
0.33
0.22
0.16
0.13
0.10
0.08
0.07
0.05
0.03
0.02
0.01
0.00
0.00
29
217.33
171.03
116.01
66.22
44.12
31.74
24.42
18.84
14.99
11.96
10.28
8.64
6.21
4.72
3.65
3.01
2.47
2.13
1.58
1.00
0.69
0.21
0.11
0.06
RDN10.OUT
CONSERV
ON-SITE
MITIGAT
WORST
ACETONE
0.585
1960.000
2442.000
fenceline.
3
55.10
40.45
24.59
12.08
7.28
4.82
3.38
2.56
1.99
1.56
1.31
1.07
0.74
0.55
0.42
0.33
0.27
0.22
0.17
0.10
0.07
0.02
0.01
0.01
30
7.33
5.23
3.04
1.41
0.83
0.54
0.38
0.29
0.23
0.18
0.15
0.13
0.09
0.06
0.05
0.04
0.03
0.03
0.02
0.01
0.01
0.00
0.00
0.00
4
104.37
76.86
47.63
24.21
15.00
9.79
7.02
5.38
4.21
3.40
2.84
2.40
1.68
1.24
0.93
0.76
0.62
0.52
0.38
0.23
0.16
0.05
0.02
0.01
31
19.70
14.49
8.79
4.30
2.58
1.70
1.22
0.94
0.75
0.59
0.50
0.42
0.29
0.21
0.16
0.13
0.10
0.09
0.06
0.04
0.03
0.01
0.00
0.00
4
3
2
2
5
156.74
117.56
75.28
40.73
24.82
17.14
12.86
10.02
7.98
6.71
5.57
83
44
60
08
1.63
1.39
1.14
0.87
0.53
0.36
0.10
0.05
0.03
32
39.53
29.77
18.67
9.45
5.78
3.87
2.81
2.18
1.74
1.39
1.17
0.98
0.69
0.49
0.38
0.30
0.24
0.21
0.15
0.09
0.06
0.02
0.01
0.01
Volume VII
Appendix VII-4
External Review Draft
Do Not Cite or Quote
-------
6
234.74
182*75
115.60
64.10
44.42
33.63
26.77
21.79
18.79
15.88
14.12
12.35
9.43
7.44
5.95
5.00
4.13
3.54
2.59
1.62
1.08
0.30
0.14
0.08
33
78.72
60.79
39.52
20.97
13.19
9.04
6.68
5.21
4.19
3.39
2.86
2.40
1.63
1.18
0.92
0.73
0.59
0.50
0.36
0.23
0.16
0.05
0.03
0.02
0,
0,
7
6.36
4.41
2.51
1.14
0.66
0.42
0.30
0.23
0.18
,14
,11
0.09
0.06
0.04
0.03
0.03
0.02
0.02
0.01
0.01
' 0.01
0.00
0.00
0.00
34
200.48
159.18
108.61
62.23
41.27
29.51
22.54
18.12
14.55
11.51
9.77
8.07
5.69
4.35
3.39
2.71
2.26
1.90
1.43
0.90
0.63
0.20
0.10
0.06
8
15.01
10.71
6.25
2.92
1.71
1.11
0.79
0.60
0.47
0.38
0.31
0.25
0.17
0.12
0.10
0.08
0.06
0.05
0.04
0.02
0.02
0.01
0.00
0.00
35
6.52
4.64
2.70
1.26
0.73
0.48
0.34
0.26
0.20
0.16
0.14
0.11
0.08
0.06
0.04
0.04
0.03
0.02
0.02
0.01
0.01
0.00
0.00
0.00
2
2
9
40.76
30.09
18.42
9.05
5.46
3.61
.60
,00
1.57
1.22
1.01
0.83
0.57
0.41
0.32
0.25
0.21
0.17
0.12
0.08
0.05
0.02
0.01
0.01
36
17.46
12.89
7.79
3.80
2.28
1.50
1.08
0.83
0.66
0.53
0.44
0.37
0.26
0.19
0.15
0.12
0.09
0.08
0.06
0.04
0.02
0.01
0.00
0.00
10
82.17
61.46
38.53
19.58
12.03
8.10
5.91
4.46
3.47
2.71
2.30
1.88
1.29
0.96
0.74
0.58
0.48
0.39
0.29
0.18
0.12
0.04
0.02
0.01
37
34.98
26.35
16.50
8.32
5.09
3.41
2.48
1.92
1.53
.22
.03
0.87
0.61
0.45
0.34
0.27
0.22
0.19
0.14
0.08
0.06
0.02
0.01
0.01
1,
1,
11
143.85
109.24
69.75
37.24
23.81
15.79
11.48
8.87
6.98
5.71
4.76
4.07
2.86
2.13
1.63
1.34
1.08
0.93
0.67
0.42
0.29
0.09
0.04
0.03
38
70.00
53.89
34.99
18.54
11.66
7.92
5.87
4.59
3.68
2.98
2.52
2.13
1.51
1.08
0.84
0.67
0.53
0.45
0.33
0.21
0.14
0.05
0.02
0.02
Volume VII
Appendix VII-4
External Review Draft
Do Not Cite or Quote
-------
12
230.43
178.20
120.69
66.17
43.87
32.26
25.18
20.09
17.15
14.38
12.69
10.99
8.25
6.47
5.13
4.33
3.56
3.08
2.26
1.41
0.96
0.29
0.13
0.07
39
5.87
4.17
2.42
1.13
0.66
0.43
0.31
0.23
0.18
0.15
0.12
0.10
0.07
0.05
0.04
0.03
0.03
0.02
0.02
0.01
0.01
0.00
0.00
0.00
13
5.05
3.54
2.02
0.91
0.53
0.34
0.24
0.18
0.14
0.11
0.09
0.08
0.05
0.04
0.03
0.02
0.02
0.02
0.01
0.01
0.00
0.00
0.00
0.00
40
15.71
11.53
7.03
3.41
2.05
1.35
0.97
0.75
0.59
0.47
0.40
0.33
0.23
0.17
0.13
0.11
0.09
0.07
0.05
0.03
0.02
0.01
0.00
0.00
14
11.88
8.47
4.93
2.30
1.35
0.88
0.62
0.47
0.37
0.30
0.25
0.21
0.14
0.10
0.08
0.06
0.05
0.04
0.03
0.02
0.01
0.00
0.00
0.00
41
31.38
23.63
14.76
7.43
4.55
3.05
2.22
1.71
1.36
1.09
0.92
0.77
0.55
0.40
0.32
0.25
0.20
0.17
0.12
0.08
0.05
0.02
0.01
0.01
15
32.14
23.71
14.49
7.13
4.28
2.82
2.04
1.57
1.24
0.99
0.81
0.67
0.46
0.33
0.26
0.20
0.16
0.14
0.10
0.06
0.04
0.01
0.01
0.00
42
62.71
48.39
31.38
16.57
10.41
7.10
5.23
4.09
3.28
2.65
2.24
1.90
1.35
1.00
0.76
0.61
0.49
0.42
0.30
0.19
0.13
0.04
0.02
0.01
16
64.86
49.08
30.89
15.70
9.68
6.46
4.72
3.65
2.87
2.24
1.88
1.54
1.05
0.77
0.60
0.47
0.39
0.32
0.23
0.14
0.10
0.03
0.02
0.01
43
9.75
7.21
4.36
2.12
1.27
0.83
0.60
0.46
0.37
29
25
0
0
0.21
0.14
0.11
0.08
0.07
0.05
0.05
0.03
0.02
0.01
0.00
0.00
0.00
17
123.22
94.45
61.15
32.54
20.62
14.20
10.57
8.05
6.31
4.94
4.17
3.40
2.41
1.81
1.39
1.10
0.92
0.77
0.57
0.35
0.24
0.08
0.04
0.02
44
19.47
14.65
9.13
4.60
2.80
1.87
1.36
1.05
0.84
0.67
0.57
0.48
0.34
0.25
0.20
0.16
0.13
0.11
0.08
0.05
0.03
0.01
0.01
0.00
Volume VH
Appendix VH-4
ReV1CW Draft
Do Not Cite or Quote
-------
3
3
2
2
18
235.70
182.34
122.25
70.85
46.26
32.22
24.63
19.63
15.77
13.59
11.43
10.07
7.34
5.66
4.60
.66
.16
.66
,03
1.27
0.87
0.26
0.12
0.07
45
7.82
5.75
3.48
1.69
1.01
0.67
0.48
0.37
0.29
0.23
0.20
0.16
0.11
0.08
0.07
0.05
0.04
0.04
0.03
0.02
0.01
0.00
0.00
0.00
19
4.21
2.95
1.68
0.76
0.44
0.28
0.20
0.15
0.12
0.09
0.08
0.06
0.04
0.03
0.02
0.02
0.01
0.01
0.01
0.01
0.00
0.00
0.00
0.00
46
15.56
11.70
7.31
3.67
2.23
1.49
1.09
0.84
0.67
0.54
0.45
0.38
0.27
0.20
0.16
0.13
0.10
0.09
0.07
0.04
0.03
0.01
0.00
0.00
20
9.83
6.99
4.08
1.90
1.11
0.72
0.51
0.39
0.31
0.25
0.20
0.17
0.12
0.08
0.06
0.05
0.04
0.04
0.03
0.02
0.01
0.00
0.00
0.00
47
10.33
7,
4
80
,85
2.44
1.49
0.99
0.72
0.56
0.44
0.36
0.30
0.25
0.18
0.13
0.10
0.-08
0.07
0.06
0.04
0.03
0.02
0.01
0.00
0.00
1.
1.
21
26.51
19.57
11.91
5.84
3.50
2.31
1.67
.28
.01
0.81
0.68
0.57
0.38
0.28
0.21
0.17
0.14
0.12
0.08
0.05
0.04
0.01
0.01
0.00
48
7.74
5.83
3.64
1.83
1.11
0.75
0.54
0.42
0.33
0.27
0.23
0.19
0.13
0.10'
0.08
0.06
0.05
0.04
0.03
0.02
0.01
0.01
0.00
0.00
22
53.54
40.40
25.41
12.94
7.91
5.31
3.87
2.99
2.39
1.92
1.61
1.35
0.91
0.65
0.51
0.40
0.33
0.27
0.20
0.12
0.08
0.03
0.01
0.01
49
13.27
9.24
5.22
2.35
1.35
0.84
0.59
0.44
0.34
0.26
0.22
0.18
0.12
0.09
0.07
0.05
0.04
0.03
0.03
0.02
0.01
0.00
0.00
0.00
23
104.61
80.85
52.49
27.97
17.67
12.09
8.98
7.03
5.55
4.35
3.64
2.99
2.05
1.53
1.19
0.93
0.78
0.64
0.48
0.29
0.20
0.06
0.03
0.02
50
30.47
21.78
12.74
6.00
3.47
2.21
1.56
1.17
0.90
0.72
0.59
0.50
0.34
0.25
0.19
0.15
0.12
0.10
0.07
0.04
0.03
0.01
0.00
0.00
Volume VU
Appendix VH-4
External Review Draft
Do Not Cite or Quote
-------
24
230.94
179.93
120.95
69.11
46.54
33.79
24.75
19.39
15.56
12.81
10.89
9.31
6.76
5.16
4.05
3.37
2.76
2.37
1.74
1.11
0.75
0.23
0.11
0.07
51
77.25
54.65
32.37
15.86
9.26
6.13
4.44
3.39
2.62
2.18
1.77
1.53
1.06
0.78
0.59
0.48
0.39
0.33
0.24
0.15
0.10
0.03
0.01
0.01
25
8.39
5.98
3.48
1.62
0.95
0.62
0.44
0.33
0.26
0.21
0.17
0.15
0.10
0.07
0.06
0.05
0.04
0.03
0.02
0.01
0.01
0.00
0.00
0.00
52
119.46
88.08
55.08
26.48
16.70
11.62
8.62
6.61
5.42
4.39
3.74
3.10
2.23
1.70
1.31
1.06
0.87
0.73
0.54
0.32
0.22
0.06
0.03
0.02
26
22.60
16.67
10.11
4.95
2.97
1.96
1.41
1.08
0.86
0.69
0.57
0.48
0.34
0.24
0.19
0.15
0.12
0.10
0.07
0.05
0.03
0.01
0.01
0.00
53
169.69
128.01
77.24
40.78
26.67
19.35
14.99
11.90
9.81
8.25
7.10
6.08
4.42
3.44
2.70
2.19
1.81
1.52
1.12
0.68
0.45
0.12
0.05
0.03
27
45.46
34.26
21.54
10.91
6.68
4.48
3.26
2.52
2.01
1.62
1.36
1.14
0.80
0.57
0.44
0.35
0.28
0.24
0.17
0.11
0.07
0.02
0.01
0.01
54
282.55
205.93
130.71
73.27
49.88
37.77
30.36
25.32
21.15
18.48
15.84
14.18
10.64
8.26
6.78
5.46
4.64
3.83
2.90
1.74
1.17
0.31
0.14
0.08
Volume
. .. ^m „
Appendix VII-4
c . D . ^ ^
External Review Draft
~ XT „. _
Do Not Cite or Quote
-------
X,m Max concentration, ppm
25.00
50.00
100.00
200.00
300.00
400.00
500.00
600.00
700.00
800.00
900.00
1000,00
1250.00
1500.00
1750.00
2000.00
2250.00
2500.00
3000.00
.4000.00
5000.00
10000.00
15000.00
20000.00
282.55
205.93
130.71
73.27
49.88
37.77
30.36
25.32
21.15
18.48
15.84
14.18
10.64
8.26
6.78
5.46
4.64
3.83
2.90
1.74
1.17
0.31
0.14
0.08
ncentration (ppm)
SSESSSSSSSS^SSSSS!
IDLH
1960.0000
2442.0000
Distance to (m)
less than
less than
25.00
25.00
Volume YE
Appendix VII-4
External Review Draft
Do Not Cite or Quote
-------
From Slab output file: RUN11.OUT
Scenario: CONSERV
Accident Location: ON-SITE
Duration: UNMITIG
Meteorology:. _„ INVERSN
Chemical: ACETONE
Vapor phase mole fraction: 0.273
LOC: 1960.000
IDLH: 2442.000
*0utput adjusted to be distance from fenceline.
X,m Max concentration, ppm
25.00 526.75
50.00 407.31
100.00 270.25
200.00 158.44
300.00 107.11
400.00 80.44
500.00 63.86
600.00 51.43
700.00 43.67
800.00 36.79
900.00 32.37
1000.00 27.94
1250.00 21.45
1500.00 16.97
1750.00 13.59
2000.00 11.58
2250.00 9.70
2500.00 8.44
3000.00 6.35
4000.00 4.20
5000.00 2.95
10000.00 0.96
15000.00 0.48
20000.00 0.29
Concentration (ppm) Distance to (m)
LOC 1960.0000 less than 25.00
IDLH 2442.0000 less than 25.00
Volume VII External Review Draft
Appendix VH-4 Do Not Cite or Quote
-------
From Slab output file:
Scenario:
^i-x Accident Location:
Duration:
vjJLJ_y Meteorology:
Chemical:
Vapor phase mole fraction:
LOG:
• IDLH:
RUNA1.OUT
CONSERV
ON-SITE
UNMITIG
INVERSN
ACETONE
0.273
1960.000
2442.000
*Output adjusted to be distance from fenceline.
X,m Max concentration, ppm
25.00
50.00
100.00
200.00
300.00
' 400.00
500.00
600.00
700.00
800.00
900.00
1000.00
1250.00
1500.00
--s, 1750.00
2000.00
_/ 2250.00
2500.00
3000.00
4000.00
5000.00
10000.00
15000.00
20000.00
163.47
136.60
103.94
72.23
56.22
46.50
39.85
34.91
30.98
28.03
25.66
23.48
19.54
16.73
14.62
13.01
11.64
10.52
8.85
6.65
5.35
2.36
1.31
0.83
Concentration (ppm)
LOC
IDLH
1960.0000
2442.0000
Distance to (m)
less than
less than
25.00
25.00
Volume VII
Appendix VII-4
External Review Draft
Do Not Cite or Quote
-------
From Slab output file: RUN12.OUT
Scenario: CONSERV
Accident Location: ON-SITE
Duration: MITIGAT
Meteorology: —-__ INVERSN
Chemical: ACETONE
Vapor phase mole fraction: 0.585
LOG: 1960.000
IDLH: 2442.000
*0utput adjusted to be distance from fenceline.
X,m Max concentration, ppm
25.00 1206.67
50.00 951.72
100.00 678.83
200.00 423.89
300.00 305.44
400.00 236.16
500.00 192.42
600.00 160.65
700.00 135.25
800.00 117.15
900.00 101.72
1000.00 89.64
1250.00 67.85
1500.00 53.05
1750.00 • 42.01
2000.00 34.52
2250.00 28.84
2500.00 24.25
3000.00 17.97
4000.00 10.75
5000.00 7.21
- Concentration (ppm) Distance to (m)
LOC 1960.0000 less than 25.00
IDLH 2442.0000 less than 25.00
Volume VH External Review Draft
Appendix VH-4 Do Not Cite or Quote
-------
From Slab output file:
Scenario:
; Accident Location:
Duration:
Meteorology:
Chemical:
Vapor phase mole fraction:
LOG:
IDLH:
RDN13.ODT
TYPICAL
ON-SITE
UNMITIG
TYPICAL
FORMALDEHYDE
0.482
9.600
19.600
*Output adjusted to be distance from fenceline.
X,m Max concentration/ ppm
25.00
50.00
100.00
200.00
300.00
400.00
500.00
600.00
700.00
- 800.00
900.00
1000.00
1250.00
1500.00
1750.00
2000.00
2250.00
^ 2500.00
3000.00
4000.00
5000.00
24.22
16.68
9.66
4.35
2.59
1.69
1.21
0.92
0.72
0.57
0.48
0.40
0.28
0.20
0.16
0.12
0.10
0.08
0.06
0.04
0.03
Concentration (ppm)
LOG
IDLH
9.6000
19.6000
Distance to (m)
101.04
40.32
Volume VII
Appendix VII-4
External Review Draft
Do Not Cite or Quote
-------
From Slab output file:
Scenario:
Accident Location:
Duration:
Meteorology:
Chemical:
Vapor phase mole fraction:
LOG:
IDLH:
RUN14 . OUT
TYPICAL
ON-SITE
MITIG
TYPICAL
FORMALDEHYDE
0.512
9.600
19.600
*Output adjusted to be distance from fenceline.
X,m Max concentration, ppm
25.00
50.00
100.00
200.00
300.00
400.00
500.00
'600.00
700.00
800.00
900.00
1000.00
1250.00
1500.00
1750.00
2000.00
2250.00
2500.00
3000.00
4000.00
5000.00-
24
16
9
4
2
1
1
0
0
0
0
0
0
0
0
0
0
0
0
0
0
.65
.98
.84
.43
.65
.73
.24
.94
.74
.58
.49
.41
.28
.20
.16
.12
.10
.08
.06
.04
.03
Concentration (ppm)
Distance to (m)
LOC
IDLH
9.6000
19.6000
104.49
41.46
Volume VH
Appendix VII-4
External Review Draft
Do Not Cite or Quote
-------
\
From Slab output file:
Scenario:
Accident Location:
Duration:
Meteorology:
Chemical:
Vapor phase mole fraction:
LOG:
IDLH:
*Output adjusted to be distance from
X,m
25.00
50.00
100.00
200.00
300.00
400.00
500.00
600.00
700.00
800.00
900.00
1000.00
1250.00
1500.00
1750.00
2000.00
2250.00
2500.00
3000.00
4000.00
X,m
25.00
50.00
100.00
200.00
300.00
400.00
500.00
600.00
700.00
800.00
900.00
1000.00
1250.00
1500.00
1750.00
2000.00
2250.00
2500.00
3000.00
4000.00
1
3.78
2.47
1.34
0.56
0.32
0.20
0.14
0.10
0.08
0.06
0.05
0.04
0.03
0.02
0.02
0.01
0.01
0.01
0.01
0.00
28
46.43
32.57
19.30
8.96
5.44
3.60
2.61
2.00
1.58
1.26
1.07
0.89
0.60
0.43
0.34
0.27
0.22
0.18
0.13
0.08
RON15.OBT
TYPICAL
ON-SITE
UNMITIG
WORST
FORMALDEHYDE
0.482
9.600
19.600
fenceline.
3 45
25.48 53.76 109.91
17.25 37.21 77.76
9.82 21.64 4.6.56
4.31 9.73 21.90
2.53 5.79 13.00
1.64 3.77 8.22
1.16 2.62 5.77
0.86 1.94 4.28
0.66 1.48 3.23
0.51 1.17 2.67
0.43 0.96 2.12
0.35 0.80 1.83
0.23 0.54 1.25
0.17 0.40 0.90
0.13 0.30 0.71
0.10 0.24 0.56
0.09 0.20 0.46
0.07 0.16 0.38
0.05 0.12 0.27
0.03 0.07 0.17
30 31 32
3.41 9.33 19.30
2.26 6.31 13.26
1.25 3.58 7.68
0.53 1.57 3.46
0.31 0.92 2.06
0.19 - 0.60 1.35
0.14 0.43 0.97
0.10 0.32 0.73
0.08 0.25 0.58
0.06 0.20 0.46
0.05 0.17 0.39
0.04 0.14 0.32
0.03 0.10 0.22
0.02 0.07 0.16
1.27 0.02 0.06 0.13
1.00 0.01 0.04 0.10
0.83 0.01 0.03 0.08
0.70 0.01 0.03 0.07
0.52 0.01 0.02 0.05
0.32 0.00 0.01 0.03
2
9.11
6.03
3.34
1.41
0.82
0.52
0.36
0.27
0.20
0.16
0.13
0.11
0.07
0.05
0.04
0.03
0.03
0.02
0.02
0.01
29
143.87
104.75
65.22
32.22
20.17
13.68
10.07
7.81
6.14
4.74
.97
.24
2.20
1.65
3,
3
Volume VII
Appendix VII-4
External Review Draft
Do Not Cite or Quote
-------
6
245.18
183.81
119.82
57.32
35.12
24.01
17.36
13.62
10.82
8.81
7.33
6.31
4.41
3.19
2.51
1.98
1.63
1.31
0.96
0.56
33
40.47
28.35
16.79
7.81
4.74
3.14
2.27
1.74
1.38
1.10
0.93
0.77
0.55
0.39
0.30
0.24
0.19
0.16
0.12
0.07
7
2.83
1.85
1.01
0.42
0.24
0.15
0.11
0.08
0.06
0.05
0.04
0.03
0.02
0.02
0.01
0.01
0.01
0.01
0.00
0.00
34
125.85
91.42
56.64
27.95
17.51
11.85
8.73
6.78
5.40
4.35
3.64
2.94
1.99
1.48
1.15
0.89
0.75
0.61
0.46
0.28
8
6.82
4.53
2.51
1.06
0.61
0.39
0.27
0.20
0.16
0.12
0.10
0.08
0.06
0.04
0.03
0.02
0.02
0.02
0.01
0.01
35
3.03
2.01
1.11
0.47
0.27
0.17
0.12
0.09
0.07
0.05
0.05
0.04
0.03
0.02
0.01
0.01
0.01
0.01
0.01
0.00
9
18.81
12.73
7.23
3.18
1.87
1.21
0.86
0.65
0.50
0.39
0.32
0;26
0.18
0.13
0.10
0.08
0.07
0.05
0.04
0.02
36
8.31
5.62
3.18
1.39
0.82
0.53
0.38
0.29
0.22
0.18
0.15
0.12
0.09
0.06
0.05
0.04
0.03
0.03*
0.02
0.01
0
0
10
39.64
27.30
15.84
7.14
4.24
2.76
1.98
1.50
1.17
0.90
0.75
0.61
0.41
0.30
0.23
18
15
0.12
0.09
0.06
37
17.11
11.77
6.80
3.07
1.83
1.20
0.86
0.65
0.51
0.41
0.34
0.28
0.20
0.15
0.12
0.09
0.07
0.06
0.05
0.03
11
83.41
58.93
35.06
16.34
9.88
6.55
4.57
3.39
2.59
2.06
1.69
1.41
0.97
0.72
0.54
0.44
0.35
0.30
0.22
0.13
38
35.86
25.13
14.88
6.90
4.19
2.78
2.01
1.54
1.22
0.97
0.82
0.69
0.49
0.36
0.28
0.22
0.18
0.15
0.11
0.07
Volume VH
A j- tm .
Appendix VII-4
_ . _ . ^
External Review Draft
~ . , „.
Do Not Cite or Quote
-------
12
223.21
164.37
104.81
53.70
32.95
21.29
15.24
11.43
8.82
7.30
5.99
5.08
3.48
2.58
2.03
1.57
1.33
1.10
0.81
0.49
39
2.73
1.81
1.00
0.42
0.24
0.16
0.11
0.08
0.06
0.05
0.04
0.03
0.02
0.02
0.01
0.01
0.01
0.01
0.01
0.00
13
2.27
1.48
0.80
0.33
0.19
0.12
0.08
0.06
0.05
0.04
0.03
0.03
0.02
0.01
0.01
0.01
0.01
0.01
0.00
0.00
40
7.47
5.07
2.86
1.26
0.74
0.48
0.34
0.26
0.20
0.16
0.13
0.11
0.08
0.06
0.04
0.04
0.03
0.02
0.02
0.01
3
2,
14
5.44
,62
.00
0.85
0.49
0.31
0.22
0.16
0.13
0.10
0.08
0.07
0.05
0.03
0.03
0.02
0.02
0.01
0.01
0.01
41
15.40
10.58
6.14
2.76
1.65
1.07
0.77
0.59
0.46
0.36
0.31
0.26
0.18
0.13
0.10
0.08
0.07
0.06
0.04
0.02
15
14.93
10.10
5.74
2.53
1.49
0.96
0.68
0.52
0.40
0.32
0.27
0.22
0.15
0.11
0.08
0.07
0.05
0.04
0.03
0.02
42
32.23
22.56
13.36
6.23
3.77
2.50
1.81
1.39
1.10
0.88
0.74
0.62
0.44
0.32
0,26
0.21
0.16
0.14'
0.10
0.06
16
31.28
21.55
12.49
5.61
3.35
2.18
1.56
1.19
0.93
0.74
0.62
0.50
0.34
0.25
0.19
0.15
0.12
0.10
0.07
0.05
43
4.66
3.15
1.79
0.79
0.46
0.30
0.21
0.16
0.13
0.10
0.08
0.07
0.05
0.04
0.03
0.02
0.02
0.02
0.01
0.01
17
66.10
46.44
27.63
12.84
7
5
.80
.13
3.72
2.85
2.22
1.71
1.43
1.16
0.80
0.59
0.45
0.35
0.30
0.24
0.18
0.11
44
9.60
6.60
3.82
1.72
1.03
0.67
0.48
0.37
0.29
0.23
0.19
0.16
0.11
0.08
0.06
0.05
0.04
0.04
0.03
0.02
V
Volume VH
Appendix VII-4
External Review Draft
Do Not Cite or Quote
-------
18
194.07
142.21
89.63
44.83
28.27
18.40
12.96
9.71
7.40
6.10
4.90
4.22
2.91
2.12
1.68
1.33
1.10
0.90
0.67
0.40
45
3.75
2.54
1.43
0.63
0.37
0.24
0.17
0.13
0.10
'0.08
0.07
0.06
0.04
0.03
0.02
0.02
0.01
0.01
0.01
0.01
19
1.89
1.23
0.67
0.28
0.16
0.10
0.07
0.05
0.04
0.03
0.03
0.02
0.01
0.01
0.01
0.01
0.01
0.00
0.00
0.00
46
7.67
5.26
3.05
1.38
0.82
0.53
0.38
0.29
0.23
0.18
0.15
0.13
0.09
0.07
0.05
0.04
0.03
0.03
0.02
0.01
20
4.54
3.02
1.67
0.71
0.41
0.26
0.18
0.14
0.11
0.08
0.07
0.06
0.04
0.03
0.02
0.02
0.01
0.01
0.01
0.01
47
5.12
3.52
2.03
0.92
0.55
0.36
0.26
0.20
0.15
0.12
0.10
0.09
0.06
0.04
0.03
0.03
0.02
0.02
0.01
0.01
21
12.45
8.41
4.77
2.10
1.23
0.80
0.57
0.43
0.34
0.26
0.22
0.18
0.13
0.09
0.07
0.06
0.04
0.04
0.03
0.02
48
3.84
2.64
1.53
0.69
0.41
0.27
0.19
0.15
0.11
0.09
0.08
0.06
0.04
0.03
0.03
0.02
0.02
0.01
0.01
0.01
22
25.90
17.82
10.30
4.64
2.77
1.81
1.29
0.98
0.77
0.61
0.52
0.43
0.29
0.21
0.16
0.13
0.10
0.09
0.06
0.04
49
5.67
3.70
01
83
0.48
0.29
0.20
0.15
0.11
0.09
0.07
0.06
0.04
0.03
0.02
0.02
0.01
0.01
0.01
0.00
2
0
23
54.60
38.27
22.72
10.54
6.40
4.24
3.06
2.35
1.85
1.48
1.23
1.00
0.67
0.50
0.39
0.30
0.25
0.21
0.15
0.09
50
13.63
9.06
5.00
2.12
1.22
0.76
0.52
0.39
0.29
0.23
0.19
0.16
0.11
0.08
0.06
0.05
0.04
0.03
0.02
0.01
Volume VII
Appendix VIM
_ . ^
*CVieW Draft
Dp Not Cite or Quote
-------
24
166.96
122.01
76.06
37.73
23.67
16.08
11.82
8.88
6.80
5.36
4.46
3.70
2.56
1.89
1.43
1.16
0.94
0.81
0.59
0.37
51
39.32
26.69
15.20
6.66
3.85
2.40
1.67
1.23
0.93
0.75
0.61
0.51
0.35
0.25
0.19
0.15
0.12
0.10
0.07
0.04
25
3.89
2.59
1.43
0.61
0.35
0.22
0.16
0.12
0.09
0.07
0.06
0.05
0.03
0.02
0.02
0.01
0.01
0.01
0.01
0.00
52
80.04
55.56
32.49
14.75
8.30
5.29
3.71
2.73
08
70
1.35
1.16
0.78
0.56
0.44
0.34
0.28
0.23
0.16
0.10
2
1
4
1,
1,
26
10.66
7.21
.09
.80
.06
0.68
0.49
0.37
0.29
0.23
0.19
0.16
0.11
0.08
0.06
0.05
0.04
0.03
0.02
0.01
53
142.45
102.38
62.81
28.18
16.50
10.95
7.75
5.81
4.63
.62
.08
2.57
1.76
1.29
0.97
0.79
0.62
0.53
0.38
0.22
3
3
27
22.11
15.19
8.78
3.96
2.36
1.54
1.11
0.84
0.66
0.52
0.44
0.37
0.26
0.18
0.14
0.11
0.09
0.08
0.06
0.03
54
252.35
182.53
115.80
62.96
41.16
29.51
22.23
16.96
14.09
11.29
9.71
8.12
5.74
4.21
3.17
2.56
2.04
1.69
1.17
0.68
Volume VII
Appendix \fld-4
External Review Draft
Do Not Cite or Quote
-------
X,m Max concentration, ppm
25.00
50.00
100.00
200.00
300.00
400.00
500.00
600.00
700.00
800.00
. 900.00
1000.00
1250.00
1500.00
1750.00
2000.00
2250.00
2500.00
3000.00
4000.00
252.35
183.81
119.82
62.96
41.16
29.51
22.23
16.96
14.09
11.29
9.71
8 . 12
5.74
4.21
3.17
2.56
2.04
1.69
1.17
0.68
Concentration (ppm)
Distance to (m)
LOG
IDLH
9.6000
19.6000
906.64
549.87
Volume VII
Appendix VII-4
External Review Draft
Do Not Cite or Quote
-------
Prom Slab output file:
Scenario:
Accident Location:
Duration:
Meteorology:
Chemical:
Vapor phase mole fraction:
LOG:
IDLH:
*Output adjusted to be distance from
X,m
25.00
50.00
100.00
200.00
300.00
400.00
500.00
600.00
700.00
800.00
900.00
1000.00
1250.00
1500.00
1750.00
2000.00
2250.00
2500.00
3000.00
4000.00
X,m
25.00
50.00
100.00
200.00
300.00
400.00
500.00
600.00
700.00
800.00
900.00
1000.00
1250.00
1500.00
1750.00
2000.00
2250.00
2500.00
3000.00
4000.00
1
3.85
2.51
1.37
0.57
0.32
0.20
0.14
0.10
0.08
0.06
0.05
0.04
0.03
0.02
0.02
0.01
0.01
0.01
0.01
0.00
28
47.21
33.12
19.68
9.16
5.56
,68
,67
,04
,61
,28
,08
3.
2.
2.
1.
1.
1.
0.87
0.59
0.43
0.34
0.26
0.22
0.18
0.13
0.08
-«- -- — --
:e from
2
9.23
6.14
3.40
1.45
0.83
0.53
0.37
0.27
0.21
0.16
0.13
0.11
0.07
0.05
0.04
0.03
0.03
0.02
0.02
0.01
29
145.62
106.02
66.35
32.80
20.54
13.93
10.26
7.69
5.88
4.65
3.87
3.22
2.21
1.64
1.24
1.01
0.82
0.70
0.52
0.32
RUN16.OUT
TYPICAL
ON-SITE
MITIGAT
WORST
FORMALDEHYDE
0.512
9.600
19.600
fence line.
3
25.94
17.59
10.02
4.40
2.59
1.67
1.16
0.86
0.65
0.51
0.43
0.35
0.24
0.17
0.13
0.10
0.09
0.07
0.05
0.03
30
3.47
2.30
1.28
0.54
0.31
0.20 -
0.14
0.10
0.08
0.06
0.05
0.04
0.03
0.02
0.02
0.01
0.01
0.01
0.01
0.00
4
54.75
37.85
22.01
9.93
5.91
3.74
2.59
1.92
1.46
1.17
0.96
0.80
0.55
0.40
0.30
0.24
0.19
0.16
0.12
0.07
31
9.51
6.44
3.65
1.60
0.94
0.61
0.43
0.33
0.26
0.20
0.17
0.14
0.10
0.07
0.06
0.04
0.04
0.03
0.02
0.01
5
110.58
78.38
47.19
22.18
12.61
8.10
5.72
4.22
3.27
2.65
2.15
1.81
1.23
0.90
0.71
0.55
0.46
0.37
0.28
0.16
32
19.62
13.50
7.81
3.53
2.11
1.38
0.99
0.75
0.59
0.47
0.39
0.33
0.23
0.16
0.13
0.10
0.08
0.07
0.05
0.03
Volume Vn
Appendix VII-4
External Review Draft
Do Not Cite or Quote
-------
6
241.68
181.60
114.17
55.57
33.92
23.32
17.32
13.54
10.51
8.84
7.16
6.23
4.32
3.22
2.52
1.94
1.63
1.34
0.98
0.58
33
41.13
28.85
17.13
7.99
4.84
3.21
2.32
1.78
1.41
1.12
0.95
0.79
0.53
0.39
0.30
0.24
0.19
0.16
0.12
0.07
0
0
7
2.88
1.89
1.02
0.43
0.24
.15
.11
0.08
0.06
0.05
0.04
0.03
0.02
0.02
0.01
0.01
0.01
0.01
0.00
0.00
34
127.50
92.88
57.75
28.47
17.83
12.09
8.90
6.91
5.43
4.20
3.53
2.88
1.96
1.47
1.13
0.90
0.74
0.62
0.46
0.29
8
6.95
4.61
2.56
1.08
0.63
0.40
0.28
0.21
0.16
0.12
0.10
0.08
0.06
0.04
0.03
0.02
0.02
0.02
0.01
0.01
35
08
05
1.14
0.48
0.28
0.18
0.12
0.09
0.07
0.06
0.05
0.04
0.03
0.02
0.02
0.01
0.01
0.01
0.01
0.00
3
2
9
19.13
12.99
7.38
3.25
1.91
1.24
0.88
0.67
0.51
0.40
0.33
0.27
0.16
0.13
0.10
0.08
0.07
0.05
0.04
0.02
36
8.44
5.71
3.24
1.43
0.84
0.54
0.39
0.29
0.23
0.18
0.15
0.13
0.09
0.06
0.05
0.04
0.03
0.03
0.02
0.01
2
1
10
40.31
27.79
16.14
7.28
4.33
2.83
02
50
1.15
0.90
0.74
0.60
0.41
0.31
0.24
0.18
0.15
0.12
0.09
0.06
37
17.43
11.97
6.93
3.13
1.87
1.22
0.87
0.67
0.52
0.41
0.35
0.29
0.20
0.15
0.12
0.09
0.07
0.06
0.05
0.03
11
84.61
59.49
35.62
16.65
10.07
6.69
4.66
3.45
2.63
2.09
1.72
1.43
0.99
0.73
0.54
0.44
0.36
0.30
0.22
0.14
38
36.46
25.59
15.17
7
4
2
08
28
84
2.06
1.58
1.24
0.99
0.84
0.70
0.50
0.35
0.28
0.22
0.18
0.15
0.11
0.07
Volume VII
A .. .._. .
Appendix VH-4
vv
c , „ . ^
External Review Draft
~ XI _.
Do Not Cte or Quote
-------
12
221.68
164.02
104.64
53.44
31.41
20.78
14.92
11.10
8.89
7.16
6.00
4.94
3.44
2.61
2.00
1.61
1.31
1.11
0.81
0.49
39
.77
.84
.02
0.43
0.25
0.16
0.11
0.08
0.06
0.05
0.04
0.03
0.02
0.02
0.01
0.01
0.01
0.01
0.01
0.00
0,
0.
2.
1,
1.
13
2.31
1.51
0.82
,34
,19
0.12
0.09
0.06
0.05
0.04
0.03
0.03
0.02
0.01
0.01
0.01
0.01
0.01
0.00
0.00
40
7.60
5.14
2.92
1.28
0.75
0.49
0.35
0.26
0.21
0.16
0.14
0.11
0.08
0.06
0.05
0.04
0.03
0.02
0.02
0.01
14
5.55
3.69
2.04
0.87
0.50
0.32
0.22
0.17
0.13
0.10
0.08
0.07
0.05
0.03
0.03
0.02
0.02
0.01
0.01
0.01
41
15.64
10.76
6.23
2.81
1.68
1.10
0.79
0.60
0.47
0.37
0.31
0.26
0.18
0.13
0.11
0.09
0.07
0.06
0.04
0.03
15
15.20
10.30
5.85
2.58
1.52
0.98
0.70
0.53
0.41
0.32
0.27
0.22
0.15
0.11
0.08
0.07
0.05
0.04
0.03
0.02
42
32.73
22.96
13.61
6.36
3.85
2.55
1.85
1.42
1.12
0.89
0.76
0.63
0.45
0.33
0.26
0.20
0.16
0.14
0.10
0.06
16
31.82
21.94
12.73
5.75
3.42
2.23
1.60
1.21
0.94
0.73
0.61
0.50
0.34
0.25
0.19
0.15
0.12
0.10
0.08
0.05
43
4.75
3.21
1.82
0.80
0.47
0.30
0.22
0.16
"0.13
0.10
0.09
0.07
0.05
0.04
0.03
0.02
0.02
0.02
0.01
0.01
3,
2,
17
67.25
47.24
28.12
13.08
7.94
5.25
80
84
2.17
1.70
1.41
1.16
0.80
0.59
0.45
0.36
0.29
0.24
0.18
0.11
44
9.75
6.70
3.89
1.76
1.05
0.69
0.49
0.37
0.29
0.23
0.20
0.16
0.11
0.08
0.07
0.05
0.04
0.04
0.03
0.02
Volume VH
Appendix VII-4
External Review Draft
Do Not Cite or Quote
-------
18
194.45
142.66
90.05
45i28
27.66
17.81
12.68
9.47
7.31
6.00
4.86
4.16
2.88
2.14
1.68
1.30
1.10
0.91
0.68
0.42
45
3.82
2.58
1.46
0.64
0.38
0.24
0.17
0.13
0.10
0.08
0.07
0.06
0.04
0.03
0.02
0.02
0.01
0.01
0.01
0.01
19
1.92
1.26
0.68
0.28
0.16
0.10
0.07
0.05
0.04
0.03
0.03
0.02
0.02
0.01
0.01
0.01
0.01
0.00
0.00
0.00
46
7.80
5.38
3.11
1.40
0.84
0.55
0.39
0.30
0.23
0.19
0.16
0.13
0.09
0.07
0.05
0.04
0.03
0.03
0.02
0.01
20
4.62
3.07
1.70
0.72
0.42
0.26
0.19
0.14
0.11
0.08
0.07
0.06
0.04
0.03
0.02
0.02
0.01
0.01
0.01
0.01
47
5.20
3.58
2.07
0.94
0.56
0.36
0.26
0.20
0.16
0.12
0.10
0.09
0.06
0.04
0.04
0.03
0.02
0.02
0.01
0.01
21
12.66
8.56
4.86
2.14
1.26
0.81
0.58
0.44
0.34
0.27
0.23
0.19
0.13
0.09
0.07
0.06
0.05
0.04
0.03
0.02
48
3.90
2.68
1.56
0.70
0.42
0.27
0.20
0.15
0.12
0.09
0.08
0.07
0.05
0.03
0.03
0.02
0.02
0.01
0.01
0.01
22
26.33
18.14
10.53
4.74
2.83
1.84
1.32
1.01
0.79
0.62
0.52
0.43
0.29
0.21
0.16
0.13
0.11
0.09
0.06
0.04
49.
5.75
3.77
2.05
0.85
0.49
0.30
0.20
0.15
0.11
0.09
0.07
0.06
0.04
0.03
0.02
0.02
0.01
0.01
0.01
0.00
23
55.49
36.96
23.15
10.79
6.53
4.32
3.13
2.40
1.87
1.45
1.21
0.98
0.67
0.50
0.39
0.30
0.25
0.20
0.15
0.09
50
13.86
9.21
5.10
2.16
1.23
0.76
0.53
0.39
0.29
0.24
0.19
0.16
0.11
0.08
0.06
0.05
0.04
0.03
0.02
0.01
Volume Vn
A j- TTTT .
Appendix VII-4
_ , . _ . _ .
External Review Draft
_. VT „. _
Do Not Cite or Quote
-------
24 25 26 27
167.97 3.96 10.86 22.47
123.25 2.63 7.34 15.50
77.17 1.46 4.17 8.96
38.30 0.62 1.83 4.05
24.08 0.36 1.08 2.41
16.37 0.23 0.70 1.58
11.49 0.16 0.50 1.13
8.57 0.12 0.38 0.86
6.55 0.09 0.29 0.67
5.28 0.07 0.23 0.53
4.33 0.06 0.19 0.45
3.67 0.05 0.16 0.37
2.54 0.03 0.11 0.25
1.86 0.03 0.08 0.18
1.42 0.02 0.06 0.14
1.16 0.02 0.05 0.11
0.94 0.01 0.04 0.09
0.80 0.01 0.03 0.08
0.58 0.01 0.02 0.06
0.36 0.00 0.01 0.03
51 52 53 54
39.86 80.52 141.28 236.20
27.13 55.86 101.88 171.82
15.49 32.81 60.70 110.32
6.82 14.39 27.53 60.81
3.80 8.19 16.10 40.61
2.40 5.27 10.73 29.13
1.68 3.69 7.57 21.75
1.23 2.70 5.88 17.33
0.92 2.11 4.57 13.96
0.76 1.69 3.70 11.52
0.60 1.38 3.04 9.56
0.52 1.15 2.59 8.22
0.35 0.78 1.78 5.69
0.25 0.57 1.29 4.07
0.19 0.44 0.99 3.24
0.15 0.34 0.79 2.51
0.12 0.28 0.64 2.08
0.10 0.23 0.53 1.661
0.07 0.17 0.37 1.22
0.05 0.10 0.22 0.69
Volume VH c , n ~
...... . External Review Draft
Appendix VII-4 _ XT _.
Do Not Cite or Quote
-------
From Slab output file:
Scenario:
Accident Location:
Duration:
Meteorology:
Chemical:
Vapor phase mole fraction:
LOG:
IDLH:
RUN17.ODT
TYPICAL
ON-SITE
UNMITIG
INVERSN
FORMALDEHYDE
0.482
9.600
19.600
*Output adjusted to be distance from fenceline.
X,m Max concentration, ppm
25.00
50.00
100.00
200.00
300.00
400.00
500.00
' 600.00
700.00
800.00
900.00
1000.00
1250.00
1500.00
1750.00
2000.00
2250.00
2500.00
3000.00
4000.00
5000.00
273.13
220.21
158.21
101.73
74.44
57.70
46.12
37.38
31.36
26.38
22.52
19.47
14.04
10.41
8.07
6.43
5.08
4.29
3.03
1.72
1.09
Concentration (ppm)
LOC
IDLH
9.6000
19.6000
Distance to (m)
1586.16
995.67
Volume VII
Appendix VII-4
External Review Draft
Do Not Cite or Quote
-------
From Slab output file:
Scenario:
/ -^ Accident Location:
( , Duration:
V x Meteorology:
Chemical:
Vapor phase mole fraction:
LOG:
IDLH:
RUN18.0UT
TYPICAL
ON-SITE
MITIGAT
INVERSN
FORMALDEHYDE
0.512
9.600
19.600
*0utput adjusted to be distance from fenceline.
X,m Max. concentration, ppm
25.00
50.00
100.00
200.00
300.00
400.00
500.00
' 600.00
700.00
800.00
900.00
1000.00
1250.00
1500.00
.- ^ 1750.00
2000.00
X 2250.00
2500.00
3000.00
4000.00
5000. OQ
275
221
160
102
75
58
46
37
31
26
22
19
14
10
8
6
5
4
3
1
1
.80
.92
.37
.75
.45
.47
.49
.68
.62
.55
.61
.52
.05
.40
.06
.42
.08
.29
.03
.72
.09
-Concentration (ppm)
LOG
IDLH
9.6000
19.6000
Distance to (m)
= = = = = = = =: = = =: = = =
1585.91
997.50
Volume VII
Appendix VII-4
External Review Draft
Do Not Cite or Quote
-------
From Slab output file:
Scenario:
Accident Location:
Duration:
Meteorology:
Chemical:
Vapor phase mole fraction:
LOG:
IDLH:
RUN19.OUT
TYPICAL
ON-SITE
UNMITIG
TYPICAL
ACETONE
0.276
1960.000
2442.000
*Output adjusted to be distance from fenceline.
X,m Max concentration, ppm
25.00
50.00
100.00
200.00
300.00
- 400.00
500.00
600.00
700.00
800.00
900.00
1000.00
1250.00
1500.00
1750.00
2000.00
2250.00
2500.00
3000.00
4000.00
' 5.24
3.58
2.06
0.92
0.55
0.35
0.25
0.19
0.15
0.12
0.10
0.08
0.06
0.04
0.03
0.03
0.02
0.02
0.01
0.01
Concentration (ppm)
Distance to (m)
LOG
IDLH
1960.0000
2442.0000
less than
less than
25.00
25.00
Volume VII
Appendix VII-4
External Review Draft
Do Not Cite or Quote
-------
From Slab output file: RUN20.OUT
Scenario: TYPICAL
Accident Location: ON-SITE
Duration: MITIGAT
Meteorology: ______ TYPICAL
Chemical: ACETONE
Vapor phase mole fraction: 0.538
LOC: 1960.000
' IDLH: . 2442.000
*Output adjusted to be distance from fenceline.
X,m Max concentration, ppm
25.00 5.82
50.00 . 4.02
100.00 2.33
200.00 1.05
300.00 0.63
400.00 0.41
' 500.00 0.29
600.00 0.22
700.00 0.17
800.00 0.14
900.00 0.12
1000.00 0.10
1250.00 0.06
1500.00 0.05
,,-^ 1750.00 • 0.04
/ 2000.00 0.03
x ^ 2250.00 0.02
2500.00 0.02
3000-.oo o.or
4000.00 0.01
5000.00 0.01
Concentration (ppm) , Distance to (m)
LOC 1960.0000 less than 25.00
IDLH 2442.0000 less than 25.00
Volume VH E^^, Review Draft
Appendk VIM ^ Not Cite Of
-------
From Slab output file:
Scenario:
Accident Location:
Duration:
Meteorology:
Chemical:
Vapor phase mole fraction:
LOG:
IDLH:
*0utput adjusted to be distance from
X,m
25.00
50.00
100.00
200.00
300.00
400.00
500.00
600.00
700.00
800.00
900.00
1000.00
1250.00
1500.00
1750.00
2000.00
2250.00
2500.00
3000.00
4000.00
X,m
25.00
50.00
100.00
200.00
300.00
400.00
500.00
600.00
700.00
800.00
900.00
1000.00
1250.00
1500.00
1750.00
2000.00
2250.00
2500.00
3000.00
4000.00
1
0.80
0.52
0.28
0.12
0.07
0.04
0.03
0.02
0.02
0.01
0.01
0.01
0.01
0.00
0.00
0.00
0.00
0.00
0.00
0.00
28
10.18
7,
4,
10
19
1.93
1.16
0.77
0.55
0.42
0.33
0.26
0.22
0.19
0.13
0.10
0.08
0.06
0.05
0.04
0.03
0.02
- -- _ -
i from
2
1.91
1.26
0.70
0.29
0.17
0.11
0.07
0.06
0.04
0.03
0.03
0.02
0.02
0.01
0.01
0.01
0.01
0.01
0.00
0.00
29
30.99
22.49
14.00
6.89
4.30
2.93
2.15
1.66
1.33
1.07
0.91
0.76
0.55
0.41
0.33
0.27
0.22
0.19
0.14
0.09
RUN21.0DT
TYPICAL
ON-SITE
UNMITIG
WORST
ACETONE
0.276
1960.000
2442.000
fenceline.
3
5.65
3.79
2.15
0.93
0.54
0.35
0.25
0.19
0.14
0.11
0.10
0.08
0.05
0.04
0.03
0.03
0.02
0.02
0.01
0.01
30
0.72
0.47
0.26
0.11
0.06
0.04
0.03
0.02
0.02
0.01
0.01
0.01
0.01
0.00
0.00
0.00
0.00
0.00
0.00
0.00
4
11.83
8.13
4.68
2.10
1.25
0.81
0.58
0.44
0,34
0.27
0.23
0.19
0.13
0.10
0.07
0.06
0.05
0.04
0.03
0.02
31
1.96
1.32
0.75
0.32
0.19
0.12
0.09
0.07
0.05
0.04
0.03
0.03
0.02
0.01
0.01
0.01
0.01
0.01
0.00
0.00
0,
0,
5
22.00
15.62
9.46
4.50
2.77
1.85
1.34
1.03
0.81
0.64
0.55
0.45
0.32
0.24
0.19
0.15
12
11
0.08
0.05
32
4.12
2.82
1.62
0.72
0.43
0.28
0.20
15
12
0.09
0.08
0.07
0.05
0.03
0.03
0.02
0.02
0.02
0.01
0.01
0.
0.
Volume VII
Appendix VII-4
External Review Draft
Do Not Cite or Quote
-------
6
41.49
31.82
21.35
11.87
7.94
5.67
4.32
3.45
2.82
2.31
1.99
1.70
1.24
0.94
0.76
0.63
0.52
0.45
0.34
0.22
33
8.82
6.14
3.62
.66
.00
.66
0.48
0.36
0.29
0.23
0.19
16
11
0.08
0.07
0.05
0.04
0.04
0.03
0.02
1,
1,
0,
0
0
7
0,60
0.39
0.21
0.09
0.05
0.03
0.02
0.02
0.01
0.01
0.01
0.01
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
34
27.69
20.04
12.39
6.07
3.78
2.56
1.87
1.45
1.15
0.93
0.79
0.66
0.48
0.35
0.28
0.23
0.19
0.16
0.12
0.08
8
1.44
0.95
0.52
0.22
0.13
0.08
0.06
0.04
0.03
0.03
0.02
0.02
0.01
0.01
0.01
0.01
0.00
0.00
0.00
0.00
35
0.64
0.42
0.23
0.10
0.06
0.04
0.02
0.02
0.01
0.01
0.01
0.01
0.01
0.00
0.00
0.00
0.00
0.00
0.00
o.-oo
9
4.10
2.76
1.56
0.68
0.40
0.26
0.18
0.14
0.11
0.08
0.07
0.06
0.04
0.03
0.02
0.02
0.01
0.01
0.01
0.01
36
1.74
1.17
0.66
0.29
0.17
0.11
0.08
0.06
0.05
0.04
0.03
0.03
0.02
0.01
0.01
0.01
0.01
o.ai
0.00
0.00
10
8.80
6.03
3.47
1.54
0.91
0.59
0.42
0.32
0.25
0.20
0.17
0.14
0.10
0.07
0.06
0.04
0.04
0.03
0.02
0.01
37
3.66
2.49
1.43
0.64
0.38
0.25
0.18
0.13
0.11
0.08
0.07
0.06
0.04
0.03
0.02
0.02
0.02
0.01
0.01
0.01
11
18.06
12.66
7.52
3.49
2.12
1.40
1.01
0.77
0.61
0.48
0.41
0.34
0.24
0.18
0.14
0.11
0.09
0.08
0.06
0.04
38
7.77
5.40
18
46
0.88
0.58
0.42
0.32
0.25
0.20
0.17
0.14
0.10
0.07
0.06
0.05
0.04
0.03
0.03
0.02
3,
1
Volume VH
Appendix W-4
External Review Draft
Do Not Cite or Quote
-------
12 13 14 15 16 17
40.19 0.48 1.15 3.20 6.88 14.63
29.93 0.31 0.76 2.16 4.69 10.22
19.56 0.17 0.42 1.22 2.71 6.04
10.35 0.07 0.18 0.53 1.20 . 2.77
6.73 0.04 0.10 0.31 0.71 1.68
4.70 0.02 0.06 0.20 0.46 1.11
3.52 0.02 0.04 0.14 0.33 0.80
2.77 0.01 0.03 0.11 0.25 0.61
2.24 0.01 0.01 0.08 0.20 0.48
1.82 0.01 0.02 0.07 0.15 0.38
1.56 0.01 0.02 0.06 0.13 0.32
1.32 0.01 0.01 0.05 0.11 0.27
0.96 0.00 0.01 0.03 0.08 0.19
0.72 0.00 0.01 0.02 0.06 0.14
0.58 0.00 0.01 0.02 0.04 0.11
0.47 0.00 0.00 0.01 0.04 0.09
0.39 0.00 0.00 0.01 0.03 0.07
0.34 0.00 0.00 0.01 0.02 0.06
0.25 0.00 0.00 0.01 0.02 0.05
0.16 0.00 0.00 0.00 0.01 0.03
39 40 41 42 43 44
0.58 1.57 3.28 6.94 0.99 2.03
0.38 1.05 2.24 4.83 0.66 1.39
0.21 0.59 1.29 2.84 0.37 0.80
0.09 0.26 0.57 1.31 0.16 0.36
0.05 0.15 0.34 0.79 0.10 0.21
0.03 0.10 0.22 0.52 0.06 0.14
0.02 0.07 0.16 0.38 0.04 0.10
0.02 0.05 0.12 0.29 0.03 0.08
0.01 0.04 0.09 0.23 0.03 0.06
0.01 0.03 0.07 0.18 0.02 0.05
0.01 0.03 0.06 0.15 0.02 0.04
0.01 0.02 0.05 0.13 0.01 0.03
0.00 0.02 0.04 0.09 0.01 0.02
0.00 0.01 0.03 0.07 0.01 0.02
0.00 0.01 0.02 0.05 0.01 0.01
0.00 0.01 0.02 0.04 0.00 0.01
0.00 0.01 0.01 0.03 0.00 0.01
0.00 0.01 0.01 0.0*3 0.00 0.01
0.00 0.00 0.01 0.02 0.00 0.01
0.00 0.00 0.01 0.01 0.00 0.00
, External Review Draft
Append* VH-4 Do Not Cite or Quote
-------
5,
3,
18
37.77
27.83
17.67
9.03
.76
.98
2.94
2.29
1.84
1.49
1.27
1.07
0.77
0.58
0.46
0.38
0.31
0.27
0.20
0.13
45
0.79
0.53
0.30
0.13
0.08
0.05
0.04
0.03
0.02
0.02
0.01
0.01
0.01
0.01
0.00
0.00
0.00
0.00
0.00
0.00
19
0.40
0.26
0.14
0.06
0.03
0.02
0.01
0.01
0.01
0.01
0.01
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
46
1.62
1.11
0.64
0.29
0.17
0.11
0.08
0.06
0.05
0.04
0.03
0.03
0.02
0.01
0.01
0.01
0.01
0.01
0.00
0.00
20
0.96
0.63
0.35
0.15
0.08
0.05
0.04
0.03
0.02
0.02
0.01
0.01
0.01
0.01
0.00
0.00
0.00
0.00
0.00
0.00
47
1.08
0.74
0.42
0.19
0.11
0.07
0.05
0.04
0.03
0.02
0.02
0.02
0.01
0.01
0.01
0.01
0.00
0.00
0.00
0.00
21
2.64
1.78
1.00
0.44
0.26
0.17
0.12
0.09
0.07
0.05
0.05
0.04
0.03
0.02
0.02
0.01
0.01
0.01
0.01
0.00
48
0.81
0.55
0.32
0.14
0.08
0.06
0.04
0.03
0.02
0.02
0.02
0.01
0.01
0.01
0.01.
0.00
0.00
0.00
0.00
0.00
22
5.63
3.84
2.21
0.99
0.59
0.38
0.27
0.21
0.16
0.13
0.11
0.09
0.06
0.05
0.04
0.03
0.02
0.02
0.01
0.01
49
1.19
0.77
0.42
0.17
0.10
0.06
0.04
0.03
0.02
0.02
0.02
0.01
0.01
0.01
0.01
0.00
0.00
0.00
0,00
0.00
23
12.07
8.41
4.. 97
2.28
1.38
0.91
0.65
0.50
0.39
0.31
0.26
0.22
0.15
0.11
0.09
0.07
0.06
0.05
0.04
0.02
50
2.89
1.91
1.05
0.44
0.26
0.16
0.11
0.09
0.07
0.05
0.04
0.04
0.02
0.02
0.01
0.01
0.01
0.01
0.01
0.00
Volume YE
Appendix VII-4
External Review Draft
Do Not Cite or Quote
-------
24 25 26 27
34.52 0.82 2.25 4.75
25.17 0.54 1.51 3.24
15.76 0.30 0.85 1.87
7.88 0.13 0.37 0.83
4.96 0.07 0.22 0.50
3.40 0.05 0.14 0.32
2.49 0.03 0.10 0.23
1.94 0.02 0.08 0.18
1.55 0.02 0.06 0.14
1.25 0.01 0.05 0.11
1.06 0.01 0.04 0.09
0.89 0.01 0.03 0.08
0.64 0.01 0.02 0.05
0.48 0.01 0.02 0.04
0.38 0.00 0.01 0.03
0.31 0.00 0.01 0.02
0.26 0.00 0.01 0.02
0.22 0.00 0.01 0.02
0.17 0.00 0.01 0.01
0.11 0.00 0.00 0.01
51 52 53 54
8.41 15.89 25.56 18.28
5.69 11.10 18.72 15.42
3.25 6.58 11.85 11.94
1.42 3.05 5.99 8.22
0.84 1.84 3.79 6.21
0.54 1.21 2.60 4.95
0.38 0.87 1.91 4.06
0.29 0.66 1.49 3.40
0.22 0.52 1.18 2.91
0.18 0.41 0.95 2.53
0.15 0.35 0.81 2.20
0.12 0.29 0.68 1.96
0.08 0.20 0.48 1.51
0.06 0.15 0.36 1.20
0.05 0.12 0.29 0.98
0.04 0.09 0.23 0.81
0.03 0.08 0.19 0.69
0.03 0.06 0.16 0.58
0.02 0.05 0.12 0.43
0.01 0.03 0.08 0.27
Volume VII External Review Draft
Appendix VH-4 Do Not Cite or Quote
-------
X,m Max concentration, ppm
25.00
50.00
100.00
200.00
300.00
400.00
500.00
600.00
700.00
800.00
900.00
1000.00
1250.00
1500.00
1750.00
2000.00
2250.00
2500.00
3000.00
4000.00
41.49
31.82
21.35 ------
11.87
7.94
5.67
4.32
3.45
2.91
2.53
2.20
1.96
1.51
1.20
0.98
0.81
0.69
0.58
0.43
0.27
Concentration (ppm)
Distance to (m)
LOG
1960.0000
2442.0000
less than
less than
25.00
25.00
Volume VII
Appendix VII-4
External Review Draft
Do Not Cite or Quote
-------
From Slab output file:
Scenario:
Accident Location:
Duration:
Meteorology:
Chemical:
Vapor phase mole fraction:
LOG:
IDLH:
*0utput adjusted to be distance
x,m
25.00
50.00
100.00
200.00
300.00
400.00
500.00
600.00
700.00
800.00
900.00
1000.00
1250.00
1500.00
1750.00
2000.00
2250.00
2500.00
3000.00
4000.00
X,m
25.00
50.00
100.00
200.00
300.00
400.00
500.00
600.00
700.00
800.00
900.00
1000.00
1250.00
1500.00
1750.00
2000.00
2250.00
2500.00
3000.00
4000.00
1
0.89
0.58
0.32
0.13
0.07
0.05
0.03
0.02
0.02
0.01
0.01
0.01
0.01
0.00
0.00
0.00
0.00
0.00
0.00
0.00
28
11.13
7.85
4.68
2.18
1.32
0.88
0.63
0.48
0.38
0.30
0.25
0.21
0.14
0.10
0.08
0.06
0.05
0.04
0.03
0.02
: from
2
2.13
1.41
0.79
0.33
0.19
0.12
0.09
0.06
0.05
0.04
0.03
0.03
0.02
0.01
0.01
0.01
0.01
0.01
0.00
0.00
29
30.42
22.42
14.23
7.23
4.61
3.18
2.35
1.78
1.37
1.08
0.90
0.75
0.52
0.39
0.29
0.24
0.19
0.16
0.12
0.08
RUN22.0UT
TYPICAL
ON-SITE
MITIGAT
WORST
ACETONE
0.538
1960.000
2442.000
fenceline.
3
6.14
4.17
2.38
1.05
0.62
0.40
0.28
0.20
0.16
0.12
0.10
0.08
0.06
0.04
0.03
0.02
0.02
0.02
0.01
0.01
30
0.80
0.53
0.29
0.13
0.07
0.05
0.03
0.02
0.02
0.01
0.01
0.01
0.01
0.01
0.00
0.00
0.00
0.00
0.00
0.00
4
12.09
8.42
4.97
2.28
1.37
0.87
0.61
0.45
0.34
0.28
0.23
0.19
0.13
0.09
0.07
0.06
0.05
0.04
0.03
0.02
•31
2.20
1.49
0.85
0.37
0.22
0.14
0.10
0.08
' 0.06
0.05
0.04
0.03
0.02
0.02
0.01
0.01
0.01
0.01
0.01
0.00
5
20.51
14.84
9.25
4.59
2.68
1.76
1.26
0.95
0.74
0.60
0.49
0.42
0.29
0.21
0.17
0.13
0.11
0.09
0.07
0.04
32
4.60
3.17
1.84
0.83
0.49
0.32
0.23
0.18
0.14
0.11
0.09
0.08
0.05
0.04
0.03
0.02
0.02
0.02
0.01
0.01
Volume VII
Appendix VII-4
External Review Draft
Do Not Cite or Quote
-------
6 7 8 9 10 11
35.34 0.66 1.60 4.56 9.52 18.03
27.32 0.43 1.06 3.10 6.59 12.87
18.00 0.24 0.59 1.76 3.84 7.81
9.44 0.10 0.25 0.78 1.73 3.74
6.11 0.06 0.14 0.45 1.03 2.30
4.40 0.04 0.09 0.29 0.68 1.48
3.38 0.02 0.06 0.21 0.48 1.04
2.71 0.02 0.05 0.16 0.36 0.78
2.16 0.01 0.04 0.12 0.27 0.59
1.84 0.01 0.03 0.09 0.21 0.48
1.52 0.01 0.02 0.08 0.18 0.39
1J34 0.01 0.02 0.06 0.15 0.33
0.95 0.00 0.01 0.04 0.10 0.23
0.72 0.00 0.01 0.03 0.07 0.17
0.57 0.00 0.01 0.02 0.06 0.13
0.44 0.00 0.01 0.02 0.04 0.10
0.37 0.00 0.00 0.02 0.04 0.08
0.31 0.00 0.00 0.01 0.03 0.07
0.23 0.00 0.00 0.01 0.02 0.05
0.14 0.00 0.00 0.01 0.01 0.03
33 34 35 36 37 38
9.71 28.02 0.71 1.95 4.07 8.56
6.81 20.56 0.47 1.32 2.80 6.03
4.06 13.00 0.26 0.75 1.62 3.58
1.89 6.53 0.11 0.33 0.73 1.67
1.15 4.12 0.06 0.19 0.44 1.01
0.76 2.83 0.04 0.13 - 0.29 0.67
0.55 2.09 0.03 0.09 0.20 0.48
0.42 1.62 0.02 0.07 0.16 0.37
0.33 1.28 0.02 0.05 0.12 0.29
0.26 0.99 0.01 0.04 0.10 0.23
0.22 0.83 0.01 0.04 0.08 0.20
0.19 0.68 0.01 0.03 0.07 0.16
0.12 0.47 0.01 0.02 0.05 0.12
0.09 0.35 0.00 0.01 0.03 0.08
0.07 0.27 0.00 0.01 0.03 0.06
0.06 0.21 0.00 0.01 0.02 0.05
0.05 0.17 0.00 0.01 0.02 0.04
0.04 0.15 0.00 0.01' 0.01 0.03
0.03 0.11 0.00 0.00 0.01 0.03
0.02 0.07 0.00 0.00 0.01 0.02
Volume VH . External Review Draft
Appendix VH-4 Do N()t
-------
12 13 14 15 16 17
34.61 0.53 1.28 3.59 7.59 15.37
26.37 0.35 0.85 2.44 5.24 10.89
17.70 0.19 0.47 1.38 3.04 6.54
9.15 0.08 0.20 0.61 1.37 3.08
5.77 0.04 0.12 0.36 0.82 1.88
4.01 0.03 0.07 0.23 0.53 1.25
2.96 0.02 0.05 0.16 0.38 0.90
2.28 0.01 0.04 0.12 0.29 0.67
1.87 0.01 0.03- 0.10 0.22 0.51
1.50 0.01 0.02 0.08 0.17 0.40
1.30 0.01 0.02 0.06 0.14 0.33
1.10 0.01 0.02 0.05 0.12 0.27
0.79 0.00 0.01 0.03 0.08 0.19
0.59 0.00 0.01 0.03 0.06 0.14
0.45 0.00 0.01 0.02 0.05 0.11
0.37 0.00 0.00 0.02 0.04 0.08
0.30 0.00 0.00 0.01 0.03 0.07
0.26 0.00 0.00 0.01 0.02 0.06
0.18 0.00 0.00 0.01 0.02 0.04
0.11 0.00 0.00 0.00 0.01 0.03
39 40 41 42 43 44
0.64 1.75 3.65 7.66 1.10 2.26
0.43 1.19 2.51 5.39 0.74 1.55
0.24 0.67 1.46 3.20 0.42 0.90
0.10 0.30 0.66 1.49 0.19 0.41
0.06 0.17 0.39 0.90 0.11 0.24
0.04 0.11 0.26 0.60 0.07 0.16
0.03 0.08 0.18 0.43 0.05 0.11
0.02 0.06 0.14 0.33 0.04 0.09
0.01 0.05 0.11 0.26 0.03 0.07
0.01 0.04 0.09 0.21 0.02 0.05
0.01 0.03 0.07 0.18 0.02 0.05
0.01 0.03 0.06 0.15 0.02 0.04
0.01 0.02 0.04 0.10 0.01 0.03
0.00 0.01 0.03 0.08 0.01 0.02
0.00 0.01 0.02 0.06 0.01 0.02
0.00 0.01 0.02 0.05 0.01 0.01
0.00 0.01 0.02 0.04 0.00 0.01
0.00 0.01 0.01 0.03' 0.00 0.01
0.00 0.00 0.01 0.02 0.00 0.01
0.00 0.00 0.01 0.01 0.00 0.00
Volume VII
Appendix VIM Extemal Review Draft
Do Not Cite or Quote
-------
18
34.10
25.58
16.73
8.89
5.64
3.72
2.71
2.06
1.61
1.34
1.11
0.95
0.66
0.49
0.39
0.30
0.26
0.21
0.16
0.10
45
0.89
0.60
0.34
0.15
0.09
0.06
0.04
0.03
0.02
0.02
0.02
0.01
0.01
0.01
0.01
0.00
0.00
0.00
0.00
0.00
19
0.44
0.29
0.16
0..07
0.04
0.02
0.02
0.01
0.01
0.01
0.01
0.01
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
46
1.80
1.24
0.72
0.32
0.19
0.13
0.09
0.07
0.05
0.04
0.04
0.03
0.02
0.02
0.01
0.01
0.01
0.01
0.01
0.00
20
1.07
0.71
0.39
0.17
0.10
0.06
0.04
0.03
0.02
0.02
0.02
0.01
0.01
0.01
0.01
0.00
0.00
0.00
0.00
0.00
47
1.20
0.83
0.48
0.22
0.13
0.08
0.06
0.05
0.04
0.03
0.02
0.02
0.01
0.01
0.01
0.01
0.01
0.00
0.00
0.00
21
2.96
2.00
1.14
0.50
0.30
0.19
0.14
0.10
0.08
0.06
0.05
0.04
0.03
0.02
0.02
0.01
0.01
0.01
0.01
0.00
48
0.90
0.62
0.36
0.16
0.10
0.06
0.05
0.03
0.03
0.02
0.02
0.02
0.01
0.01
0.01
0.00
0.00
0.00
0.00
0.00
22
6.23
4.30
2.50
1.13
0.67
0.44
0.31
0.24
0.19
0.15
0.12
0.10
0.07
0.05
0.04
0.03
0.02
0.02
0.01
0.01
49
1.33
0.87
0.47
0.20
0.11
0.07
0.05
0.03
0.03
0.02
0.02
0.01
0.01
0.01
0.01
0.00
0.00
0.00
0.00
0.00
1,
1,
23
12.99
9.18
5.49
2.57
,56
,03
0.75
0.57
0.45
0.34
0.29
0.23
0.16
0.12
0.09
0.07
0.06
0.05
0.04
0.02
50
3.20
2.13
1.18
0.50
0.29
0.18
0.12
0.09
0.07
0.06
0.04
0.04
0.03
0.02
0.01
0.01
0.01
0.01
0.01
0.00
Volume VH
Appendix VII-4
External Review Draft
Do Not Cite or Quote
-------
24 25 26 27
32.51 0.92 2.52 5.30
24.11 0.61 1.71 3.65
15.51 0.34 0.97 2.12
8.03 0.14 0.43 0.95
5.18 0.08 0.25 0.57
3.43 0.05 0.16 0.37
2.44 0.04 0.12 0.27
1.85 0.03 0.09 0.20
1.42 0.02 0.07 0.16
1.18 0.02 0.05 0.13
0.95 0.01 0.05 0.11
0.83 0.01 0.04 0.09
0.58 0.01 0.03 0.06
0.42 0.01 0.02 0.04
0.33 0.00 0.01 0.03
0.26 0.00 0.01 0.03
0.22 0.00 0.01 0.02
0.18 0.00 0.01 0.02
0.14 0.00 0.01 0.01
0.08 0.00 0.00 0.01
51 52 53 54
8.42 14.76 22.67 13.65
5.82 10.55 16.90 10.91
3.39 6.45 10.69 7.99
1.53 2.98 5.18 5.36
0.87 1.75 3.16 4.08
0.55 1.16 2.19 3.28
0.39 0.82 1.60 2.71
0.29 0.61 1.26 2.30
0.22 0.48 0.99 1.99
0.18 0.39 0.82 1.71
0.14 0.32 0.68 1.52
0.12 0.27 0.58 1.33
0.08 0.18 0.41 1.00
0.06 0.13 0.30 0.77
0.05 0.10 0.23 0.61
0.04 0.08 0.18 0.50
0.03 0.07 0.15 0.41
0.02 0.05 0.12 0.35*
0.02 0.04 0.09 0.25
0.01 0.02 0.05 0.15
Volume VII _ , _ .
Appendix VIM External Rev,ew Draft
Do Not Cite or Quote
-------
X,m Max concentration, ppm
25.00
50.00
100.00
200.00
300.00
400.00
500.00
600.00
700.00
800.00
900.00
1000.00
1250.00
1500.00
1750.00
2000.00
2250.00
2500.00
' 3000.00
4000.00
35.34
27.32
18.00 ------
9.44
6.11
4.40
3.38
2.71
2.16
1.84
1.52
1.34
1.00
0.77
0.61
0.50
0.41
0.35
0.25
0.15
Concentration (ppm)
Distance to (m)
LOG
1960.0000
2442.0000
less than
less than
25.00
25.00
Volume VII
Appendix VII-4
External Review Draft
Do Not Cite or Quote
-------
From Slab output file:
Scenario:
Accident Location:
Duration:
Meteorology--
Chemical:
Vapor phase mole fraction:
LOC:
IDLH:
RUN23.OUT
TYPICAL
ON-SITE
UNMITIG
INVERSN
ACETONE
0.276
1960.000
2442.000
*0utput adjusted to be distance from fenceline.
X,m Max concentration, ppm
25.00
50.00
100.00
200.00
300.00
400.00
500.00
600.00
700.00
800.00
900.00
1000.00
1250.00
1500.00
1750.00
2000.00
2250.00
2500.00
3000.00
4000.00
5000.00
75.76
59.28
41.52
25.61
18.16
14.02
11.33
9.49
8.04
6.91
6.04
5.30
4.00
3.15
2.53
2.06
1.74
1.45
1.09
0.67
0.45
- Concentration (ppm)
Distance to (m)
LOC
IDLH
1960.0000
2442.0000
less than
less than
25.00
25.00
Volume Vn
Appendix VII-4
External Review Draft
Do Not Cite or Quote
-------
From Slab output file: RUNA3.OUT
Scenario: TYPICAL
Accident Location: ON-SITE
Duration: UNMITIG
Meteorology: -~ -- INVERSN
Chemical: ACETONE
Vapor phase mole fraction: 0.276
LOC: 1960.000
IDLH: • 2442.000
*Output adjusted to be distance from fenceline.
X,m Max concentration, ppm
25.00
50.00
100.00
200.00
300.00
400.00
500.00
' 600.00
700.00
800.00
900.00
1000.00
1250.00
1500.00
->, 1750.00
2000.00
s 2250.00
2500.00
3000.00
4000.00
5000.00
10000.00
15000.00
. 20000.00
4.90
4.13
3.23
2.30
1.82
1.51
1.29
1.11
0.97
0.86
0.76
0.67
0.51
0.40
0.32
0.26
0.22
0.18
0.13
0.08
0.05
0.01
0.01
0.00
Concentration (ppm) Distance to (m)
========================================
LOC 1960.0000 less than 25.00
IDLH 2442.0000 less than 25.00
Volume VH . External Review Draft
Appendix Vn-4 Do Not Cite or Quote
-------
From Slab output file:
Scenario:
Accident Location:
Duration:
Meteorology:
Chemical:
Vapor phase mole fraction:
LOC:
IDLH:
RUN24.OUT
TYPICAL
ON-SITE
MITIGAT
INVERSN
ACETONE
0
538
1960.000
2442.000
*Output adjusted to be distance from fenceline.
X,m Max concentration, ppm
25.00
50.00
100.00
200.00
300.00
. 400.00
500.00
• 600.00
700.00
800.00
900.00
1000.00
1250.00
1500.00
1750.00
2000.00
2250.00
2500.00
3000.00
4000.00
5000.0.0
44.91
35.94
25.49
16.38
12.12
9.45
7.67
6.36
5.35
4.62
3.95
3.51
2.60
1.98
1.54
1.27
1.03
0.87
0.63
0.36
0.24
- Concentration (ppm)
Distance to (m)
LOC
IDLH
1960.0000
2442.0000
less than
less than
25.00
25.00
Volume
Appendix VII-4
External Review Draft
Do Not Cite or Quote
-------
From Slab output file: RUN49.0UT
Scenario: CONSERV
Accident Location: ON-SITE
Duration: UNMITIG
Meteorology: — --_.. TYPICAL
Chemical: HCL
Vapor phase mole fraction: 1.000
LOC: 9.900
• IDLH: 49.100
*Output adjusted to be distance from fenceline.
X,m Max concentration, ppm
25.00
50.00
100.00
200.00
300.00
400.00
500.00
• 600.00
700.00
800.00
900.00
1000.00
1250.00
1500.00
N. 1750.00
2000.00
^ 2250.00
2500.00
3000.00
4000.00
5000.00
10000.00
15000.00
20000.00
59
167
263
222
153
106
77
59
46
36
30
25
17
12
10
8
6
5
4
2
1
0
0
0
.01
.55
.91
.38
.10
.62
.62
.15
.24
.82
.95
.51
.60
.96
.11
.05
.47
.52
.02
.39
.61
.50
.25
.16
Concentration (ppm) Distance to (m)
LOC 9.9000 1775.30
IDLH 49.1000 677.85
Volume VH External Review Draft
Appendix VIM Do Not Cite or
-------
From Slab output file: RUN50.OUT
Scenario: CONSERV
Accident Location: ON-SITE
Duration: MITIGAT
Meteorologyi __ TYPICAL
Chemical: HCL
Vapor phase mole fraction: 1.000
LOC: 9.900
IDLH: 49.100
*Output adjusted to be distance from fenceline.
X,m Max concentration, ppm
25.00
50.00
100.00
200.00
300.00
400.00
500. 00
600.00
700.00
800.00
900.00
1000.00
1250.00
1500.00
1750.00
2000.00
2250.00
2500.00
3000.00
4000.00
5000.00
10000.00
15000.00
20000.00
33
94
149
125
86
60
43
33
26
20
17
14
10
7
5
4
3
2
2
1
0
0
0
0
.45
.94
.15
.49
.42
.21
.98
.52
.20
.87
.57
.52
.01
.12
.47
.29
.45
.89
.07
.27
.87
.27
.14
.09
Concentration (ppm) Distance to (m)
LOC 9.9000 1259.72
IDLH 49.1000 less than 25.00
Volume VII External Review Draft
Appendix VH-4 Do Not Cite or Quote
-------
From Slab output file:
Accident
1 '
Scenario:
Location:
Duration :
Meteorology:
'•-ii _,---'
Vapor phase mole
*Output adjusted
X,m
25.00
50.00
100.00
200.00
300.00
400.00
500.00
600.00
700.00
800.00
900.00
1000.00
1250.00
1500.00
1750.00
2000.00
2250.00
2500.00
3000.00
4000.00
5000.00
10000.00
^-"" 15000.00
X,m
25.00
50.00
100.00
200.00
300.00
400.00
500.00
600.00
700.00
800.00
900.00
1000.00
1250.00
1500.00
1750.00
2000.00
2250.00
2500.00
3000.00
4000.00
5000.00
10000.00
15000.00
Chemical:
fraction:
LOG:
IDLH:
— «> - - — --
to be distance from
1
211.86
146.49
79.62
33.78
18.35
11.54
7.96
5.90
4.59
3.61
2.97
2.46
1.66
1.20
0.90
0.72
0.57
0.48
0.35
0.20
0.14
0.04
0.02
28
0.19
9.45
185.57
317.92
274.10
209.95
160.67
124.98
98.44
81.72
67.50
57.55
40.03
29.58
22.99
18.28
15.20
12.77
9.36
5.64
3.80
1.13
0.58
2
424.91
351.70
213.55
93.58
52.32
32.61
22.67
16.99
13.15
10.26
8.48
6.99
4.77
3.37
2.56
2.03
1.60
1.35
0.97
0.59
0.40
0.12
0.06
29
0.00
0.03
1393.75
1893.05
1113.48
734.35
528.11
404.80
322.17
261.48
223.73
189.89
137.83
105.85
83.11
67.32
54.83
45.57
33.57
20.13
13.80
4.25
2.08
RUNS 1. OUT
CONSERV
ON-SITE
UNMITIG
WORST
HCL
1.000
9.900
49.100
fenceline.
3
2069.98
1499.70
767.54
296.31
166.02
105.06
73.32
54.82
42.39
33.17
28.01
23.00
15.34
10.94
8.46
6.65
5.37
4.48
3.20
1.95
1.32
0.39
0.19
30
159.42
125.72
74.80
32.73
18.19
11.66
8.10
5.93
4.54
3.68
2.94
2.51
1.71
1.25
0.95
0.76
0.62
0.51
0.38
0.23
0.16
0.05
0.03
4
3969.77
2569.52
1266.58
527.85
306.72
203.43
146.94
112.11
87;93
71.07
59.99
50.24
33.58
24.83
19.18
14.98
12.32
10.21
7.30
4.49
3.02
0.90
0.43
31
123.07
158.30
158.58
92.18
.54.76
36.63
25.96
19.19
15.27
12.19
9.88
8.40
5.78
4.19
3.18
2.60
2.11
1.78
1.32
0.80
0.54
0.17
0.09
5
5654.50
3413.61
1728.28
809.76
496.06
350.67
263.84
207.52
166.60
140.51
118.39
100.51
70.02
52.47
40.65
32.02
26.90
22.14
16.55
9.83
6.70
1.97
0.94
32
43.50
104.96
169.22
151.26
108.22
76.83
56.85
44.09
35.11
28.12
23.53
19.66
13.70
9.98
7.80
6.32
5.10
4.33
3.20
1.92
1.29
0.41
0.21
Volume VIE
Appendix VIM
External Review Draft
Do Not Cite or Quote
-------
6
8087.54
5029.25
2774.64
1422.03
950.41
708.22
561.12
459.07
379.64
320.12
271.24
238.70
176.96
137.03
110.72
92.00
75.88
65.70
49.06
31.16
21.22
5.93
2.65
33
0.06
5.57
87.02
208.35
193.31
157.53
125.15
100.29
80.89
67.46
56.59
48.18
34.02
25.35
19.84
15.86
13.12
11.10
8.16
4.92
3.32
1.01
0.51
7
160.13
112.70
60.75
25.63
13.88
8.73
6.02
4.45
3.46
2.72
2.21
1.84
1.26
0.91
0.69
0.55
0.44
0.37
0.26
0.16
0.11
0.03
0.02
34
0.00
0.00
70.67
1419.08
1063.05
719.95
516.66
393.46
310.84
250.00
211.54
178.73
128.45
97.26
76.15
62.97
52.07
42.80
31.16
18.87
12.89
3.94
1.97
8
275.56
235.56
146.82
66.10
37.41
23.44
16.40
12.31
9.54
7.46
6.16
5.08
3.49
2.53
1.95
1.55
1.22
1.03
0.75
0.45
0.30
0.09
0.05
35
146.70
113.42
66.75
28.89
16.24
10.33
7.21
5.30
4.00
3.26
2.63
2.22
1.51
1.11
0.84
0.67
0.55
0.45
0.34
0.21
0.14
0.05
0.02
9
487.33
595.85
479.75
233.80
132.85
84.43
58.67
43.51
33.36
26.14
21.65
17.56
12.05
8.74
6.75
5.29
4.20
3.53
2.53
1.53
1.03
0.30
0.16
36
115.86
147.67
141.92
81.20
48.71
32.46
22.99
17.02
13.30
10.77
8.69
7.46
5.10
3.73
2.83'
2.29
1.88
1.56
1.16
0.71
0.48
0.16
0.08
10
1052.67
1406.00
1146.94
529.50
294.82
188.48
131.47
97.69
75.02
60.21
49.71
41.22
27.89
20.91
16.05
12.45
9.98
8.31
5.96
3.62
2.44
0.73
0.37
37
39.11
88.73
146.41
129.24
92.17
66.24
49.23
37.92
30.52
24.67
20.52
17.29
11.98
8.83
6.75
5.53
4.50
3.80
2.82
1.72
1.17
0.37
0.20
11
2724.16
3633.70
2145.70
895.39
504.97
341.83
248.46
189.28
150.02
124.26
102.70
88.49
61.51
44.85
34.21
26.71
22.35
18.16
13.54
8.17
5.54
1.68
0.82
38
0.13
3.76
55.20
150.74
145.75
123.45
101.02
82.46
67.67
56.53
48.12
40.91
28.87
21.75
17.28
13.94
11.44
9.73
7.23
4.44
2.99
0.93
0.48
Volume VII
Appendix VII-4
External Review Draft
Do Not Cite or Quote
-------
12
6279.70
6763.27
3306.22
1487.99
946.98
678.83
526.62
428.58
359.38
303.33
256.51
221.09
162.21
123.43
98.71
81.63
67.18
58.12
43.26
27.42
18.97
5.53
2.56
39
137.71
103.52
60.24
25.98
14.68
9.24
6.45
4.78
3.64
2.91
2.39
2.00
1.35
1.00
0.76
0.59
0.50
0.41
0.30
0.19
0.13
0.04
0.02
13
133..14
92.18
48.59
20.75
10.96
7.05
4.85
3.53
2.77
2.19
1.78
1.49
1.01
0.73
0.55
0.44
0.36
0.30
0.22
0.13
0.09
0.03
0.01
40
112.50
141.45
130.04
72.78
43.91
29.18
20.71
15.41
11.84
9.69
7.81
6.66
4.56
3.34
2.55
2.04
1.68
1.39
1.04
0.64
0.44
0.14
0.07
14
224.16
188.93
115.88
51.86
29.11
18.37
12.83
9.58
7.47
5.88
4.84
4.02
2.76
1.99
1.52
1.23
0.99
0.83
0.60
0.36
0.24
0.08
0.04
41
37.08
80.70
128.86
113.97
81.29
58.88
43.80
33.43
26.90
21.95
18.04
15.37
10.68
7.92
6.05
4.94
4.04
3.40
2.53
1.55
1.06
0.34
0.18
15
214.24
304.18
293.89
165.02
98.65
63.97
45.13
33.74
26.02
20.30
17.08
13.98
9.49
6.88
5.38
4.29
3.43
2.90
2.08
1.24
0.84
0.26
0.13
42
0.13
2.77
41.62
119.55
117.04
100.58
83.57
69.25
57.61
48.12
41.53
35.34
25.40
19.24
15.29*
12.36
10.07
8.65
6.44
4.04
2.73
0.86
0.44
16
142.89
391.73
531.14
370.75
230.16
152.36
107.75
80.23
61.61
49.34
40.83
33.86
22.86
16.81
13.10
10.33
8.26
6.91
4.95
2.98
2.01
0.60
0.31
43
100.85
113.65
88.27
46.53
27.26
18.06
12.71
9.33
7.45
5.93
4.90
4.08
2.79
2.02
1.59
1.27
1.03
0.87
0.64
0.40
0.28
0.09
0.05
17
96.19
910.76
1515.31
891.63
505.59
332.65
235.97
175.55
138.05
112.63
91.65
78.56
54.58
40.54
31.11
23.96
19.80
16.18
11.52
7.13
4.83
1.46
0.73
44
37.27
66.35
89.20
72.80
50.29
35.92
26.41
20.58
16.45
13.14
11.16
9.24
6.46
4.82
3.79
3.01
2.50
2.09
1.53
0.97
0.68
0.22
0.12
Volume VII
Appendix VII-4
External Review Draft
Do Not Cite or Quote
-------
18
78.93
4889.99
4110.25
1681.69
990.89
688.97
519.15
414.02
340.55
283.95
246.74
214.38
159.23
119.04
92.75
76.26
62.45
53.44
39.91
24.65
16.98
5.10
2.44
45
92.23
96.74
73.24
37.52
22.14
14.46
10.28
7.66
5.81
4.79
3.
3.
,85
,30
2.27
1,
1,
1.
66
,25
02
0.82
0.70
0.52
0.32
0.22
0.07
0.04
19
113.59
77.77
41.23
17.33
9.29
5.93
4.08
2.96
2.30
1.83
1.46
1.24
0.84
0.61
0.46
0.37
0.30
0.25
0.18
0.11
0.07
0.02
0.01
46
36.88
61.38
78.32
59.89
41.13
29.14
21.57
16.45
13.10
10.76
8.78
7.52
5.22
3.83
2.99
2.43
1.96
1.68
1.24
0.78
0.54
0.18
0.10
20
196.26
159.57
96.00
43.53
23.84
15.33
10.64
7.83
6.17
4.89
3.98
3.33
2.28
1.66
1.25
1.02
0.83
0.70
0.51
0.30
0.21
0.07
0.03
47
34.01
51.05
59.31
42.21
28.23
19.77
14.41
11.00
8.86
7.03
5.96
4.89
3.43
2.58
2.01
1.59
1.33
1.11
0.83
0.51
0.36
0.12
0.07
21
153.22
219.72
217.66
127.82
77.68
50.49
35.84
27.07
21.07
16.54
13.81
11.40
7.85
5.67
4.40
3.54
2.84
2.42
1.76
1.04
0.70
0.22
0.11
48
30.41
43.25
47.27
32.54
21.67
15.07
11.01
8.32
6.61
5.38
4.39
3.75
2.61
1.92
1.50
1.21
0.98
0.84
0.62
0.39
0.27
0.09
0.05
22
67.49
197.00
310.40
252.64
170.33
117.57
85.07
64.47
50.13
40.00
33.27
27.23
18.78
13.78
10.83
8.62
6.94
5.85
4.19
2.52
1.70
0.52
0.27
49
349.00
241.29
127.00
53.44
28.32
18.06
12.42
9.00
7.04
5.56
4.42
3.69
2.45
1.74
1.31
1.05
0.82
0.69
0.50
0.29
0.20
0.06
0.03
23
'1.94
62.36
533.42
583.34
406.39
283.54
205.62
154.78
120.70
98.65
80.33
68.29
46.99
34.80
26.95
21.28
17.38
14.31
10.27
6.25
4.23
1.27
0.65
50
1105.73
694.13
339.34
139.34
74.70
48.21
33.56
24.55
19.37
15.32
12.32
10.23
6.85
4.87
3.71
2.94
2.31
1.97
1.41
0.84
0.57
0.16
0.08
Volume VII
Appendix VII-4
External Review Draft
Do Not Cite or Quote
-------
24
0.00
77.85
3564.67
1889.01
1051.39
707.83
520.24
406.11
328.39
270.46
233.30
.199.89
147.58
113.91
86.81
70.81
57.86
48.81
36.31
21.98
15.05
4.55
2.24
51
1825.46
1153.39
608.51
287.20
172.10
117.01
85.60
66.09
52.44
41.72
34.87
29.07
20.00
14.60
11.46
9.03
7.39
6.13
4.39
2.69
1.80
0.52
0.24
25
175.51
139.67
84.30
37.55
20.53
13.23
9.19
6.73
5.25
4.20
3.38
2.87
1.95
1.42
1.08
0.87
0.71
0.59
0.44
0.26
' 0.18
0.06
0.03
52
2856.08
1826.44
1051.41
519.04
326.88
226.75
169.92
132.13
105.63
84.48
72.00
59.86
42.07
32.10
25.07
19.52
16.45
13.37
9.96
5.88
3.97
1.12
0.53
26
133.60
179.50
180.96
106.12
64.20
42.22
29.92
22.52
17.72
14.04
11.61
9.66
6.62
4.81
3.71
2.99
2.41
2.05
1.51
0.90
0.61
0.19
0.10
53
3801.56
2573.77
1547.47
807.94
539.34
390.98
293.63
232.27
188.04
155.67
133.46
114.95
83.42
63.77
49.56
40.51
33.21
28.30
20.95
12.85
8.66
2.37
1.06
27
51.41
133.36
217.24
188.45
132.40
93.00
68.30
52.49
41.35
32.79
27.57
22.72
15.78
11.54
9.08
7.28
5.84
5.00
3.65
2.17
1.47
0.46
0.23
54
5314.38
3891.35
2532.95
1477.99
1034.23
774.63
604.16
488.84
401.77
346.16
295.76
261.73
195.76
151.82
121.69'
101.26
84.15
72.16
52.93
33.10
22.17
6.00
2.81
Volume VII
Appendix V1I-4
External Review Draft
Do Not Cite or Quote
-------
X,n Max concentration, ppm
25.00
50.00
100.00
200.00
300.00
400.00
500.00
600.00
700.00
800.00
900.00
1000.00
1250.00
1500.00
1750.00
2000.00
2250.00
2500.00
3000.00
4000.00
5000.00
10000.00
15000.00
8087.54
6763.27
4110.25
1893.05
1113.48
774.63
604.16
488.84
401.77
346.16
295.76
261.73
195.76
151.82
121.69
101.26
84.15
72.16
52.93
33.10
22.17
6.00
2.81
Concentration (ppm)
Distance to (n)
LOG
JDLH
9.9000
49.1000
8793.28
3193.13
Volume VH
Appendix VII-4
External Review Draft
Do Not Cite or Quote
-------
From Slab output file:
Scenario:
Accident Location:
/ Duration:
v Meteorology:
Chemical:
Vapor phase mole fraction:
LOG:
IDLH:
*Output adjusted to be distance from
X,m
25.00
50.00
100.00
200.00
300.00
400.00
500.00
600.00
700.00
800.00
900.00
1000.00
1250.00
1500.00
1750.00
2000.00
2250.00
2500.00
3000.00
4000.00
5000.00
10000.00
15000.00
20000.00
X,ffl
25.00
50.00
100.00
200.00
300.00
400'. 00
500.00
600.00
700.00
800.00
900.00
1000.00
1250.00
1500.00
1750.00
2000.00
2250.00
2500.00
3000.00
4000.00
5000.00
10000.00
15000.00
20000.00
2,
1.
1
118.24
82.50
44.84
19.15
10.44
6.56
4.54
3.37
2.60
,00
,62
1.32
0.89
0.62
0.48
0.38
0.31
0.26
0.18
0.11
0.08
0.02
0.01
0.01
28
0.11
5.35
105.22
178.75
154.22
117.95
90.39
70.30
55.42
46.06
38.08
32.48
22.62
16.54
12.55
9.69
8.01
6.58
4.71
2.92
1.99
0.62
0.32
0.20
— «• — --
:e f rojn
2
235.73
195.48
118.75
52.40
29.42
18.38
12.81
9.44
7.20
5.52
4.57
3.69
2.48
1.81
1.39
1.07
0.88
0.72
0.51
0.32
0.22
0.07
0.03
0.02
29
0.00
0.01
775.35
992.64
582.63
384.54
277.28
213.59
170.98
139.25
117.75
97.71
68.00
50.13
39.86
32-37
26.55
22.68
16.75
10.58
7.31
2.25
1.11
0.67
RUN52.0UT
CONSERV
ON-SITE
MITIGAT
WORST
HCL
1.000
9.900
49.100
fenceline.
3
1109.99
799.39
409.30
159.22
90.33
57.33
40.23
29.74
22.61
17.55
14.58
11.87
8.05
5.92
4.52
3.47
2.90
2.34
1.73
1.04
0.70
0.21
0.10
0.06
30
88.97
70.38
42.18
18.58
10.33
6.64
4.62
3.38
2.60
2.11
1.68
1.44
0.98
O.Tl
0.54
0.43
0.35
0.29
0.21
0.12
0.08
0.03
0.01
0.01
4
2052.56
1324.15
654.07
274.88
161.19
107.96
76.75
57.35
44.14
35.81
29.49
24.86
17.14
12.72
9.70
7.83
6.38
5.35
3.93
2.38
1.62
0.47
0.23
0.14
31
68.82
88.87
89.36
52.20
31.07
20.85
14.78
10.90
8.69
6.95
5.64
4.80
3.31
2.40
1.82
1.47
1.17
0.98
0.71
0.42
0.29
0.09
0.05
0.03
5
2872.74
1725.89
875.08
413.12
254.83
178.53
130.11
99.78
79.85
66.73
55.20
48.05
34.36
25.83
20.57
16.71
13.69
11.65
8.55
5.35
3.62
1.06
0.49
0.29
32
24.68
59.25
96.26
86.13
61.55
43.70
32.33
25.13
20.01
16.01
13.44
11.26
7.83
5.71
4.34
3.47
2.74
2.33
1.68
1.02
0.70
0.22
0.12
0.07
Volume VII
Appendix VII-4
External Review Draft
Do Not Cite or Quote
-------
6
4070.16
2527.86
1397.32
717.40
470.09
338.22
261.44
214.77
180.42
152.35
'134.48
117.13
89.81
71.87
58.13
48.35
40.73
34.91
26.33
16.49
11.30
3.13
1.39
0.79
33
0.03
3.16
49.50
118.18
109.65
89.17
71.02
56.86
45.85
38.29
32.16
27.39
19.29
14.44
11.14
8.68
,07
.88
4.24
2.60
1.78
0.56
0.29
.0.18
7
5
7
89.59
63.13
34.26
14.53
7.89
4.97
3.43
2.54
1.98
1.55
1.26
1.03
0.68
0.48
0.37
0.29
0.23
0.20
0.14
0.09
0.06
0.02
0.01
0.01
34
0.00
0.00
40.05
767.08
565.99
382.34
274.82
209.97
166.73
134.92
114.21
96.20
66.68
48.86
37.83
30.60
24.59
21.07
15.58
9.70
6.69
2.08
1.03
0.63
8
154.00
131.88
82.54
37.33
21.16
13.29
9.33
7.00
5.43
4.24
3.50
2.84
1.89
1.34
1.05
0.82
0.66
0.55
0.40
0.24
0.17
0.05
0.03
0.02
35
81.90
63.35
37.63
16.37
9.22
5.90
4.11
3.03
2.29
1.86
1.51
1.27
0.86
0.63
0.48
0.38
0.32
0.26
0.19
0.11
0.08
0.03
0.01
0.01
9
273.09
332.75
266.55
129.90
74.16
47.19
32.89
24.42
18.63
14.36
11.80
9.44
6.34
4.65
3.55
2.73
2.25
1.84
1.32
0.81
0.55
0.17
0.09
0.05
36
64.86
82.84
79.96
46.06
27.68
18.45
13.12
9.72
7.61
6.17
4.97
4.26
2.92
2.14
1.62
1.29
1.04
0.86
0.63
0.37
0.25
0.08
0.04
0.03
10
586.08
768.00
618.73
286.01
159.70
102.93
72.34
53.93
41.32
32.63
26.49
21.71
14.69
10.68
8.12
6.26
5.24
4.23
3.13
1.88
1.28
0.40
0.20
0.12
37
22.13
50.32
83.06
73.39
52.47
37.77
28.07
21.60
17.39
14.08
11.73
9.90
6.86
5.05
3.87
3.11
2.49
2.10
1.52
0.91
0.62
0.20
0.11
0.07
11
1470.49
1910.00
1111.16
465.04
264.91
180.35
130.77
96.96
75.92
61.86
50.10
43.14
30.05
22.18
17.18
13.97
11.14
9.61
7.05
4.39
3.01
0.90
0.44
0.26
38
0.07
2.13
31.41
85.98
82.99
70.05
57.30
46.86
38.48
32.15
27.37
23.27
16.40
12.43
9.68
7.64
6.20
5.20
3.75
2.31
1.58
0.51
0.26
0.16
Volume VII
Appendix VII-4
External Review Draft
Do Not Cite or Quote
-------
12
3253.49
3429.95
1663.11
752.57
479.74
335.18
252.45
202.13
165.96
139.34
121.29
105.93
79.27
62.57
50.34
41.76
35.28
30.28
23.02
14.43
9.95
2.91
1.34
0.77
39
76.64
57.84
33.95
14.78
8.33
5.27
3.68
2.74
2
1
.08
.67
1.37
1.15
0.78
0.57
0.44
0.34
0.29
0.23
0.17
0.10
0.07
0.02
0.01
0.01
13
74.33
51.77
27.39
11.75
6.24
4.01
2.76
2.01
1.58
1.25
1.01
0.85
0.57
0.40
0.30
0.24
0.19
0.16
0.12
0.07
0.05
0.01
0.01
0.01
40
62.90
79.50
73.20
41.32
24.98
16.62
11.83
8.80
6.76
5.54
4.47
3.81
2.61
1.91
1.46
1.17
0.96
0.78
0.57
0.34
0.23
0.08
0.04
0.03
14
125.00
105.86
65.13
29.35
16.54
10.47
7.30
5.46
4.26
3.35
2.77
2.29
1.53
1.08
0.84
0.66
0.53
0.45
0.32
0.20
0.13
0.04
0.02
0.01
41
21.01
45.71
73.22
64.81
46.34
33.61
25.05
19.13
15.39
12.55
10.31
8.80
6.13
4.54
3.47
2.82
2.30
1.92
1.39
0.82
0.56
0.18
0.10
0.06
15
120.21
170.30
165.10
92.74
55.69
36.09
25.48
19.07
14.74
11.56
9.72
7.95
5.27
3.76
2.90
2.27
1.82
1.52
1.09
0.67
0.46
0.14
0.07
0.05
42
0.08
1.57
23.75
68.43
66.72
57.36
47.58
39.43
32.82
27.44
23.68
20.13
14.47
10.99
8.74
7.01
5.60
4.75
3.44
2.10
1.44
0.46
0.24
0.15
16
80.78
221.13
296.65
206.21
128.44
84.83
60.20
44.99
34.60
27.77
22.81
18.60
12.23
8.90
6.81
5.27
4.36
3.56
2.54
1.58
1.07
0.34
0.17
0.11
43
56.24
63.60
49.98
26.43
15.54
10.26
7.27
5.34
4.27
3.40
2.81
2.34
1.60
1.15
0.91
0.73
0.59
0.50
0.37
0.23
0.16
0.05
0.03
0.02
17
54.04
507.66
821.77
477.49
271.98
179.11
127.86
95.61
75.32
60.75
48.36
41.00
27.91
20.35
15.30
12.19
9.95
8.33
6.12
3.70
2.52
0.77
0.39
0.24
44
21.14
37.64
50.67
41.53
28.74
20.54
15.09
11.76
9.42
7.54
6.40
5.30
3.70
2.76
2.17
1.72
1.44
1.20
0.88
0.55
0.38
0.12
0.06
0.04
Volume
Appendix VII-4
External Review Draft
Do Not Cite or Quote
-------
18
43.93
2622.17
2101.31
857.95
504.94
352.66
267.22
208.85
167.18
137.05
118.02
. 99.79
72.90
57.11
45.98
37.13
31.74
26.50
20.25
12.67
8.70
2.60
1.25
0.72
45
51.53
54.32
41.42
21.33
12.58
8.23
5.86
4.38
3.33
2.74
2.20
1.89
1.30
0.95
0.72
0.59
0.47
0.40
0.30
0.18
0.13
0.04
0.02
0.01
19
63.76
43.74
23.25
9.80
5.28
3.37
,32
2
1,
68
1.31
1.04
0.84
0.71
0.48
0.35
0.25
0.20
0.16
0.14
0.10
0.06
0.04
0.01
0.01
0.00
46
20.92
34.80
44.54
34.21
23.53
16.70
12.36
9.42
7.48
6.14
5.03
4.31
3.00
2.20
1.71
1.39
1.12
0.96
0.71
0.45
0.31
0.10
0.05
0.03
20
110.01
89.34
54.10
24.67
13.55
8.75
6.08
4.47
3.53
2.80
2.28
1.91
1.30
0.93
0.69
0.56
0.44
0.38
0.27
0.17
0.11
0.04
0.02
0.01
47
19.27
28.94
33.73
24.04
16.16
11.34
8.27
6.30
5.07
4.03
3.42
2.80
1.97
1.48
1.15
0.91
0.76
0.63
0.48
0.29
0.21
0.07
0.04
0.02
21
85.73
123.56
122.29
71.94
43.93
28.68
20.31
15.40
12.01
9.43
7.88
6.51
4.47
3.16
2.43
1.91
1.50
1.28
0.92
0.56
0.38
0.12
0.06
0.04
48
17.23
24.58
26.90
18.55
12.40
8.62
6.30
4.76
3.79
3.08
2.51
2.15
50
10
0.86
0.69
0.56
0.48
0.35
0.22
0.16
0.05
0.03
0.02
1.
1.
22
38.12
111.76
175.40
142.22
96.41
66.29
48.04
36.44
28.36
22.66
18.85
15.43
10.43
7.51
5.79
4.51
3.65
3.02
2.16
1.34
0.91
0.29
0.15
0.09
49
193.53
134.17
70.95
29.98
15.93
10.19
6.85
4.86
3.80
2.96
2.41
1.97
1.30
0.93
0.72
0.56
0.45
0.37
0.26
0.16
0.11
0.03
0.02
0.01
23
1.09
35.20
300.31
322.80
225.10
156.67
113.86
85.84
67.18
55.03
44.92
38.23
25.74
18.68
14.14
10.85
9.03
7.32
5.37
3.27
2.23
0.70
0.35
0.22
50
590.72
371.11
182.43
75.85
41.02
25.79
17.59
12.93
10.07
7.80
6.46
5.23
3.52
2.59
1.99
1.53
1.27
1.03
0.76
0.45
0.30
0.09
0.04
0.03
Volume
Appendix VII-4
External Review Draft
Do Not Cite or Quote
-------
24
0.00
43.60
1877.08
970.06
542.38
365.74
270.14
211.75
170.17
136.61
116.31
97.20
69.72
53.05
42.49
34.28
28.71
24.18
17.95
11.50
7.97
2.43
1.16
0.70
51
922.02
585.44
310.32
148.33
87.31
57.55
41.88
32.54
25.73
20.82
17.47
14.76
10.34
7.72
5.90
4.79
3.89
3.28
2.41
1.46
0.98
0.28
0.13
0.08
25
97.89
78.29
47.54
21.28
11.67
7.55
5.25
3.84
3.00
2.40
1.93
1.65
1.12
0.81
0.60
0.48
0.39
0.33
0.24
0.14
' 0.10
0.03
0.02
0.01
52
1435.20
922.18
531.67
263.28
158.96
109.30
81.59
63.78
50.57
42.59
35.34
30.81
21.98
16.37
12.84
10.43
8.49
7.22
5.23
3.22
2.14
0.60
0.27
0.16
26
74.59
100.70
102.10
60.11
36.40
23.96
16.98
12.84
10.11
8.01
6.64
5.53
3.78
2.75
2.06
1.65
1.30
1.10
0.80
0.48
0.33
0.10
0.06
0.04
53
1905.78
1295.98
780.35
407.12
262.09
186.00
141.95
112.93
92.05
78.78
66.34
58.44
42.80
32.45
26.44
21.33
17.93
14.86
10.98
6.60
4.44
1.21
0.55
0.30
27
29.08
75.55
123.12
106.27
74.86
52.73
38.82
29.88
23.53
18.59
15.66
12.93
8.99
6.38
4.97
3.92
3.13
2.63
1.90
1.16
0.79
0.25
0.13
0.08
54
2662.19
1950.68
1266.48
757.34
520.49
389.23
306.74
249.22
212.16
180.98
158.55.
138.35
103.53
83.24
67.18
55.06
46.35
39.36
29.50
18.11
12.14
3.21
1.38
0.79
Volume VII
Appendix VII-4
External Review Draft
.Do Not Cite or Quote
-------
X,m Max concentration, ppn
25.00
50.00
100.00
200.00
300.00
400.00
500.00
600.00
700.00
800.00
900.00
1000.00
1250.00
1500.00
1750.00
2000.00
2250.00
2500.00
3000.00
4000.00
5000.00
10000.00
15000.00
20000.00
4070.16
3429.95
2101.31 ------
992.64
582.63
389.23
306.74
249.22
212.16
180.98
158.55
138.35
103.53
83.24
67.18
55.06
46.35
39.36
29.50
18.11
12.14
3.21
1.39
0.79
Concentration (ppm)
Distance to (m)
LOG
IDLH
9.9000
49.1000
6254.60
2171.13
Volume VII
Appendix VII-4
External Review Draft
Do Not Cite or Quote
-------
From Slab output file:
Scenario:
Accident Location:
Duration:
Meteorology:
Chemical:
Vapor phase mole fraction:
LOG:
IDLH:
RUN53.OUT
CONSERV
ON-SITE
UNMITIG
INVERSN
HCL
1
000
9.900
49.100
*Output adjusted to be distance from fenceline.
X,m Max concentration, ppm
25.00
50.00
100.00
200.00
300.00
400.00
500.00
600.00
700.00
800.00
900.00
1000.00
1250.00
1500.00
'' \ 1750.00
2000.00
- ^ 2250.00
2500.00
3000.00
4000.00
5000'. 00
10000.00
15000.00
20000. 00
6922
5380
3699
2196
1539
1166
917
759.
641
549
477
423
321
250
206
170
146
122
95
60
42
12
6
3
.40
.31
.98
.71
.06
.96
.96
.06
.81
.87
.37
.41
.14
.66
.91
.55
.00
.98
.13
.26
.33
.83
.18
.60
Concentration (ppm)
LOG
IDLH
9.9000
49.1000
Distance to (m)
12204.31
4622.65
Volume VII
Appendix VII-4
External Review Draft
Do Not Cite or Quote
-------
From Slab output file:
Scenario:
Accident Location:
Duration:
Meteorology:- -»--_-
Chemical:
Vapor phase mole fraction:
LOG:
IDLH:
*Output adjusted to be distance from fenceline.
X,m Max concentration, ppm
RUN54.OUT
CONSERV
ON-SITE
MITIGAT
INVERSN
HCL
1
000
9.900
49.100
25.00
50.00
100.00
200.00
300.00
400.00
500.00
600.00
700.00
800.00
900.00
1000.00
1250.00
1500.00
1750.00
2000.00
2250.00
2500.00
3000.00
4000.00
5000.00
10000.00
15000.00
20000.00
3914.84
3051.54
2133.12
1277.65
915.36
698.19
553.50
465.95
389.78
339.32
290.62
261.54
197.50
153.22
126.38
102.52
88.40
74.27
57.16
35.67
24.63
7.06
3.31
1.91
Concentration (ppm)
LOG
IDLH
9.9000
49.1000
Distance to (m)
9191.12
3375.25
Volume VH
Appendix VII-4
External Review Draft
Do Not Cite or Quote
-------
From Slab output file:
Scenario:
Accident Location: ON- SITE
Acciaen UNMITIG
Meteorology: ----_.- TYPICAL
Chemical: HCL
Vapor phase mole fraction: 1
IDLH! 49.100
'Output adjusted to be distance from -fencelme.
X,m Max concentration, ppm
25.00
50.00
100.00
200.00
300.00
400.00
500.00
' 600.00
700.00
800.00
900.00
1000.00
1250.00
1500.00
-— x 1750.00
2000.00
_/ 2250.00
2500.00
3000.00
4000.00
5000.00
27.52
19.71
11.40
5.39
3.13
2.10
1.51
1.13
0.88
0.72
0.60
0.50
0.34
0.25
0.19
0.15
0.12
0.10
0.07
0.05
0.03
-Concentration (ppm) -
LOG9.9000 125.02
IDLH 49.1000 less than -25.00
Volume VII External Review Draft
Appendix VH-4 Do Not cite or
-------
From Slab output file: RUN56.0UT
Scenario: TYPICAL
Accident Location: ON-SITE
Duration: MITIGAT
Meteorology: ----_- TYPICAL
Chemical: HCL
Vapor phase mole fraction: 1.000
LOC: 9.900
IDLH: 49.100
*0utput adjusted to be distance from fenceline.
X,m Max concentration, ppm
25.00
50.00
100.00
200.00
300.00
400.00
500.00
'600.00
700.00
800.00
900.00
1000.00
1250.00
1500.00
1750.00
2000.00
2250.00
2500.00
3000.00
4000.00
5000.00
27.52
19.71
11.40
5.39
3.13
2.10
1.51
1.13
0.88
0.72
0.60
0.50
0.34
0.25
0.19
0.15
0 .-12
0.10
0.07
0.05
0.03
•Concentration (ppm) Distance to (m)
LOC 9.9000 125.02
IDLH 49.1000 less than 25.00
Volume VH External Review Draft
Appendix VH-4 D0 Not Cite or Quote
-------
From Slab output file:
Scenario:
Accident Location:
Duration:
Meteorology:
Chemical:
Vapor phase mole fraction:
LOG:
IDLH:
*Output adjusted to be distance from
X,m
25.00
50.00
100.00
200.00
300.00
400.00
500.00
600.00
700.00
800.00
900.00
1000.00
1250.00
1500.00
1750.00
2000.00
2250.00
2500.00
3000.00
4000.00
X,m
25.00
50.00
100.00
200.00
300.00
400.00
500.00
600.00
700.00
800.00
900.00
1000.00
1250.00
1500.00
1750.00
2000.00
2250.00
2500.00
3000.00
4000.00
1
4.36
2.96
1.59
0.69
0.38
0.25
0.17
0.13
0.09
0.08
0.06
0.05
0.03
0.02
0.02
0.01
0.01
0.01
0.01
0.00
28
52.24
38.13
22.70
11.07
6.58
4.46
3.24
2.46
1.92
1.59
1.31
1.09
0.73
0.54
0.41
0.32
0.27
0.22
0.16
0.10
- ** — _.-
e from
2
10.38
7.16
3.92
1.75
0.98
0.64
0.45
0.32
0.24
0.20
0.16
0.13
0.09
0.07
0.05
0.04
0.03
0.03
0.02
0.01
29
154.85
117.55
74.27
38.84
24.00
16.72
12.20
8.92
6.86
5.59
4.48
3.87
2.67
1.94
1.51
1.22
1.00
0.84
0.61
0.39
RDN57.ODT
TYPICAL
ON-SITE
DNMITIG
WORST
HCL
1.000
9.900
49.100
fence line.
3
29.27
20.65
11.71
5.41
3.09
2.03
1.40
1.02
0.78
0.63
0.50
0.43
0.29
0.21
0.16
0.13
0.10
0.09
0.06
0.04
30
3.89
2.69
1.47
0.66
0.37
0.24
0.17
0.13
0.10
0.08
0.06
0.05
0.04
0.03
0.02
0.02
0.01
0.01
0.01
0.00
4
60.80
43.78
25.43
12.07
7.01
4.48
3.11
2.27
1.78
1.42
1.15
0.97
0.66
0.48
0.37
0.30
0.24
0.20
0.15
0.09
31
10.58
7.48
4.21
1.95
1.12
0.74
0.53
0.39
0.30
0.25
0.20
0.17
0.12
0.09
0.07
0.05
0.04
0.04
0.03
0.02
5
117.61
86.89
52.44
26.18
14.84
9.72
6.81
5,
4.
3,
07
03
,17
2.68
2.19
1.49
1.13
0.87
0.67
0.57
0.46
0.34
0.20
32
21.93
15.74
9.05
4.29
2.49
1.66
1.20
0.90
0.70
0.58
0.47
0.40
0.28
0.20
0.16
0.12
0.10
0.08
0.06
0.04
Volume VH
Appendix VII-4
External Review Draft
Do Not Cite or Quote
-------
7
5
3
3
2
6
235.68
183.07
121.80
60.68
38.36
26.76
20.08
15.53
12.49
10.32
8.63
30
09
88
02
37
1.97
1.63
1.19
0.71
33
45.54
33.28
19.77
9.63
5.72
3.89
2.82
2.14
1.67
1.38
1.14
0.97
0.66
0.48
0.37
0.29
0.24
0.20
0.14
0.09
7
3.27
2.22
1.19
0.52
0.29
0.19
0.13
0.10
0.07
0.06
0.05
0.04
0.03
0.02
0.01
0.01
0.01
0.01
0.01
0.00
34
136.66
103.87
65.20
33.98
20.97
14.60
10.80
8.23
6.21
5.08
4.09
3.50
2.40
1.76
1.34
1.10
0.88
0.76
0.56
0.35
8
7.77
5.38
2.95
1.31
0.73
0.48
0.34
0.25
0.19
0.15
0.12
0.10
0.07
0.05
0.04
0.03
0.02
0.02
0.01
0.01
35
3.46
2.39
1.31
0.58
0.33
0.21
0.15
0.11
0.08
0.07
0.06
0.05
0.03
0.02
0.02
0.01
0.01
0.01
0.01
O.-OO
9
21.64
15.24
8.60
3.98
2.28
1.51
1.08
0.80
0.60
0.49
0.39
0.33
0.22
0.16
0.12
0.10
0.08
0.07
0.05
0.03
36
9.43
6.64
3.75
1.73
0.99
0.66
0.47
0.35
0.27
0.22
0.18
0.15
0.11
0.08
0.06
0.05
0.04
0.03*
0.02
0.01
10
45.07
32.37
18.77
8.88
5.16
3.45
2.45
1.79
1.36
1.10
0.88
0.75
0.51
0.37
0.28
0.23
0.18
0.15
0.11
0.07
37
19.49
13.91
8.03
3.80
2.21
1.48
1.06
0.80
0.62
0.51
0.42
0.35
0.25
0.18
0.14
0.11
0.09
0.08
0.06
0.03
11
92.36
67.87
40.65
20.05
11.89
7.98
5.54
4.05
3.14
2.53
2.04
1.74
1.19
0.86
0.67
0.54
0.43
0.37
0.27
0.17
38
40.37
29.43
17.45
8.54
5.06
3.44
2.50
1.90
1.48
1.22
1.01
0.86
0.60
0.44
0.34
0.26
0.22
0.18
0.13
0.08
Volume VH
Appendix VIM
External Review Draft
Do Not Cite or Quote
-------
12
223.63
171.20
110.80
58.96
33.96
22.99
16.78
13.08
10.30
8.44
7.01
6.01
4.24
3.13
2.42
1.96
1.59
1.34
0.96
^ 0.59
39
, 3.11
^ 2.15
1.18
0.53
0.29
0.19
0.13
0.10
0.08
0.06
0.05
0.04
0.03
0.02
0.02
0.01
0.01
0.01
0.01
0.00
13
2.62
1.78
0.95
0.42
0.23
0.15
0.10
0.08
0.06
0.05
0.04
0.03
0.02
0.02
0.01
0.01
0.01
0.01
0.00
0.00
40
8.47
5.97
3.36
1.56
0.89
0.59
0.42
0.32
0.24
0.20
0.16
0.14
0.09
0.07
0.06
0.04
0.04
0.03
0.02
0.01
14
6.22
4.30
2.35
1.05
0.59
0.38
0.27
0.20
0.15
0.12
0.10
0.08
0.06
0.04
0.03
0.02
0.02
0.02
0.01
0.01
41
17.47
12.55
7.22
3.42
1.99
1.33
0.96
0.72
0.56
0.46
0.38
0.32
0.22
0.17
0.13
0.10
0.08
0.07
0.05
0.03
15
17.17
12.06
6.82
3.15
1.80
1.19
0.85
0.64
0.49
0.40
0.33
0.28
0.18
0.13
0.10
0.08
0.07
0.05
0.04
0.02
42
36.31
26.42
15.64
7.66
4.55
3.08
2.24
1.70
1.33
1.10
0.91
0.77
0.54
0.40
0.30
0.24
0.20
0.16
0.12
0.07
16
35.64
25.51
14.74
6.99
4.06
2.71
1.95
1.47
1.14
0.92
0.74
0.62
0.42
0.31
0.23
0.18
0.15
0.12
0.09
0.06
43
5.32
3.73
2.10
0.97
0.56
0.37
0.26
0.20
0.15
0.12
0.10
0.09
0.06
0.04
0.03
0.03
0.02
0.02
0.01
0.01
17
73.93
54.20
32.28
15.85
9.42
6.39
4.64
3.49
2.63
2.14
1.71
1.45
0.98
0.72
0.55
0.44
0.36
0.30
0.22
0.14
44
10.97
7.84
4.51
2.13
1.24
0.83
0.60
0.45
0.35
0.29
0.24
0.20
0.14
0.10
0.08
0.06
0.05
0.05
0.03
0.02
Volume VII
Appendix VIM
External ReviBW Draft
Do Nw Che Qr
-------
18
201.39
153.60
97.94
52.10
32.56
21.25
15.05
11.13
8.99
7.18
• 6.04
4.99
3.43
2.64
2.04
1.61
1.34
1.12
0.84
0.51
45
4.26
2.99
1.69
0.78
0.44
0.30
0.21
0.16
0.12
0.10
0.08
0.07
0.05
0.04
0.03
0.02
0.02
0.02
0.01
0.01
19
2.18
1.48
0.79
0.35
0.19
0.12
0.09
0.06
0.05
0.04
0.03
0.03
0.02
0.01
0.01
0.01
0.01
0.01
0.00
0.00
46
8.77
6.27
3.60
1.70
0.99
0.66
0.48
0.36
0.28
0.23
0.19
16
11
0.08
0.06
0.05
0.04
0.04
0.03
0.02
0
0
20
5.18
3.58
1.96
0.88
0.49
0.32
0.23
0.17
0.13
0.10
0.09
0.07
0.05
0.04
0.03
0.02
0.02
0.01
0.01
0.01
47
5.86
4.18
2.40
1.14
0.66
0.44
0.32
0.24
0.19
0.15
0.13
0.11
0.07
0.06
0.04
0.03
0.03
0.02
0.02
0.01
21
14.23
10.03
5.64
2.61
1.49
0.99
0.71
0.53
0.41
0.33
0.27
0.23
0.16
0.11
0.09
0.07
0.06
0.05
0.03
0.02
48
4.39
3.13
1.81
0.85
0.49
0.33
0.24
0.18
0.14
0.11
0.09
0.08
0.06
0.04
0.03
0.03
0.02
0.02
0.01
0.01
22
29.44
21.07
12.21
5.77
3.35
2.24
1.61
1.21
0.94
0.77
0.63
0.53
0.35
0.26
0.20
0.16
0.13
0.11
0.08
0.05
49
6.54
4.45
2.39
1.04
0.57
0.36
0.24
0.18
0.13
0.11
0.08
0.07
0.05
0.03
0.03
0.02
0.02
0.01
0.01
0.01
23
61.26
44.81
26.63
13.08
7.75
5.26
,81
90
26
83
,47
,23
,84
3.
2.
2.
1.
1,
1,
0,
0.61
0.47
0.37
0.31
0.25
0.19
0.11
50
15.47
10.69
5.87
2.63
1.47
0.93
0.64
0.47
0.36
0.29
0.23
0.20
0.13
0.10
0.07
0.06
0.05
0.04
0.03
0.02
Volume VII
Appendix VH-4
External Review Draft
Do Not Cite or Quote
-------
24
177.10
135.00
85.35
44.91
27.91
19.17
13.41
9.91
7.79
6.27
5.12
4.34
3.01
2.22
1.76
1.38
1.16
0.95
0.71
N 0.43
51
/ 44.40
31.47
17.87
8.30
4.56
2.93
2.04
1.48
1.17
0.93
0.76
0.63
0.43
0.31
0.24
0.19
0.15
0.13
0.09
0.06
25
4.45
,07
1.69
0.75
. 0.42
0.27
0.19
0.14
0.11
0.09
0.07
0.06
0.04
0.03
0.02
0.02
0.02
0.01
0.01
0.01
52
86.17
62.28
36.62
16.77
9.38
6.08
4.30
3.28
2.54
2.01
1.68
1.40
0.96
0.70
0.53
0.42
0.34
0.29
0.21
0.12
26
12.19
8.56
4.83
2.23
1.27
0.85
0.60
0.45
0.35
0.29
0.23
0.20
0.14
0.10
0.08
0.06
0.05
0.04
0.03
0.02
53
142.85
106.75
66.62
31.20
18.64
12.50
9.12
6.94
5.33
4.45
3.57
3.11
2.14
1.54
1.20
0.95
0.77
0.64
0.45
0.27
27
25.18
17.97
10.40
4.92
2.85
1.91
1.37
1.03
0.80
0.66
0.54
0.46
0.31
0.23
0.17
0.14
0.11
0.09
0.07
0.04
54
206.49
155.77
107.65
63.55
42.95
31.57
24.58
19.60
15.75
13.30
11.04
9.54
6.67
4.93
3.85
2.96
2.49
2.02
1.47
0.84
Volume Vn
Appendix VII-4
External Review Draft
Do Not Cite or Quote
-------
X,m Max concentration, ppm
25.00
50.00
100.00
200.00
300.00
400.00
500.00
600.00
700.00
800.00
900.00
1000.00
1250.00
1500.00
1750.00
2000.00
2250.00
2500.00
3000.00
4000.00
235.68
183.07
121. ao ------
63.55
42.95
31.57
24.58
19.60
15.75
13.30
11.04
9.54
6.67
4.93
3.85
2.96
2.49
2.02
1.47
0.84
Concentration (ppm)
Distance to (m)
9.9000
49.1000
976.22
270.14
Volume VII
Appendix VU-4
External Review Draft
Do Not Cite or Quote
-------
From Slab output file:
Scenario:
Accident Location:
Duration:
Meteorology:
Chemical:
Vapor phase mole fraction:
LOG:
IDLH:
*Output adjusted to be distance from
X,m
25.00
50;00
100.00
200.00
300.00
400.00
500.00
600.00
700.00
800.00
900.00
1000.00
1250.00
1500.00
1750.00
2000.00
2250.00
2500.00
3000.00
4000.00
X,m
25.00
50.00
100.00
200.00
300.00
400.00
500.00
600.00
700.00
800.00
900.00
1000.00
1250.00
1500.00
1750.00
2000.00
2250.00
2500.00
3000.00
4000.00
1
4.36
2.96
1.59
0.69
0.38
0.25
0.17
0.13
0.09
0.08
0.06
0.05
0.03
0.02
0.02
0.01
0.01
0.01
0.01
0.00
28
52.24
38.13
22.70
11.07
6.58
4.46
3.24
2.46
1.92
1.59
1.31
1.09
0.73
0.54
0.41
0.32
0.27
0.22
0.16
0.10
2
10.38
7.16
3.92
1.75
0.98
0.64
0.45
0.32
0.24
0.20
0.16
0.13
0.09
0.07
0.05
0.04
0.03
0.03
0.02
0.01
29
154.85
117.55
74.27
38.84
24.00
16.72
12.20
8.92
6.86
5.59
4.48
3.87
2.67
1.94
1.51
1.22
1.00
0.84
0.61
0.39
RUN58.0DT
TYPICAL
ON-SITE
MITIGAT
WORST
HCL
1.000
9.900
49.100
fenceline.
3
29.27
20.65
11.71
5.41
3.09
2.03
1,
1,
.40
.02
0.78
0.63
0.50
0.43
0.29
0.21
0.16
0.13
0.10
0.09
0.06
0.04
30
3.89
2.69
1.47
0.66
0.37
0.24
0.17
0.13
0.10
0.08
0.06
0.05
0.04
0.03
0.02
0.02
0.01
0.01
0.01
0.00
4
60.80
43.78
25.43
12.07
7.01
4.48
3.11
2.27
1.78
1.42
1.15
0.97
0.66
0.48
0.37
0.30
0.24
0.20
0.15
0.09
31
10.58
7.48
4.21
1.95
1.12
0.74
0.53
0.39
0.30
0.25
0.20
0.17
0.12
0.09
0.07
0.05
0.04
0.04
0.03
0.02
5
117.61
86.89
52.44
26.18
14.84
9.72
6.81
5.
4.
07
03
3.17
2.68
2.19
1.49
1.13
0.87
0.67
0.57
0.46
0.34
0.20
32
21.93
15.74
9.05
4.29
2.49
1.66
1.20
0.90
0.70
0.58
0.47
0.40
0.28
0.20
0.16
0.12
0.10
0.08
0.06
0.04
Volume Vn
Appendix VII-4
External Review Draft
Do Not Cite or Quote
-------
5
3
3
6
235.68
183.07
121.80
60.68
38.36
26.76
20.08
15.53
12.49
10.32
8.63
7.30
.09
.88
.02
2.37
1.97
1.63
1.19
0.71
33
45.54
33.28
19.77
9.63
5.72
3.89
2.82
2.14
1.67
1.38
1.14
0.97
0.66
0.48
0.37
0.29
0.24
0.20
0.14
0.09
7
3.27
2.22
1.19
0.52
0.29
0.19
0.13
0.10
0.07
0.06
0.05
0.04
0.03
0.02
0.01
0.01
0.01
0.01
0.01
0.00
34
136.66
103.87
65.20
33.98
20.97
14.60
10.80
8.23
6.21
5
4
08
09
3.50
2.40
1.76
1.34
1.10
0.88
0.76
0.56
0.35
8
7.77
5.38
2.95
1.31
0.73
0.48
0.34
0.25
0.19
0.15
0.12
0.10
0.07
0.05
0.04
0.03
0.02
0.02
0.01
0.01
35
3.46
2.39
1.31
0.58
0.33
0.21
0.15
0.11
0.08
0.07
0.06
0.05
0.03
0.02
0.02
0.01
0.01
0.01
0.01
O.Ot)
9
21.64
15.24
8.60
3.98
2.28
1.51
1.08
0.80
0.60
0.49
0.39
0.33
0.22
0.16
0.12
0.10
0.08
0.07
0.05
0.03
36
9.43
6.64
3.75
1.73
0.99
0.66
0.47
0.35
0.27
0.22
0.18
0.15
0.11
0.08
0.06
0.05
0.04
0.03*
0.02
0.01
10
45.07
32.37
18.77
8.88
5.16
3.45
2.45
1.79
1.36
1.10
0.88
0.75
0.51
0.37
0.28
0.23
0.18
0.15
0.11
0.07
37.
19.49
13.91
8.03
3.80
2.21
1.48
1.06
0.80
0.62
0.51
0.42
0.35
0.25
0.18
0.14
0.11
0.09
0.08
0.06
0.03
11
92.36
67.87
40.65
20.05
11.89
7.98
5.54
4.05
3.14
2.53
2.04
1.74
1.19
0.86
0.67
0.54
0.43
0.37
0.27
0.17
38
40.37
29.43
17.45
8.54
5.06
3.44
2.50
1.90
1.48
1.22
1.01
0.86
0.60
0.44
0.34
0.26
0.22
0.18
0.13
0.08
Volume VH
Appendix VH-4
External Review Draft
Do Not Cite or Quote
-------
12
223.63
171.20
110.80
58,96
33.96
22.99
16.78
13.08
10.30
8.44
7.01
6.01
4.24
3.13
2.42
1.96
1.59
1.34
0.96
0.59
39
3.11
2.15
1.18
0.53
0.29
0.19
0.13
0.10
0.08
0.-06
0.05
0.04
0.03
0.02
0.02
0.01
0.01
0.01
0.01
0.00
13
2.62
1.78
0.95
0.42
0.23
0.15
0.10
0.08
0.06
0.05
0.04
0.03
0.02
0.02
0.01
0.01
0.01
0.01
0.00
0.00
40
8.47
5.97
3.36
1.56
0.89
0.59
0.42
0.32
0.24
0.20
0.16
0.14
0.09
0.07
0.06
0.04
0.04
0.03
0.02
0.01
14
6.22
4.30
2.35
1.05
0.59
0.38
0.27
0.20
0.15
0.12
0.10
0.08
0.06
0.04
0.03
0.02
0.02
0.02
0.01
0.01
41
17.47
12.55
7.22
3.42
1.99
1.33
0.96
0.72
0.56
0.46
0.38
0.32
0.22
0.17
0.13
0.10
0.08
0.07
0.05
O.JD3
15
17.17
12.06
6.82
3.15
1.80
1.19
0.85
0.64
0.49
0.40
0.33
0.28
0.18
0.13
0.10
0.08
0.07
0.05
0.04
0.02
42
36.31
26.42
15.64
7.66
4.55
3.08
2.24
1.70
1.33
1.10
0.91
0.77
0.54
0.40
0.30
0.24
0.20
0.16
0.12
0.07
16
35.64
25.51
14.74
6.99
4.06
2.71
1.95
1.47
1.14
0.92
0.74
0.62
0.42
0.31
0.23
0.18
0.15
0.12
0.09
0.06
43
5.32
3.73
2.10
0.97
0.56
0.37
0.26
0.20
• 0.15
0.12
0.10
0.09
0.06
0.04
0.03
0.03
0.02
0.02
0.01
0.01
3
2
17
73.93
54.20
32.28
15.85
9.42
6.39
4.64
,49
,63
2.14
1.71
1.45
0.98
0.72
0.55
0.44
0.36
0.30
0.22
0.14
44
10.97
7.84
4.51
2.13
1.24
0.83
0.60
0.45
0.35
0.29
0.24
0.20
0.14
0.10
0.08
0.06
0.05
0.05
0.03
0.02
Volume Vn
Appendix VII-4
External Review Draft
Do Not Cite or Quote
-------
18
201.39
153.60
97.94
52.10
32.56
21.25
15.05
11.13
8.99
7.18
6.04
4.99
3.43
2.64
2.04
1.61
34
1
1
12
0.84
0.51
45
4.26
2.99
1.69
0.78
0.44
0.30
0.21
0.16
0.12
0.10
0.08
0.07
0.05
0.04
0.03
0.02
0.02
0.02
0.01
0.01
19
2.18
1.48
0.79
0.35
0.19
0.12
0.09
0.06
0.05
0.04
0.03
0.03
0.02
0.01
0.01
0.01
0.01
0.01
0.00
0.00
46
8.77
6.27
3.60
1.70
0.99
0.66
0.48
0.36
0.28
0.23
0.19
0.16
0.11
0.08
0.06
0.05
0.04
0.04
0.03
0.02
20
5.18
3.58
1.96
0.88
0.49
0.32
0.23
0.17
0.13
0.10
0.09
0.07
0.05
0.04
0.03
0.02
0.02
0.01
0.01
0.01
47
5.86
4.18
2.40
1.14
0.66
0.44
0.32
0.24
0.19
0.15
0.13
0.11
0.07
0.06
0.04
0.03
0.03
0.02
0.02
0.01
21
14.23
10.03
5.64
2.61
1.49
0.99
0.71
0.53
0.41
0.33
0.27
0.23
0.16
0.11
0.09
0.07
0.06
0.05
0.03
0.02
48
4.39
3.13
1.81
0.85
0.49
0.33
0.24
0.18
0.14
0.11
0.09
0.08
0.06
0.04
0.03
0.03
0.02
0.02
0.01
0.01
22
29.44
21.07
12.21
5.77
3.35
2.24
1.61
1.21
0.94
0.77
0.63
0.53
0.35
0.26
0.20
0.16
0.13
0.11
0.08
0.05
49
6.54
4.45
2.39
1.04
0.57
0.36
0.24
0.18
" 0.13
0.11
0.08
0.07
0.05
0.03
0.03
0.02
0.02
0.01
0.01
0.01
3
2
23
61.26
44.81
26.63
13.08
7.75
5.26
81
90
2.26
1.83
1.47
1.23
0.84
0.61
0.47
0.37
0.31
0.25
0.19
0.11
50
15.47
10.69
5.87
2.63
1.47
0.93
0.64
0.47
0.36
0.29
0.23
0.20
0.13
0.10
0.07
0.06
0.05
0.04
0.03
0.02
Volume VH
Appendix Vn-4
External Review Draft
Do Not Cit£ Qr
-------
24
177.10
135.00
. 85,35
44.91
27.91
19.17
13.41
9.91
7.79
6.27
5.12
4.34
3.01
2.22
1.76
1.38
1.16
0.95
0.71
0.43
51
44.40
31.47
17.87
8.30
4.56
93
04
48
1.17
0.93
0.76
0.63
0.43
0.31
0.24
0.19
0.15
0.13
0.09
0.06
2
2,
1,
25
4.45
3.07
1.69
0.75
0.42
0.27
0.19
0.14
0.11
0.09
0.07
0.06
0.04
0.03
0.02
0.02
0.02
0.01
0.01
0.01
52
86.17
62.28
36.62
16.77
9.38
6.08
4.30
3.28
2.54
2.01
1.68
1.40
0.96
0.70
0.53
0.42
0.34
0.29
0.21
0.12
26
12.19
8.56
4.83
2.23
1.27
0.85
0.60
0.45
0.35
0.29
0.23
0.20
0.14
0.10
0.08
0.06
0.05
0.04
0.03
0.02
53
142.85
106.75
66.62
31.20
18.64
12.50
9.12
6.94
5.33
4.45
3.57
3.11
2.14
1.54
1.20
0.95
0.77
0.64
0.45
0.27
27
25.18
17.97
10.40
4.92
2.85
1.91
1.37
1.03
0.80
0.66
0.54
0.46
0.31
0.23
0.17
0.14
0.11
0.09
0.07
0.04
54
206.49
155.77
107.65
63.55
42.95
31.57
24.58
19.60
15.75
13.30
11.04
9.54
6.67
,93
.85
2.96
2.49
2.02'
1.47
0.84
4
3
Volume VII
Appendix VII-4
External Review Draft
Do Not Cite or Quote
-------
X,m Max concentration, ppn
25.00
50.00
100.00
200.00
300.00
400.00
500.00
600.00
700.00
800.00
. 900.00
1000.00
1250.00
1500.00
1750.00
2000.00
2250.00
2500.00
3000.00
4000.00
235.68
183.07
121.80 ------
63.55
42.95
31.57
24.58
19.60
. 15.75
13.30
11.04
9.54
6.67
4.93
3.85
2.96
2.49
2.02
1.47
0.84
Concentration (ppm)
Distance to (n)
LOG
IDLH
9.9000
49.1000
976.22
270.14
Volume VH
Appendix VII-4
External Review Draft
Do Not Cite or Quote
-------
From Slab output file:
Scenario:
Accident Location:
Duration:
Meteorology:
Chemical:
Vapor phase mole fraction:
LOG:
• IDLH:
RUNS9.OUT
TYPICAL
ON-SITE
UNMITIG
INVERSN
HCL
1.000
9.900
49.100
*0utput adjusted to be distance from fenceline.
X,m Max concentration, ppm
25.00
50.00
100.00
200.00
300.00
400.00
500.00
600.00
700.00
800.00
900.00
1000.00
1250.00
1500.00
-^ 1750.00
2000.00
^ 2250.00
2500.00
3000.00
4000.00
5000.00
' 295.17
237.54
170.19
110.30
81.48
63.57
51.14
41.76
35.16
29.88
25.56
22.23
16.08
12.01
9.36
7.52
5.97
5.04
3.60
2.06
1.30
.Concentration (ppm)
Distance to (m)
LOC
IDLH
9.9000
49.1000
1699.08
521.79
Volume VII
Appendix VII-4
External Review Draft
Do Not Cite or Quote
-------
From Slab output file:
Scenario:
Accident Location:
Duration:
Meteorology:
Chemical:
Vapor phase mole fraction:
LOG:
IDLH:
RDN60.OUT
TYPICAL
ON-SITE
MITIGAT
INVERSN
HCL
1.000
9.900
49.100
*Output adjusted to be distance from fenceline.
X,m Max concentration, ppm
25.00
50.00
100.00
200.00
300.00
400.00
500.00
600.00
700.00
800.00
900.00
1000.00
1250.00
1500.00
1750.00
2000.00
2250.00
2500.00
3000.00
4000.00
5000.00
' 295
237
170
110
81
63
51
41
35
29
25
22
16
12
9
7
5
5
3
2
1
.17
.54
.19
.30
.48
.57
.14
.76
.16
.88
.56
.23
.08
.01
.36
.52
.97
.04
.60
.06
.30
-Concentration (ppm)
LOG
IDLH
9.9000
49.1000
Distance to (m)
1699.08
521.79
Volume VII
Appendix VII-4
External Review Draft
Do Not Cite or Quote
-------
From Slab output file:
Scenario:
Accident Location:
( Duration:
Meteorology:
Chemical:
Vapor phase mole fraction:
LOC:
IDLH:
RUNS1.OUT
CONSERV
OFFSITE
UNMITIG
TYPICAL
FORMALDEHYDE
0.484
9.600
19.600
X,m Max concentration, ppm
25.00
50.00
100.00
200.00
300.00
400.00
500.00
" 600.00
700.00
800.00
900.00
1000.00
1250.00
1500.00
1750.00
x-^ 2000.00
2250.00
v ^ 2500.00
3000.00
4000.00
5000.00
10000.00
15000.00
20000.00
2252.21
1352.68
660.84
259.13
137.95
87.72
60.74
44.88
34.65
27.39
22.55'
18.84
12.90
9.50
7.28
5.73
4.78
3.97
2.92
1.80
1.18
0.36
0.19
0.12
Concentration (ppm)
LOC
IDLH
9.6000
19.6000
Distance to (m)
1492.39
979.60
Volume VII
Appendix VII-4
External Review Draft
Do Not Cite or Quote
-------
From Slab output file:
Accident
Scenario:
Location:
Duration:
Meteorology:
Vapor phase mole
*
X,m
25.00
50.00
100.00
200.00
300.00
400.00
500.00
600.00
700.00
800.00
900.00
1000.00
1250.00
1500.00
1750.00
2000.00
2250.00
2500.00
3000.00
4000.00
5000.00
10000.00
15000.00
20000.00
X,m
25.00
50.00
100.00
200.00
300.00
400.00
500.00
600.00
700.00
800.00
900.00
1000.00
1250.00
1500.00
1750.00
2000.00
2250.00
2500.00
3000.00
4000.00
5000.00
10000.00
15000.00
20000.00
Chemical :
fraction :
LOG:
IDLH:
1
709.87
313.46
113.17
35.62
17.42
10.59
7.06
5.07
3.84
2.98
2.42
2.00
1.34
0.97
0.73
0.57
0.46
0.37
0.26
0.15
0.10
0.03
0.02
0.01
28
3600.96
2287.96
1200.44
509.44
281.81
183.88
129.28
96.43
75.23
60.07
49.79
41.84
28.94
21.49
16.62
13.16
11.03
9.18
6.79
4.18
2.72
0.82
0.42
0.27
"* — :
2
1337.45
666.18
267.16
90.29
44.91
27.56
18.58
13.46
10.24
7.99
6.52
5.41
3.64
2.65
2.01
1.57
1.28
1.02
0.72
0.43
0.29
0.09
0.04
0.03
29
8147.33
5589.23
3294.62
1600.52
958.79
658.43
480.52
368.35
293.49
238.53
200.29
170.38
120.76
91.16
71.37
57.19
48.30
40.17
27.25
16.27
10.95
3.30
1.61
0.97
RUN62.0DT
CONSERV
OFFSITE
UNMITIG
WORST
FORMALDEHYDE
0.484
9.600
19.600
3
2820.11
1592.17
726.30
271.94
141.62
89.23
61.10
44.73
34.33
26.96
22.12
18.41
12.46
9.10
6.87
5.10
4.18
3.36
2.36
1.44
0.97
0.29
0.14
0.09
30
496.91
247.89
98.81 '
33.11
16.41
10.07
6.80
4.92
3.74
2.92
2.38
1.98
1.33
0.97
0.74*
0.58
0.48
0.40
0.29
0.18
0.13
0.04
0.02
0.01
4
5082.00
3046.30
1491.72
596.84
322.19
206.18
143.00
105.69
81.74
64.60
52.94
44.16
30.25
21.71
15.74
11.97
9.77
7.79
5.63
3.39
2.28
0.68
0.33
0.20
31
1034.15
583.51
263.54
96.74
49.97
31.26
21.36
15.62
11.99
9.43
7.73
6.43
4.37
3.20
2.44
1.92
1.60
1.32
0.97
0.61
0.42
0.13
0.07
0.04
5
9002.40
5639.57
2907.66
1233.92
692.69
453.26
321.63
241.42
189.01
151.39
125.70
105.78
70.99
49.16
36.20
28.32
22.97
18.80
13.70
7.94
5.31
1.53
0.73
0.43
32
1797.25
1077.96
526.14
205.76
109.46
69.73
48.15
35.51
27.42
21.67
17.85
14.91
10.19
7.50
5.76
4.54
3.79
3.15
2.32
1.47
1.02
0.30
0.16
0.10
Volume VII
Appendix VII-4
External Review Draft
Do Not Cite or Quote
-------
6
20795.87
12574.32
6080.10
2635.45
1578.03
1101.97
825.67
649.97
511.21
392.23
326.09
271.55
190.21
139.39
111.47
89.02
73.53
61.14
44.24
26.93
17.85
4.77
2.22
1.25
33
3142.77
1998.73
1047.86
443.14
244.90
159.27
11Z.17
83.78
65.33
52.13
43.11
36.19
25.05
18.59
14.37
11.40
9.56
7.97
5.89
3.77
2.50
0.74
0.38
7
530.79
234.53
84.67
26.73
13.10
7.92
5.30
3.82
2.88
2.24
1.82
1.50
1.00
0.73
0.55
0.43
0.35
0.29
0.21
0.12
0.08
0.02
0.01
0.01
34
7114.80
4889.56
2884.88
1401.66
839.31
570.15
416.04
319.49
254.26
206.30
173.14
147.22
104.30
78.64
61.47
49.37
41.69
35.01
26.06
14.89
9.92
2.98
1.50
f\ r\ f\
1000.27
496.55
198.93
66.67
33.15
20.35
13.72
9.94
7.57
5.90
4.82
3.99
2.69
1.96
1.49
1.16
0.97
0.80
0.58
0.34
0.23
0.07
0.04
0.02
•j e
442.21
220.39
87.76
29.39
14.60
8.93
6.03
4.36
3.32
2.59
2.12
1.75
1.18
0.86
0.66
0.51
0.43
0.35
0.26
0.16
0.11
0.03
0.02
n m
9
2087.65
1176.70
535.41
198.50
103.07
64.57
44.28
32.37
24.83
19.52
15.99
13.30
9.03
6.60
5.03
3.95
3.29
2.70
1.87
1.12
0.75
0.22
0.11
0.07
36
919.60
518.23
234.03
86.07
44.37
27.76
18.98
13.87
10.63
8.36
6.84
5.69
3.87
2.83
l".70
1.42
1.17
0.86
0.54
0.38
0.11
0.06
0.04
10
3676.79
2209.17
1079.44
430.91
230.82 .
147.81
102.44
75.77
58.57
46.23
38.04
31.77
21.71
15.94
12.23
9.64
7.78
6.17
4.34
2.63
1.77
0.53
0.27
0.16
37
1593.97
956.77
465.45
182.62
96.98
61.60
42.60
31.43
24.25
19.16
15.79
13.20
9.05
6.67
5.12
4.03
3.36
2.79
2.05
1.30
0.91
0.27
0.14
0.09
11
6453.33
4099.29
2155.28
926.65
518.54
341.37
241.40
180.99
141.32
112.66
93.24
78.40
54.38
40.26
30.60
22.84
18.55
14.80
10.60
6.38
4.32
1.29
0.63
0.38
38
2787.84
1770.86
929.16
392.51
216.51
140.81
99.15
73.94
57.55
45.87
38.01
31.95
22.12
16.43
12.70
10.08
8.45
7.04
5.19
3.33
2.33
0.68
0.35
0.23
0.25
Volume VH
Appendix VH-4
External Review Draft
Do Not Cite or Quote
-------
12
14745.87
9790.35
5362.37
2475.31
1474.97
1016.98
749.56
583.26
469.60
384.31
325.45
279.00
192.23
134.31
100.05
79.98
65.05
54.16
39.68
23.76
16.02
4.51
2.08
1.19
39
397.85
198.25
78.80
26.44
13.10
8.04
5.43
3.92
2.99
2.33
1.90
1.58
1.07
0.78
0.59
0.46
0.38
0.32
0.23
0.15
0.10
0.03
0.02
0.01
13
423.66
187.. 46
67.71
21.39
10.45
6.34
4.24
3.05
2.31
1.79
1.46
1.20
0.80
0.58
0.44
0.34
0.28
0.23
0.17
0.10
0.07
0.02
0.01
0.01
40
826.03
467.00
210.48
77.33
39.87
24.95
17.06
12.47
9.57
7.52
6.15
5.12
3.48
2.55
1.95
1.53
1.27
1.05
0.77
0.49
0.34
0.11
0.06
0.04
14
796.99
397.62
158.56
53.11
26.38
16.18
10.90
7.88
6.00
4.69
3.83
3.18
2.14
1.56
1.19
0.93
0.77
0.63
0.46
0.28
0.19
0.06
0.03
0.02
41
1432.64
859.78
418.60
164.02
87.02
55.26
38.26
28.21
21.77
17.21
14.16
11.83
8.11
5.98
4.59
3.62
3.02
2.50
1.84
1.17
0.81
0.25
0.13
0.08
15
1661.73
935.86
423.57
156.76
81.07
50.78
34.77
25.43
19.50
15.33
12.55
10.45
7.11
5.20
3.97
3.11
2.59
2.14
1.56
0.92
0.61
0.19
0.10
0.06
42
2507.12
1593.13
836.14
352.41
194.07
126.05
88.72
66.22
51.53
41.07
34.02
28.59
19.80
14.68
11.35
9.00
7.55
6.29
4.67
2.99
2.09
0.62
0.32
0.21
16
2904.00
1743.76
851.72
336.77
179.89
114.80
79.48
58.68
45.35
35.86
29.53
24.66
16.87
12.42
9.53
7.49
6.24
5.17
3.79
2.20
1.47
0.44
0.22
0.14
43
514.65
290.30
131.45
48.31
24.88
15.56
10.62
7.78
5.97
4.69
3.84
3.20
2.17
1.59
1.22
0.95
0.79
0.66
0.48
0.30
0.21
0.07
0.04
0.02
17
5082.00
3236.41
1702.79
729.32
407.00
266.32
187.87
140.74
109.90
87.56
72.62
61.07
42.25
31.30
24.17
19.13
16.02
13.22
9.02
5.37
3.62
1.09
0.55
0.33
44
893.79
534.92
260.95
102.07
54.03
34.45
23.80
17.56
13.55
10.70
8.82
7.37
5.05
3.71
2.85
2.25
1.88
1.56
1.15
0.73
0.51
0.17
0.09
0.06
Volume Vn
Appendix VIM
External Review Draft
Do Not Cite or Quote
-------
18
11535.33
7850.48
4525.58
2166.38
1296.46
889.40
653.67
504.40
402.83
328.36
276.68
236.12
168.43
123.26
89.31
68.93
56.49
46.04
33.91
19.94
13.52
( x 3.95
( 1.91
y 1.09
45
411.24
231.95
105.00
38.60
19.88
12.45
8.49
6.22
4.77
3.74
3.07
2.56
1.74
1.27
0.97
0.76
0.64
0.53
0.39
0.24
0.17
0.06
0.03
0.02
/ x
19
352.67
155.93
56.17
17.82
8.73
5.29
3.54
2.54
1.92
1.49
1.21
1.00
0.67
0.48
0.37
0.29
0.24
0.19
0.14
0.09
0.06
0.02
0.01
0.01
46
711.48
428.26
208.33
81.69
43.31
27.52
19.02
14.02
10.82
8.56
7.03
5.87
4.03
2.97
2.28
,80
.50
1.24
0.92
0.58
0.41
0.14
0.08
0.05
1.
1,
20
666.31
331.00
131.81
44.21
21.92
13.45
9.06
6.55
4.98
3.90
3.18
2.64
1.78
1.30
0.99
0.77
0.64
0.53
0.39
0.24
0.16
0.05
0.03
0.02
47
474.32
284.59
138.90
54.51
28.84
18.33
12.67
9.35
7.21
5.68
4.68
3.92
2.68
1.98
1.52
1.20 .
1.00
0.83
0.61
0.39
0.27
0.09
0.05
0.03
21
1381.01
777.50
352.50
129.91
67.09
41.96
28.70
20.99
16.09
12.64
10.37
8.64
5.86
4.28
3.28
2.57
2.14
1.77
1.30
0.79
0.52
0.16
0.08
0.05
48
354.45
213.00
103.92
40.76
21.64
13.75
9.50
6.99
5.39
4.27
3.52
2.94
2.01
1.48
1.14 *
0.90
0.75
0.62
0.46
0.29
0.20
0.07
0.04
0.03
22
2408.71
1446.39
702.51
277.25
147.91
94.13
65.14
48.10
37.13
29.35
24.18
20.20
13.82
10.16
7.79
6.16
5.14
4.25
3.13
1.92
1.26
0.38
0.20
0.13
49
1066.41
474.55
172.39
54.25
26.17
15.82
10.55
7.60
5.76
4.46
3.63
3.00
2.00
1.42
1.03
0.78
0.64
0.51
0.36
0.22
0.15
0.04
0.02
0.01
23
4215.64
2675.75
1405.84
598.36
333.09
217.37
153.03
114.48
89.35
71.23
58.99
49.57
34.34
25.48
19.68
15.60
13.06
10.87
8.02
4.64
3.08
0.92
0.48
0.30
50
2024.73
1015.43
411.37
140.61
70.23
43.28
29.14
21.11
16.07
12.53
10.20
8.44
5.59
3.86
2.83
2.19
1.78
1.43
1.02
0.62
0.41
0.12
0.06
0.03
Volume Vn
Appendix VII-4
External Review Draft
Do Not Cite or Quote
-------
24
9534.80
6526.26
3824.54
1855.93
1117.00
766.66
559.53
429.95
343.11
279.19
234.68
199.85
141.81
107.11
84.05
67.46
54.38
42.76
29.97
18.22
12.27
3.63
1.73
1.04
51
4517.33
2545.84
1154.16
432.25
225.15
141.73
96.94
71.03
54.54
42.75
35.01
28.79
18.40
12.87
9.46
7.42
5.98
4.89
3.52
2.04
1.37
0.39
0.18
0.11
25
567.89
283.45
112.91
37.83
18.76
11.50
7.74
5.63
4.29
3.34
2.73
2.26
1.52
1.11
0.84
0.66
0.55
0.45
0.33
0.21
0.14
0.04
0.02
0.01
52
8582.93
5055.67
2373.13
913.93
488.19
312.10
217.07
160.60
124.30
97.89
77.35
62.56
40.84
28.90
21.39
17.17
13.67
11.43
8.20
4.81
3.19
0.86
0.40
0.23
26 •
1182.57
665.98
301.53
110.82
57.07
35.82
24.49
17.91
13.73
10.78
8.84
7.36
5.00
3.66
2.80
2.20
1.83
1.51
1.11
0.70
0.47
0.14
0.07
0.05
53
15407.33
8793.31
3964.85
1572.03
881.83
587.96
422.02
321.89
247.58
187.12
153.02
125.56
84.95
61.23
47.15
37.49
29.91
25.25
18.03
10.83
7.16
1.91
0.85
0.48
27
2058.61
1233.04
599.81
236.16
125.47
80.07
55.38
40.84
31.51
24.88
20.49
17.13
11.71
8.61
6.62
5.23
4.36
3.61
2.66
1.69
1.12
0.34
0.17
0.11
54
30604.93
13987.60
5998.06
2607.79
1605.17
1107.62
766.18
585.28
464.84
389.46
328.25
284.37
206.13
156.48
120.18*
99.76
80.46
69.34
50.31
30.30
19.95
5.12
2.32
1.26
Volume VH
Appendix VII-4
External Review Draft
Do Not Cite or Quote
-------
X,m Max concentration, ppm
25.00
50.00
100.00
200.00
300.00
400.00
500.00
600.00
700.00
800.00
900.00
1000.00
1250.00
1500.00
1750.00
2000.00
2250.00
2500.00
3000.00
4000.00
5000.00
10000.00
15000.00
20000.00
30604.93
13987.60
6080.10
2635.45
1605.17
1107.62
825.67
649.97
. 511.21
392.23
328.25
284.37
206.13
156.48
120.18
99.76
80.46
69.34
50.31
30.30
19.95
5.12
2.32
1.26
ncentration (ppm)
Distance to (m)
IDLH
9.6000
19.6000
8489.07
5119.39
Volume VII
Appendix VII-4
External Review Draft
Do Not Cite or Quote
-------
From Slab output file:
Scenario:
Accident Location:
Duration:
Meteorology:
Chemical:
Vapor phase mole fraction:
LOG:
IDLH:
RUNS3.OUT
CONSERV
OFFSITE
UNMITIG
INVERSN
FORMALDEHYDE
0.484
9.600
19.600
X,m . Max concentration,. ppm
25.00
50.00
100.00
200.00
300.00
400.00
500.00
600.00
700.00
800.00
900.00
1000.00
1250.00
1500.00
1750.00
2000.00
2250.00
2500.00
3000.00
4000.00
5000.00
10000.00
15000.00
20000.00
29537.00
14459.07
6685.56
2995.96
1884.70
1342.85
1041.36
836.73
683.27
588.78
500.84
440.83
325.33
253.08
206.40
166.11
143.19
120.26
92.06
57.32
39.52
11.47
5.40
3.10
Concentration (ppm)
LOG
IDLH
9.6000
19.6000
Distance to (m)
11542.35
8551.02
Volume Vn
Appendix VII-4
External Review Draft
Do Not Cite or Quote
-------
From Slab output file:
Scenario:
Accident Location:
Duration:
Meteorology:
Chemical:
Vapor phase mole fraction:
LOG:
IDLH:
RUNA6.OUT
CONSERV
OFFSITE
UNMITIG
INVERSN
ACETONE
0.274
1960.000
2442.000
X,m Max concentration,, ppm
• 25.00
50.00
100.00
200.00
300.00
400.00
500.00
600.00
'700.00
800.00
900.00
1000.00
1250.00
1500.00
1750.00
^—^ 2000.00
2250.00
^^ 2500.00
3000.00
4000. 00
5000.00
1313
442
232
130
93
74
62
53
47
42
38
34
28
24
21
19
17
15
12
8
6
.34
.38
.92
.86
.98
.48
.07
.59
.28
'.38
.33
.91
.95
.72
.55
.28
.35
.60
.77
.95
.57
Concentration (ppm)
Distance to (m)
LOG
IDLH
1960.0000
2442.0000
less than
less than
25.00
25.00
Volume VII
Appendix VU-4
External Review Draft
Do Not Cite or Quote
-------
From Slab output file: RUN64.OUT
Scenario: CONSERV
Accident Location: OFFSITE
Duration: UNMITIG
Meteorology: TYPICAL
Chemical: ACETONE
Vapor phase mole fraction: 0.274
LOC: 1960.000
IDLH: 2442.000
X,m Max concentration, ppm
• 25.00
50.00
100.00
200.00
300.00
400.00
. 500.00
600.00
' 700.00
800.00
900.00
1000.00
1250.00
1500.00
1750.00
2000.00
2250.00
2500.00
3000.00
4000.00
5000.00
10000.00
15000.00
20000.00
218.20
130.83
63.74
25.33
13.55
8.66
6.01
4.43
3.42
2.71
2.23
1.86
1.27
0.93
0.71
0.56
0.47
0.39
0.29
0.18
0.13
0.04
0.02
0.02
Concentration (ppm) Distance to (m)
LOC 1960.0000 less than 25.00
IDLH 2442.0000 less than 25.00
Volume VII External Review Draft
Appendix VD-4 Do Not Cite or Quote
-------
From Slab output file:
Scenario:
Accident Location:
Duration:
Meteorology:
Chemical:
Vapor phase mole fraction:
LOG:
IDLH:
1
67.68
30.00
10.92
X,m
25.00
50.00
100.00
200.00
300.00
400.00
500.00
600.00
700.00
800.00
900.00
1000.00
1250.00
1500.00
1750.00
2000.00
2250.00
2500.00
3000.00
4000.00
5000.00
10000.00
15000.00
20000.00
X,m
25.00
50.00
100.00
200.00
300.00
400.00
500.00
600.00
700.00
800.00
900.00
1000.00
1250.00
1500.00
1750.00
2000.00
2250.00
2500.00
3000.00
4000.00
5000.00
10000.00
15000.00
20000.00
3.43
1.66
1.00
0.67
0.48
0.36
0.28
0.23
0.19
0.13
0.09
0.07
0.05
0.04
0.04
0.03
0.02
0.01
0.00
0.00
0.00
28
348.89
220.72
115.84
49.71
27.71
18.16
12.82
9.60
7.50
5.98
4.95
4.15
2.87
2.13
1.65
1.30
1.09
0.91
0.67
0.43
0.30
0.10
0.06
0.04
••• "• = 0= «™
2
128.78
64.44
26.08
8.89
4.45
2.74
1.84
1.33
1.01
0.79
0.64
0.53
0.36
0.26
0.20
0.15
0.13
0.11
0.08
0.05
0.03
0.01
0.01
0.00
29
795.51
534.08
302.74
144.24
86.32
59.25
43.45
33.51
26.85
21.98
18.55
15.84
11.32
8.59
6.76
5.45
4.61
3.89
2.94
1.91
1.36
0.48
0.27
0.18
RUN 6 5. OUT
CONSERV
OFFSITE
UNMITIG
WORST
ACETONE
0.274
1960.000
2442.000
3
288.61
161.69
73.24
27.38
14.22
8.94
6.13
4.48
3.44
2.71
2.21
1.84
1.24
0.91
0.69
0.54
0.45
0.37
0.27
0.17
0.12
0.04
0.02
0.01
30
47.40
23.60
9.39
3.15
1.56
0.96
0.64
0.47
0.36
0.28
0.23
0.19
0.13
0.09
0.07
0.05
0.05
0.04
0.03
0.02
0.01
0.00
0.00
0.00
4
545.26
320.25
150.15
58.06
30.83
19.75
13.72
10.15
7.85
6.22
5.13
4.30
2.95
2.17
1.66
1.31
1.09
0.90
0.66
0.42
0.29
0.10
0.05
0.04
31
98.91
55.55
25.14
9.28
4.79
2.99
2.05
1.50
1.15
0.90
0.74
0.62
0.42
0.31
0.23
0.18
0.15
0.13
0.09
0.06
0.04
0.01
0.01
0.00
4,
3
3,
5
980.92
555.45
251.78
100.35
56.14
37.46
26.89
20.49
16.23
13.13
11.00
9.33
6.59
,97
,88
.10
2.61
2.19
1.63
1.05
0.74
0.26
0.14
0.10
32
172.71
103.47
50.30
19.86
10.58
6.76
4.68
3.45
2.66
2.11
1.73
1.45
0.99
0.73
0.56
0.44
0.37
0.30
0.22
0.14
0.10
0.03
0.02
0.01
Volume Vn
Appendix Vn-4
External Review Draft
Do Not Cite or Quote
-------
6
1861.83
862.09
377.44
167.70
103.67
74.41
57.29
46.02
38.16
32.25
27.96
24.55
18.59
14.65
11.91
9.89
8.57
7.39
5.76
3.92
2.87
1.11
0.63
0.41
33
303.23
191.91
100.76
42.94
23.91
15.63
11.03
8.26
6.45
5.14
4.26
3.58
2.47
1.83
1.42
1.12
0.94
0.78
0.58
0.37
0.26
0.09
0.05
0.03
7
50.69
22,39
8.08
2.53
1.24
0.75
0.50
0.36
0.27
0.21
0.17
0.14
0.10
0.07
0.05
0.04
0.03
0.03
0.02
0.01
0.01
0.00
0.00
0.00
34
689.57
467.33
270.74
130.24
78.16
53.70
39.22
30.24
24.18
19.69
16.56
14.12
10.06
7.62
5.99
4.81
4.06
3.41
2.56
1.67
1.18
0.42
0.23
0.15
8
95.72
47.60
19.13
6.47
3.23
1.98
1.34
0.97
0.73
0.57
0.47
0.39
0.26
0.19
0.14
0.11
0.09
0.08
0.06
0.04
0.02
0.01
0.00
0.00
35
42.20
20.95
8.35
2.80
1.39
0.85
0.57
0.41
0.32
0.25
0.20
0.17
0.11
0.08
0.06
0.05
0.04
0.03
0.02
0.02
0.01
0.00
0.00
0.00
9
204.22
115.03
52.36
19.67
10.25
6.45
4.42
3.24
2.49
1.95
1.60
1.33
0.90
0.66
0.50
0.39
0.33
0.27
0.20
0.12
0.08
0.03
0.02
0.01
36
87.68
49.32
22.31
8.22
4.25
2.65
1.81
1.33
1.02
0.80
0.66
0.55
0.37
0.27
0.21
0.16
0.14
0.11
0.08
0.05
0.04
0.01
0.01
0.00
10
371.73
222.32
108.42
43.22
23.24
14.87
10.32
7.62
5.88
4.64
3.82
3.19
2.18
1.60
1.22
0.96
0.80
0.66
0.49
0.31
0.21
0.07.
0.04
0.03
37
152.89
91.58
44.49
17.54
9.34
5.94
4.12
3.04
2.34
1.85
1.53
1.27
0.87
0.64
0.49
0.39
0.32
0.27
0.20
0.12
0.09
0.03
0.02
0.01
11
663.99
408.92
206.00
86.15
47.98
31.55
22.44
16.88
13.23
10.61
8.83
7.45
5.18
3.86
2.99
2.38
1.99
1.66
1.23
0.79
0.55
0.19
0.10
0.07
38
267.79
169.96
89.13
37.81
21.03
13.73
9.68
7.24
5.63
4.48
3.72
3.13
2.17
1.61
1.24
0.98
0.82
0.68
0.51
0.32
0.23
0.08
0.04
0.03
Volume Vn
Appendix VII-4
External Review Draft
Do Not Cite or Quote
-------
12
1536.23
844.69
385.91
168.05
101^91
71.95
54.36
43.09
35.29
29.46
25.34
' 22.02
16.29
12.72
10.25
8.43
7.21
6.15
4.74
3.18
2.30
0.85
0.49
0.33
39
37.99
18.85
7.50
2.51
1.24
0.76
0.51
0.37
0.28
0.22
0.18
0.15
0.10
0.07
0.06
0.04
0.04
0.03
0.02
0.01
0.01
0.00
0.00
0.00
13
40.28
17-..84
6.43
2.03
0.99
0.60
0.40
0.29
0.22
0.17
0.14
0.11
0.08
0.06
0.04
0.03
0.03
0.02
0.02
0.01
0.01
0.00
0.00
0.00
40
78.73
44.29
20.05
7.37
3.80
2.38
1.63
1.19
0.91
0.72
0.59
0.49
0.33
0.24
0.19
0.15
0.12
0.10
0.07
0.05
0.03
•0.01
0.01
0.00
14
76.26
37.99
15.16
5.09
2.53
1.56
1.05
0.76
0.58
0.45
0.37
0.31
0.21
0.15
0.11
0.09
0.07
0.06
0.04
0.03
0.02
0.01
0.00
0.00
41
137.27
82.16
40.04
15.70
8.35
5.31
3.69
2.72
2.10
1.66
1.36
1.14
0.78
0.57
0.44
0.35
0.29
0.24
0.18
0.11
0.08
0.03
0.01
0.01
15
160.47
90.41
41.12
15.31
7.96
5.00
3.42
2.50
1.92
1.51
1.24
1.03
0.70
0.51
0.39
0.30
0.25
0.21
0.15
0.10
0.07
0.02
0.01
0.01
42
240.39
152.49
79.94
33.87
18.75
12.24
8.61
6.43
5.02
4.01
3.31
2.78
1.93
1.43
1.10
0.87
0.73
0.61
0.45
0.29
0.20
0.07
0.04
0.03
16
284.96
171.36
83.82
33.51
18.01
11.52
7.99
5.90
4.56
3.61
2.97
2.47
1.69
1.24
0.95
0.75
0.62
0.51
0.38
0.24
0.16
0.06
0.03
0.02
43
49.05
27.74
12.49
4.59
2.36
1.48
1.01
0.74
0.57
0.44
0.37
0.30
0.21
0.15
0.12
0.09
0.08
0.06
0.05
0.03
0.02
0.01
0.00
0.00
17
505.07
317.40
165.35
70.77
39.76
26.09
18.43
13.83
10.80
8.62
7.15
6.02
4.16
3.09
2.39
1.89
1.58
1.32
0.97
0.62
0.43
0.15
0.08
0.05
44
85.21
51.05
24.86
9.72
5.15
3.27
2.26
1.67
1.29
1.02
0.84
0.70
0.48
0.35
0.27
0.21
0.18
0.15
0.11
0.07
0.05
0.02
0.01
0.01
Volume VII
Appendix VE-4
External Review Draft
Do Not Cite or Quote
-------
18
1179.11
733.66
372.44
166.13
99.22
68.94
51.35
40.24
32.67
27.02
22.98
19.79
14.40
11.10
8.86
7.22
6.15
5.21
3.96
2.63
1.88
0.68
0.38
0.26
45
39.18
22.09
9.98
3.65
1.89
1.18
0.81
0.59
0.45
0.36
0.29
0.24
0.16
0.12
0.09
0.07
0.06
0.05
0.04
0.02
0.02
0.01
0.00
0.00
0,
0,
19
33.70
14.84
5.34
1.69
0.83
0.50
0.34
0.24
0.18
14
11
0.09
0.06
0.05
0.03
0.03
0.02
0.02
0.01
0.01
0.01
0.00
0.00
0.00
46
67.95
40.80
19.84
7.76
4.10
2.62
1.81
1.33
1.03
0.81
0.67
0.56
0.38
0.28
0.22
0.17
0.14
0.12
0.09
0.06
0.04
0.01
0.01
0.00
20
63.39
31.49
12.58
4.23
2.10
1.29
0.87
0.63
0.48
0.37
0.30
0.25
0.17
0.12
0.09
0.07
0.06
0.05
0.04
0.02
0.02
0.01
0.00
0.00
47
45.21
27.12
13.19
5.17
2.74
1.74
1.20
0.89
0.68
0.54
0.45
0.37
0.25
0.19
0.14
0.11
0.09
0.08
0.06
0.04
0.03
0.01
0.00
0.00
21
132.80
74.67
33.85
12.56
6.49
4.08
2.79
2.04
1.57
1.23
1.01
0.84
0.57
0.42
0.32
0.25
0.21
0.17
0.13
0.08
0.05
0.02
0.01
0.01
48
33.79
20.30
9.89
3.87
2.05
1.30
0.90
0.66
0.51
0.41
0.33
0.28
0.19
0.14
O.ll
0.09
0.07
0.06
0.04
0.03
0.02
0.01
0.00
0.00
22
233.63
140.07
68.46
27.21
14.59
9.32
6.47
4.78
3.69
2.92
2.40
2.00
1.37
1.01
0.77
0.61
0.51
0.42
0.31
0.19
0.13
0.05
0.02
0.02
49
103.30
46.33
17.02
5.40
2.60
1.57
1.04
0.75
0.57
0.44
0.36
0.29
0.20
0.14
0.11
0.08
0.07
0.06
0.04
0.03
0.02
0.01
0.00
0.00
23
411.91
260.06
136.47
58.68
32.75
21.54
15.21
11.40
8.91
7.12
5.90
4.95
3.41
2.53
1.96
55
30
08
0.80
0.51
0.35
0.12
0.07
0.04
50
200.75
100.42
40.90
13.99
6.98
4
2
2
1
1.
1.
1.
30
90
10
60
1.24
1.01
0.84
0.56
0.41
0.31
0.24
0.20
0.16
0.12
0.07
0.05
0.02
0.01
0.01
Volume VH
Appendix VII-4
External Review Draft
Do Not Cite or Quote
-------
24
946.21
621.98
340.86
157.34
93.91
64.80
47.69
37.01
29.81
24.43
20.69
17.74
12.75
9.74
7.72
6.25
5.30
4.47
3.39
2.22
1.58
0.57
0.32
0.21
51
616.50
322.22
122.36
40.94
20.81
13.06
8 ."98
6.60
5.09
4.02
3.30
2.75
1.88
1.38
1.06
0.83
0.69
0.57
0.42
0.27
0.18
0.06
0.03
0.02
25
54.34
27.02
10.76
3.62
1.79
1.10
0.74
0.53
0.41
0.32
0.26
0.22
0.15
0.11
0.08
0.06
0.05
0.04
0.03
0.02
0.01
0.00
0.00
0.00
52
1037.55
505.37
199.71
73.44
39.82
25.90
18.36
13.82
10.85
8.70
7.23
6.10
4.26
3.18
2.46
1.95
1.64
1.36
1.01
0.64
0.45
0.15
0.09
0.06
26
113.25
63.69
28.86
10.65
5.50
3.45
2.36
1.73
1.33
1.04-
0.85
0.71
0.48
0.35
0.27
0.21
0.18
0.15
0.11
0.07
0.05
0.02
0.01
0.01
53
1491.47
662.86
271.48
109.40
63.34
43.52
32.12
24.96
20.12
16.55
14.05
12.06
8.71
6.68
5.31
4.29
3.65
3.09
2.34
1.53
1.09
0.40
0.22
0.14
27
198.38
118.94
57.93
22.94
12.25
7.83
5.42
4.01
3.10
2.44
2.01
1.68
1.15
0.84
0.65
0.51
0.42
0.35
0.26
0.16
0.11
0.04
0.02
0.01
54
1687.29
1018.47
450.46
191.01
116.47
82.00
63.19
50.94
42.39
36.06
31.48
27.63
21.22
16.93,
13.9*
11.79
10.21
8.95
7.10
4.85
3.68
1.46
0.77
0.47
Volume VII
Appendix VII-4
External Review Draft
Do Not Cite or Quote
-------
X,m Max concentration, ppm
25.00
50.00
100.00
200.00
300.00
400.00
500.00
600.00
700.00
800.00
900.00
1000.00
1250.00
1500.00
1750.00
2000.00
2250.00
2500.00
3000.00
4000.00
5000.00
10000.00
15000.00
20000.00
1861.83
1018.47
450.46
191.01
116.47
82.00
63.19
50.94
. 42.39
36.06
31.48
27.63
21.22
16.93
13.98
11.79
10.21
8.95
7.10
4.85
3.68
1.46
0.77
0.47
Concentration (ppm)
Distance to (n)
LOG
IDLH
1960.0000
2442.0000
less than
less than
25.00
25.00
Volume VH
Appendix VH-4
External Review Draft
Do Not Cite or Quote
-------
From Slab output file:
Scenario:
Accident Location:
Duration:
v , Meteorology:
Chemical:
Vapor phase mole fraction:
LOG:
• IDLH:
RUNS6.OUT
CONSERV
OFFSITE
UNMITIG
INVERSN
ACETONE
0.274
1960.000
2442.000
X,m Max concentration, ppm
25.00
50.00
100.00
200.00
300.00
400.00
500.00
600.00
' 700.00
800.00
900.00
1000.00
1250.00
1500.00
1750.00
2000.00
2250.00
2500.00
3000.00
4000.00
5000.00
3188.68
1676.45
802.96
351.70
213.25
149.28
112.46
88.30
73.32
61.56
52.43
45.80
33.98
26.29
21.31
17.80
14.77
12.96
9.92
6.46
4.59
Concentration (ppm)
LOG
IDLH
1960.0000
2442.0000
Distance to (m)
45.31
37.34
Volume
Appendix VII-4
External Review Draft
Do Not Cite or Quote
-------
From Slab output file:
Scenario:
Accident Location:
Duration:
Meteorology:
Chemical:
Vapor phase mole fraction:
LOC:
IDLH:
RUNS7.OUT
TYPICAL
OFFSITE
UNMITIG
TYPICAL
FORMALDEHYDE
0.482
9.600
19.600
X,m Max concentration, ppm
' 25.00
50.00
100.00
200.00
300.00
400.00
500.00
600.00
'"700.00
800.00
900.00
1000.00
1250.00
1500.00
1750.00
2000.00
2250.00
2500.00
3000.00
4000.00
5000.00
178.57
71.38
24.74
7.76
3.84
2.29
1.54
1.12
0.86
0.69
0.55
0.46
0.31
0.22
0.17
0.13
0.11
0.09
0.06
0.04
0.03
Concentration (ppm)
LOC
IDLH
9.6000
19.6000
Distance to (m)
189.15
130.28
Volume VH
Appendix VII-4
External Review Draft
Do Not Cite or Quote
-------
From Slab output file:
Scenario:
,----, Accident Location:
Duration:
^ ^ Meteorology:
~~~ Chemical :
Vapor phase mole
X.VL
*fc 9 "•*
25.00
50.00
100.00
200.00
300.00
400.00
500.00
600.00
700.00
800.00
900.00
1000.00
1250.00
1500.00
1750.00
2000.00
2250.00
2500.00
3000.00
4000.00
-x 5000.00
XfTH
f ^^
_^ 25.00
50.00
100.00
200.00
300.00
400.00
500.00
600.00
700.00
800.00
900.00
1000.00
1250.00
1500.00
1750.00
2000.00
2250.00
2500.00
3000.00
4000.00
5000.00
fraction:
LOG:
IDLH:
1
43.32
13.49
3.87
1.05
0.49
0.28
0.18
0.13
0.10
0.08
0.06
0.05
0.03
0.02
0.02
0.01
0.01
0.01
0.01
0.00
0.00
28
296.96
128.40
47.37
15.64
7.95
4.84
3.30
2.41
1.87
1.50
1.21
1.02
0.67
0.48
0.37
0.28
0.23
0.19
0.14
0.09
0.06
RUN68.ODT
TYPICAL
OFFSITE
UNMITIG
WORST
FORMALDEHYDE
2
89 . 32
30.43
9.33
2.64
1.24
0.72
0.47
0.33
0.25
0.19
0.15
0.13
0.08
0.06
0.04
0.03
0.03
0.02
0.02
0.01
0.01
29
711.41
349.84
146.46
53.81
28.82
18.04
12.59
9.35
7.34
5.80
4.53
3.80
2.50
1.81
1.35
1.09
0.88
0.74
0.54
d. 33
0.23
0.482
9.600
19.600
3
210.76
79.25
26.06
7.82
3.80
2.23
1.49
1.07
0.80
0.62
0.49
0.41
0.27
0.19
0.14
0.11
0.09
0.07
0.05
0.03
0.02
30
33.45
11.42
3.49
0.99
0.47
0.27
0.18
0.12
0.10
0.08
0.06
0.05
0.03
0.02
0.02
0.01
0.01
0.6l
0.01
0.00
0.00
4
385.74
156.86
54.92
17.39
8.60
5.11
3.43
2.38
1.80
1.-40
1.09
0.93
0.61
0.43
0.32
0.26
0.21
0.17
0.12
0.07
0.05
31
78.03
29.07
9.54
2.85
1.38
0.81
0.54
0.39
0.30
0.24
0.19
0.16
0.11
0.08
0.06
0.05
0.04
0.03
0.02
0.01
0.01
5
681.57
296.27
112.08
37.94
19.45
11.33
7.32
5.29
4.03
3.09
2.54
2.06
1.37
0,99
0.77
0.59
0.49
0.40
0.29
0.17
0.11
32
142.85
57.20
19.72
6.17
3.06
1.82
1.23
0.89
0.69
0.55
0.44
0.37
0.25
0.18
0.14
0.11
0.09
0.07
0.05
0.03
0.02
Volume VII
Appendix VD4
External Review Draft
Do Not Cite or Quote
-------
6
1277.30
580.01
249.24
99.28
50.52
32.05
22.35
16.47
12.73
10.34
8.34
7.09
4.83
3.45
2.72
2.
1,
1.
1.
0.
,09
,74
,38
,02
,59
0.39
33
259.32
112.28
41.30
13.61
6.94
4.21
2.87
2.10
,63
,31
,06
0.89
0.61
0.44
0.33
0.26
0.21
0.17
0.12
0.08
0.05
1,
1,
1,
7
32.46
10.11
2.90
0.79
0.37
0.21
0.14
0.10
0.07
0.06
0.05
0.04
0.02
0.02
0.01
0.01
0.01
0.01
0.00
0.00
0.00
34
625.57
306.99
128.15
46.71
25.00
15.67
10.90
8.11
6.36
5.15
4.18
3.47
2.27
1.63
1.23
0.96
0.80
0.66
0.49
0.30
0.20
8
66.98
22.83
6.98
1.98
0.93
0.54
0.35
0.25
0.19
0.15
0.12
0.10
0.06
0.05
0.03
0.03
0.02
0.02
0.01
0.01
0.01
35
29.74
10.14
3.10
0.88
0.41
0.24
0.16
0.11
0.08
0.07
0.05
0.04
0.03
0.02
0.02
0.01
0.01
0.01
0.01
0.00
0.00
9
157.00
58.71
19.24
5.76
2.80
1.65
1.10
0.79
0.60
0.48
0.37
0.31
0.20
0.15
0.11
0.08
0.07
0.06
0.04
0.03
0.02
36
69.45
25.79
8.49
2.53
1.23
0.72
0.48
0.35
0.27
0.21
0.17
0.14
0.09
0.07
0.05
0.04
0.03
0.03
0.02
0.01
0.01
1,
1,
10
287.62
116.30
40.50
12.73
6.30
3.75
2.52
.82
,40
1.1-0
0.86
0.72
0.47
0.34
0.25
0.19
0.16
0.13
0.10
0.06
0.04
37
126.67
50.84
17.49
5.46
2.71
1.62
1.09
0.79
0.61
0.49
0.39
0.33
0.22
0.16
0.13
0.10
0.08
0.07
0.05
•0.03
0.02
11
519.57
226.95
85.11
28.45
14.50
8.77
5
4
1.
1.
1.
.98
.14
3.15
2.46
93
62
08
0.78
0.58
0.47
0.37
0.31
0.23
0.14
0.09
38
230.70
99.59
36.60
12.06
6.12
3.73
2.55
1.86
1.45
1.16
0.94
0.79
0.54
0.40
0.30
0.24
0.19
0.16
0.11
0.07
0.05
Volume
Appendix VII-4
External Review Draft
Do Not Cite or Quote
-------
12
1135.47
536.17
227.08
. 87.35
48.16
28.83
19.12
14.09
10.81
8.30
6.98
5.67
3.85
2.85
2.16
1.71
1.40
1.17
0.85
0.50
0.34
39
26.75
9.11
2.79
0.79
0.37
0.21
0.14
0.10
0.08
0 .06
0.05
0.04
0.03
0.02
0.01
0.01
0.01
0.01
0.01
0.00
0.00
13
25.96
S.10
2.32
0.63
0.29
0.17
0.11
0.08
0.06
0.05
0.04
0.03
0.02
0.01
0.01
0.01
0.01
0.01
0.00
0.00
0.00
40
62.31
23.20
7.64
2.28
1.11
0.65
0.44
0.31
0.24
0.19
0.15
0.13
0.09
0.06
0.05
0.04
0.03
0.03
0.02
0.01
0.01
14
53.68
18.27
5.57
1.58
0.74
0.43
0.28
0.20
0.15
0.12-
0.10
0.08
0.05
0.04
0.03
0.02
0.02
0.01
0.01
0.01
0.00
41
114.26
45.61
15.74
4.93
2.44
1.46
0.98
0.71
0.55
0.44
0.35
0.29
0.20
0.15
0.11
0.09
0.07
0.06
0.04
0.03
0.02
15
125.59
46.69
15.27
4.57
2.23
1.31
0.88
0.63
0.48
0.38
0.31
0.26
0.17
0.12
0.09
0.07
0.06
0.05
0.03
0.02
0.01
42
207.36
89.35
32.89
10.83
5.53
3.35
2.28
1.67
1.30
1.04
0.84
0.71
0.48
0.36
0.28
0.22
0.
0,
0.
0.06
0.04
,18
,15
,11
16
229.52
92.36
31.95
10.04
4.96
2.96
1.99
1.44
1.11
0.88
0.71
0.59
0.38
0.28
0.21
0.16
0.13
0.11
0.08
0.05
0.03
43
39.00
14.49
4.77
1.42
0.69
0.41
0.27
0.20
0.15
0.12
0.10
0.08
0.05
0.04
0.03
0.02
0.02
0.02
0.01
0.01
0.00
17
415.69
181.09
67.44
22.39
11.41
6.93
4.69
3.44
2.67
2.10
1.64
1.37
0.90
0.65
0.48
0.38
0.31
0.26
0.19
0.11
0.08
44
70.96
28.45
9.81
3.07
1.52
0.91
0.61
0.44
0.34
0.27
0.22
0.18
0.12
0.09
0.07
0.06
0.05
0.04
0.03
0.02
0.01
Volume VII
Appendix VII-4
External Review Draft
Do Not Cite or Quote
-------
18
964.41
469.61
197.52
74,27
40.14
25.34
16.54
11.84
9.13
7.09
5.79
4.74
3.17
2.32
1.81
1.40
1.17
0.94
0.71
0.42
0.29
45
31.58
11.69
3.84
1.14
0.55
0.33
0.22
0.16
0.12
0.10
0.08
0.06
0.04
0.03
0.02
0.02
0.02
0.01
0.01
0.01
0.00
19
21.64
6.72
1.94
0.52
0.24
0.14
0.09
0.06
0.05
0.04
0.03
0.03
0.02
0.01
0.01
0.01
0.01
0.00
0.00
0.00
0.00
46
56.67
22.73
7.84
2.45
1.22
0.72
0.49
0.35
0.27
0.22
0.18
0.15
0.10
0.07
0.06
0.04
0.04
0.03
0.02
0.01
0.01
20
44.61
15.24
4.65
1.32
0.62
0.36
0.23
0.17
0.13
0.10
0.08
0.07
0.04
0.03
0.02
0.02
0.01
0.01
0.01
0.01
0.00
47
37.85
15.15
5.23
1.63
0.81
0.48
0.33
0.24
0.18
0.15
0.12
0.10
0.07
0.05
0.04
0.03
0.02
0.02
0.02
0.01
0.01
21
104.17
38.81
12.73
3.81
1.85
1.09
0.73
0.52
0.40
0.32
0.25
0.21
0.14
0.10
0.08
0.06
0.05
0.04
0.03
0.02
0.01
48
28.62
11.39
3.93
1.23
0.61
0.36
0.24
0.18
0.14
0.11
0.09
0.07
0.05
0.04
0.03
0.02
0.02
0.0^
0.01
0.01
0.00
22
190.94
76.27
26.46
8.28
4.10
2.45
1.65
1.19
0.92
0.73
0.59
0.49
0.32
0.23
0.18
0.14
0.11
0.09
0.07
0.04
0.03
49
64.99
20.21
5.81
1.58
0.73
0.42
0.26
0.18
0.14
0.10
0.08
0.07
0.04
0.03
0.02
0.02
0.01
0.01
0.01
0.01
0.00
23
346.54
150.36
55.72
18.42
9.36
5.69
3.88
2.83
2.20
1.76
1.42
1.18
0.77
0.55
0.42
0.32
0.27
0.21
0.16
0.10
0.07
50
133.02
45.47
13.95
3
1
1
95
86
07
0.69
0.47
0.36
0.28
0.22
0.18
0.12
0.09
0.06
0.05
0.04
0.03
0.02
0.01
0.01
Volume VH
A .. ,._ .
Appendix VIM
c , B . ^
External Review Draft
_. ... _. _
Do Not Cite or Quote
-------
5
4
24
825.86
403.50
169.90
62.77
33.75
21.20
14.79
10.95
8.23
6.46
04
28
2.86
2.05
1.53
1.24
0.98
0.85
0.61
0.38
0.26
51
319.24
120.82
40.21
12.13
5.87
3.34
2.14
1.52
1.15
0.89
0.71
0.59
0.38
0.27
0.20
0.16
0.13
0.11
0.08
0.05
0.03
25
38.24
13..03
3.99
1.13
0.53
0.31
0.20
0.14
0.11
0.09
0.07
0.06
0.04
0.03
0.02
0.02
0.01
0.01
0.01
0.00
0.00
' 52
571.39
230.17
81.73
26.18
12.86
7.27
4.74
3.41
2.57
1.96
1.62
1.30
0.85
0.62
0.47
0.36
0.30
0.24
0.17
0.10
0.07
26
89.42
33.23
10.90
3.26
1.58
0.93
0.62
0.45
0.34
0.27
0.22
0.18
0.12
0.09
0.07
0.05
0.04
0.04
0.03
0.02
0.01
53
895.39
375.41
145.17
50.96
24.58
14.90
10.09
7.29
5.40
4.39
3.48
2.96
1.98
1.40
1.05
0.84
0.66
0.56
0.39
0.23
0.15
27
163.33
65.48
22.59
7.04
3.50
2.09
1.41
1.02
0.78
0.63
0.50
0.42
0.29
0.20
0.15
0.12
0.10
0.08
0.06
0.04
0.02
54
"1233.92
560.27
256.16
95.44
56.14
37.29
27.29
20.97
16.28
13.41
10.91
9.33
6.36
4.52
3.48.
2.71
2.20
1.77*
1.25
0.70
0.45
Volume VII
Appendix VH-4
External Review Draft
Do Not Cite or Quote
-------
X,m Max concentration, ppm
25.00
50.00
100.00
200.00
300.00 .
400.00
500.00
600.00
700.00
800.00
900.00
1000.00
1250.00
1500.00
1750.00
2000.00
2250.00
2500.00
3000.00
4000.00
5000.00
1277.30
580.01
256.16 —— --
99.28
56.14
37.29
27.29
20.97
16.28
13.41
10.91
9.33
6.36
4.52
3.48
2.71
2.20
1.77
1.25
0.70
0.45
Concentration (ppm)
Distance to (m)
LOG
IDLH
9.6000
19.6000
982.84
629.22
Volume Vn
Appendix VII-4
External Review Draft
Do Not Cite or Quote
-------
From Slab output file:
Scenario:
/' \ Accident Location:
( Duration:
v—-/ Meteorology:
Chemical:
Vapor phase mole fraction:'
LOC :
IDLH:
RUNS9.OUT
TYPICAL
OFFSITE
UNMITIG
INVERSN
FORMALDEHYDE
0.482
9.600
19.600
X,m Max concentration, ppm
25.00
50.00
100.00
200.00
300.00
400.00
500.00
600.00
'"700.00
800.00
900.00
1000.00
1250.00
1500.00
1750.00
--N 2000.00
2250.00
^ 2500.00
3000.00
4000.00
5000.00
1130
552
276
140
93
69
54
44
35
29
25
21
15
11
8
6
5
4
3
1
1
.37
.61
.05
.62
.94
.90
.61
.01
.95
.93
.46
.60
.28
.41
.78
.84
.49
.53
.16
.79
.13
Concentration (ppm)
LOC
IDLH
9.6000
19.6000
Distance to (m)
1671.96
1078.99
Volume YE
Appendix VII-4
External Review Draft
Do Not Cite or Quote
-------
From Slab output file:
Scenario:
Accident Location:
Duration:
Meteorology:
Chemical:
Vapor phase mole fraction:
LOG:
IDLH:
RUN70.OUT
TYPICAL
OFFSITE
UNMITIG
TYPICAL
ACETONE
0.276
1960.000
2442.000
X,m Max concentration, ppm
25,00
50.00
100.00
200.00
300.00
400.00
500.00
'600.00
700.00
800.00
900.00
1000.00
1250.00
1500.00
1750.00
2000.00
2250.00
2500.00
3000.00
4000.00
5000.00
41.15
15.85
5.35
1.65
0.81
0.48
0.32
0.23
0.18
6.14
0.11
0.10
0.06
0.05
0.04
0.03
0.02
0.02
0.01
0.01
0.01
Concentration (ppm)
Distance to (m)
LOG
IDLH
1960.0000
2442.0000
less than
less than
25.00
25.00
Volume Vn
Appendix VII-4
External Review Draft
Do Not Cite or Quote
-------
From Slab output file:
Scenario:
- , Accident Location:
(" Duration:
\v Meteorology:
^ Chemical:
Vapor phase mole fraction:
LOG:
X,m
25.00
50.00
100.00
200.00
300.00
400.00
500.00
600.00
700.00
800.00
900.00
1000.00
1250.00
1500.00
1750.00
2000.00
2250.00
2500.00
3000.00
4000.00
5000.00
X,m
25.00
50.00
100.00
200.00
300.00
400.00
500.00
600.00
700.00
800.00
900.00
1000.00
1250.00
1500.00
1750.00
2000.00
2250.00
2500.00
3000.00
4000.00
5000.00
IDLH;
1
9.34
2.87
0.82
0.22
0.10
0.06
0.04
0.03
0.02
0.02
0.01
0.01
0.01
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
28
68.76
28.81
10.40
3.39
1.71
1.03
0.70
0.51
0.40
0.32
0.25
0.21
0.15
0.11
0.08
0.07
0.05
0.05
0.03
0.02
0.01
— «•— — —
2
19.47
6.51
1.96
0.55
0.26
0.15
0.10
0.07
0.05
0.04
0.03
0.03
0.02
0.01
0.01
0.01
0.01
0.01
0.00
0.00
0.00
29
163.37
77.04
31.56
11.55
6.16
3.85
2.69
1.99
1.56
1.26
1.03
0.87
0.61
0.45
0.35
0.28
0.23
0.20
0.15
0.09
0.07
RUN71.ODT
TYPICAL
OFFSITE
UNMITIG
WORST
ACETONE
0.276
1960.000
2442.000
3
48.75
17.85
5.78
1.71
0.82
0.48
0.32
0.23
0.17
0.14
0.11
0.09
0.06
0.04
0.03
0.03
0.02
0.02
0.01
0.01
0.01
30
7.34
2.45
0.74
0.21
0.10
0.06 -
0.04
0.03
0.02
0.02
0.01
0.01
0.01
0.00
0.00
0.00
0.00
0.0*0
0.00
0.00
0.00
4
89.68
35.26
12.09
3.76
1.86
1.10
0.74
0.53
0.41
0.32
0.26
0.22
0.15
0.11
0.08
0.06
0.05
0.04
0.03
0.02
0.01
31
17.59
6.28
2.00
0.59
0.29
17
11
0.08
0.06
•0.05
0.04
0.03
0.02
0.02
0.01
0.01
0.01
0.01
0.00
0.00
0.00
0,
0,
5
144.78
59.56
22.43
7.73
4.01
2.46
1.69
1.24
0.96
0.77
0.62
0.52
0.36
0.26
0.20
0.16
0.13
0.11
0.08
0.05
0.04
32
32.70
12.55
4.21
1.30
0.64
0.38
0.26
0.18
0.14
0.11
0.09
0.08
0.05
0.04
0.03
0.02
0.02
0.02
0.01
0.01
0.00
Volume VU
Appendix VU-4
External Review Draft
Do Not Cite or Quote
-------
6
202.45
92.62
42.14
18.19
10.78
7.22
5.27
4.05
3.26
2.69
2.23
1.92
1.36
1.03
0.82
0.66
0.55
0.47
0.36
0.22
0.15
33
60.02
25.01
9.01
2.93
1.47
0.89
0.61
0.44
0.34
0.27
0.22
0.19
0.13
0.09
0.07
0.06
0.05
0.04
0.03
0.02
0.01
7
7.01
2.15
0.61
0.16
0.08
0.04
0.03
0.02
0.01
0.01
0.01
0.01
0.01
0.00
0.00
0.00
0.00
0.00
0.00
0.00
- 0.00
34
145.65
68.95
28.21
10.20
5.42
3.37
2.35
1.74
1.36
1.10
0.90
0.76
0.53
0.39
0.30
0.24
0.20
0.17
0.13
0.08
0.06
8
14.69
4.88
1.47
0.41
0.19
0.11
0.07
0.05
0.04
0.03
0.02
0.02
0.01
0.01
0.01
0.01
0.00
0.00
0.00
0.00
0.00
35
6.58
2.18
0.66
0.18
0.09
0.05
0.03
0.02
0.02
0.01
0.01
0.01
0.01
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
9
35.94
13.03
4.20
1.24
0.60
0.35
0.23
0.17
0.13
0.10
0.08
0.07
0.04
0.03
0.02
0.02
0.02
0.01
0.01
0.01
0.00
36
15.63
5.58
1.78
0.53
0.25
0.15
0.10
0.07
0.05
0.04
0.03
0.03
0.02
0.01
0.01
0.01
0.01
O.Ol
0.00
0.00
0.00
10
67.05
26.31
9.00
2.77
1.36
0.81
0.54
0.39
0.30
0.24
0.19
0.16
0.11
0.08
0.06
0.05
0.04
0.03
0.02
0.01
0.01
37
28.89
11.12
3.74
1.15
0.56
0.34
0.23
0.16
0.13
0.10
0.08
0.07
0.05
0.03
0.03
0.02
0.02
0.01
0.01
0.01
0.00
3
1
1
11
118.93
50.05
18.43
6.10
10
88
28
0.93
0.72
0.58
0.46
0.39
0.26
0.19
0.15
0.12
0.10
0.08
0.06
0.04
0.03
38
53.20
22.13
7.93
2.58
1.30
0.78
0.53
0.39
0.30
0.24
0.19
0.16
0.11
0.08
0.06
0.05
0.04
0.04
0.03
0.02
0.01
Volume
. .. ,_ .
Appendix VIM
c . , D ^ „
External Review Draft
-. K, _. _
Do Not Cite or Quote
-------
12
211.19
94.63
40.85
16.45
9.34
6.07
4.35
3.28
2.61
2.14
1.76
1.50
1.05
0.79
0.62
0.50
0.41
0.35
0.26
0.17
0.12
39
6.04
1.99
0.59
0.17
0.08
0.04
0.03
0.02
0.02
0.01
0.01
0.01
0.01
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
13
5.62
1.72
0.49
0.13
0.06
0.03
0.02
0.02
0.01
0.01
0.01
0.01
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
' 40
14.05
5.02
1.61
0.47
0.23
0.13
0.09
0.06
0.05
0.04
0.03
0.03
0.02
0.01
0.01
0.01
0.01
0.01
0.00
0.00
0.00
14
11.75
3.93
1.18
0.33
0.15
0.09
0.06
0.04
0.03
0.02
0.02
0.02
0.01
0.01
0.01
0.00
0.00
0.00
0.00
0.00
0.00
41
26.02
9.97
3.35
1.03
0.51
0.30
0.20
0.15
0.11
0.09
0.07
0.06
0.04
0.03
0.02
0.02
0.01
0.01
0.01
0.01
0.00
15
28.32
10.23
3.28
0.97
0.47
0.27
0.18
0.13
0.10
0.08
0.06
0.05
0.04
0.03
0.02
0.02
0.01
0.01
0.01
0.00
0.00
42
48.01
19.83
7.08
2.29
1.16
0.70
0.48
0.35
0.27
0.22
0.17
0.15
0.10
0.07
0.06
0.05
0.04
0.03
0.02
0.01
0.01
16
53.13
20.66
7.03
2.17
1.06
0.63
0.42
0.31
0.23
0.19
0.15
0.12
0.08
0.06
0.05
0.04
0.03
0.03
0.02
0.01
0.01
43
8.90
3.17
1.01
0.30
0.14
0.08
0.06
0.04
0.03
0.02
0.02
0.02
0.01
0.01
0.01
0.00
0.00
0.00
0.00
0.00
0.00
17
96.58
40.82
14.93
4.88
2.46
1.49
1.01
0.73
0.57
0.45
0.37
0.31
0.21
0.15
0.12
0.09
0.08
0.06
0.05
0.03
0.02
44
16.21
6.19
2.08
0.64
0.31
0.19
0.13
0.09
0.07
0.06
0.04
0.04
0.03
0.02
0.01
0.01
0.01
0.01
0.01
0.00
0.00
Volume VH
Appendix VII-4
External Review Draft
Do Not Cite or Quote
-------
18
202.02
92.13
38.46
. 14.72
8.11
5.17
3.67
2.73
2.16
1.76
1.44
1.22
0.85
0.63
0.50
0.40
0.33
0.28
0.21
0.13
0.09
45
7.10
2.53
0.81
0.24
0.11
0.07
0.04
0.03
0.02
0.02
0.02
0.01
0.01
0.01
0.00
0.00
0.00
0.00
0.00
o.oo
0.00
19
4.67
1..43
0.41
0.11
0.05
0.03
0.02
0.01
0.01
0.01
0.01
0.01
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
46
12.97
4.96
1.66
0.51
0.25
0.15
0.10
0.07
0.06
0.04
0.04
0.03
0.02
0.01
0.01
0.01
0.01
0.01
0.00
o.oo
0.00
20
9.79
3.26
0.98
0.28
0.13
0.07
0.05
0.03
0.03
0.02
0.02
0.01
0.01
0.01
0.00
0.00
0.00
0.00
0.00
0.00
0.00
47
8.69
3.31
1.11
0.34
0.17
0.10
0.07
0.05
0.04
0.03
0.02
0.02
0.01
0.01
0.01
0.01
0.00
0.00
0.00
o.-oo
0.00
21
23.58
8.47
2.70
0.80
0.39
0.23
0.15
0.11
0.08
0.07
0.05
0.04
0.03
0.02
0.02
0.01
0.01
0.01
0.01
0.00
0.00
48
6.51
2.48
0.83
0.25
0.13
0.07
0.05
0.04
0.03
0.02
0.02
0.02
0.01
0.01
0.01
0.00
0.00
0.00
0.00
o.oo
0.00
0
0
22
43.87
16.97
5.75
1.77
0.87
0.52
0.35
0.25
.19
.15
0.12
0.10
0.07
0.05
0.04
0.03
0.02
0.02
0.02
0.01
0.01
49
13.94
4.30
1.22
0.33
0.15
0.09
0.06
0.04
0.03
0.02
0.02
0.02
0.01
0.01
0.01
0.00
0.00
0.00
0.00
o.oo
0.00
2
1
23
80.49
33.84
12.32
4.01
.02
.22
0.83
0.60
0.47
0.37
0.30
0.25
0.17
0.13
0.10
0.08
0.06
0.05
0.04
0.02
0.02
50
30.18
9.91
2.96
0.83
0.39
0.22
0.15
0.10
0.08
0.06
0.05
0.04
0.03
0.02
0.02
0.01
0.01
0.01
0.01
o.oo
0.00
Volume
Appendix VIM
External Review Draft
Do Not Qte
-------
24 25 26. 27
183.28 8.40 20.15 37.34
85.42 2.-80 7.20 14.42
35.14 0.84 2.30 4.86
13.05 0.24 0.68 1.50
7.06 0.11 0.33 0.74
4.44 0.06 0.19 0.44
3.13 0.04 0.13 0.29
2.31 0.03 0.09 0.21
1.82 0.02 0.07 0.16
1.48 0.02 0.06 0.13
1.20 0.01 0.04 0.10
1.02 0.01 0.04 0.09
0.71 0.01 0.03 0.06
0.53 0.01 0.02 0.04
0.41 0.00 0.01 0.03
0.33 0.00 0.01 0.03
0.27 0.00 0.01 0.02
0.23 0.00 0.01 0.02
0.17 0.00 0.01 0.01
0.11 0.00 0.00 0.01
0.08 0.00 0.00 0.01
51 52 53 54
73.22 118.75 151.02 54.32
26.40 45.36 63.43 31.24
8.60 16.22 26.02 18.45
2.59 5.33 9.85 10.80
1.25 2.70 5.37 7.66
0.74 1.63 3.40 5.87
0.49 1.11 2.39 4.73
0.35 0.80 1.78 3.90
0.27 0.62 1.40 3.29
0.21 0.49 1.13 2.79
0.17 0.40 0.92 2.45
0.14 0.33 0.78 2.15
0.09 0.22 0.54 1.63
0.07 0.16 0.39 1.28
0.05 0.13 0.31 1.04
0.04 0.10 0.25 0.86
0.03 0.08 0.20 °*73
0.03 0.07 0.17 0.60
0.02 0.05 0.13 0.45
0.01 0.03 0..08 0.28
0.01 0.02 0.05 0.19
Volume VH External Review Draft
Appendix Vfl-4 • Do Not Cite
-------
X,m Max concentration/ ppm
25.00
50.00
100.00
200.00
300.00
400.00
500.00
600.00
700.00
800.00
900.00
1000.00
1250.00
1500.00
1750.00
2000.00
2250.00
2500.00
3000.00
4000.00
5000.00
211.19
94.63
42.14
18.19
10.78
7.22
5.27
4.05
3.29
2.79
2.45
2.15
1.63
1.28
1.04
0.86
0.73
0.60
0.45
0.28
0.19
Concentration (ppm)
LOG 1960.0000
IDLH 2442.0000
Distance to (m)
less than
less than
25.00
25.00
Volume VII
Appendix VII-4
External Review Draft
Do Not Cite or Quote
-------
From Slab output file:
Scenario:
Accident Location:
; Duration:
v Meteorology:
Chemical:
Vapor phase mole fraction:
LOG:
IDLH:
RUN?2.OUT
TYPICAL
OFFSITE
UNMITIG
INVERSN
ACETONE
0.276
1960.000
2442.000
X,m Max concentration, ppm
• 25.00
50.00
100.00 .
200.00
300.00
400.00
500.00
600.00
'700.00
800.00
900.00
1000.00
1250.00
1500.00
1750.00
<— x 2000.00
2250.00
•,^/ 2500.00
3000.00
4000. 00
5000.00
364.49
166.35
76.63
36.12
23.15
17.15
13.38
10.83
9.08
7.77
6.64
5.87
4.36
3.37
2.67
2.20
1.83
1.54
1.15
0.69
0.46
Concentration (ppm)
Distance to (m)
LOG
IDLH
1960.0000
2442.0000
less than
less than
25.00
25.00
Volume Vn
Appendix VI1-4
External Review Draft
Do Not Cite or Quote
-------
From Slab output file:
Scenario:
Accident Location:
Duration:
Meteorology:
Chemical:
Vapor phase mole fraction:
LOG:
' IDLH:
RUNA7.OUT
TYPICAL
OFFSITE
UNMITIG
INVERSN
ACETONE
0.276
1960.000
2442.000
X,m Max concent rat ion,. ppm
25.00
50.00
100.00
200.00
300.00
400.00
500.00
600.00
' 700.00
800.00
900.00
1000.00
1250.00
1500.00
1750.00
2000.00
2250.00
2500.00
3000.00
4000.00
5000.00
10000.00
15000.00
20000.00
Concentration (ppm)
LOG 1960.0000
IDLH 2442.0000
18.00
8.87
4.94
2.91
2.16
1.72
1.45
1.24
1.08
0'.94
0.83
0.74
0.56
0.44
0.34
0.28
0.23
0.19
0.14
0.08
0.05
0.01
0.01
0.00
Distance to (m)
less than 25.00
less than 25.00
Volume Vn
Appendix VII-4
External Review Draft
Do Not Cite or Quote
-------
ATTACHMENT 4
ISC-COMPDEP Outputs Using Screening Meteorology
Volume VII External Review Draft
Appendix VH-4 Do Not Cite or Quote
-------
A. On-Site Fire Scenario
Volume VII External Review Draft
Appendix VIM Do Not Cite or Quote
-------
CO STARTING
TITLEONE
TJTLETWO
NQDELOPT
AVERT1ME
POLLUTID
TERRHGTS
ELEVUNIT
RUNORNOT
ERRORFIL
CO FINISHED
WTI Storage Tank Rupture, Screen Modeling -- ONSITE ORG.
1 Point source; 26 receptors*up~t
-------
RE FINISHED
NE STARTING _
ME INPUTFIL SCREEN.MET ~
ME ANEMHGHT 10.0 METERS
ME SURFDATA 94823 1993
NE UAIROATA 94823 1993
** ME PROFFILE TEMPS ISCJTENP.STK
** ME PROFFILE WINDS IS(fWIND.STIC
** DAYRANGE 1/3
NE FINISHED
TG STARTING
** INPUTFIL Ht1100k.out
•* LOCATION 538.4 4497.8 km
TG FINISHED
OU STARTING
RECTABLE ALLAVE FIRST-SECOND
DAYTABLE ALLAVE
NAXTABLE ALLAVE SO
** MAXIFILE 3 ALL 30.0 MAXIALL.FIL 25
** NAXIFILE 24 ALL 10.0 MAXIALL.FIL 25
** POSTFILE 1 ALL INDIV POST2C.BIN 20
** POSTFILE PERIOD ALL PLOT PSTANALL.FIL 21
** Note that the following two input cards generate PLOTFILEs with the file
** unit dynamically allocated by the ISCST2 program. Mien porting the model
** to another conputer system, the user may need to specify the file units
** as is done on the previous four input cards.
** PLOTFILE 3 ALL 2ND PLT03ALL.FIL
** PLOTFILE 24 ALL 2ND PLT24ALL.FIL
** OU PLOTFILE 1 ALL 1ST ONSITE.PL1
OU PLOTFILE 1 ALL 1ST ONSITE.PLT
OU FINISHED
*** SETUP Finishes Successfully ***
«»««>••«»••«•«««»»•«••«<«»«*»»»
Volume YE External Review Draft
Appendix VTI-4 Do Not Cite or Quote
-------
*** ISCOMDEP VERSION 94227 *** *** WTI Storage Tank Rupture, Screen Modeling -- ONSITE ORG. TANK ***
•** 1 Point source; 26 receptors up to 50KM away; Vapor. ***
*** MODELING OPTIONS USED: CONC RURAL" TLEV GRDRIS NOSTD
*** MODEL SETUP OPTIONS SUMMARY ***
**Intermediate Terrain Processing is Selected
••Model Is Setup For Calculation of Average concentration Values.
-- SCAVENGING/DEPOSITION LOGIC -
••Model Uses NO DRY DEPLETION. DDPLETE « F
••Model Uses NO WET DEPLETION. UDPLETE = F
**NO WET SCAVENGING Data Provided.
••Model Does NOT Use GRIDDED TERRAIN Data for Depletion Calculations
••Model Uses RURAL Dispersion.
••Model Uses User-Specified Options:
1. Gradual Plune Rise.
2. Not Use Stack-tip Downwash.
3. Buoyancy-induced Dispersion.
4. Calias Processing Routine.
5. Not Use Missing Data Processing Routine.
6. Default Wind Profile Exponents.
7. Default Vertical Potential Temperature Gradients.
••Model Accepts Receptors on ELEV Terrain.
••Model Assumes No FLAGPOLE Receptor Heights.
"Model Calculates 1 Short Ten* Average(s) of: 1-HR
••This Run Includes: 1 Source(s); 1 Source Group(s); and 26 Receptor(s)
••The Model Assumes A Pollutant Type of: FUGITIVE
•model Set To Continue RUNning After the Setup Testing.
••Output Options Selected:
Model Outputs Tables of Highest Short Tern Values fay Receptor (RECTABLE Keyword)
Model Outputs Tables of Overall Maximum Short Ten* Values (MAXTABLE Keyword)
Model Outputs Tables of Concurrent Short Term Values fay Receptor for Each Day Processed (DAYTABLE Keyword)
Model Outputs External File(s) of High Values for Plotting (PLOTFILE Keyword)
••NOTE: The Following Flags Nay Appear Following CONC Values: c tor Cain Hours
• for Missing Hours
b for Both Calm and Missing Hours
•misc. Inputs: Aram. Hgt. (•) « 10.00 ; Decay Coef. * 0.0000 ; Rot. Angle - 0.0
Emission Units * GRAMS/SEC ; Emission Rate Unit Factor • 0.10000E+0
Output Units • MICROGRAMS/M**3
••Input Runstream File: ONSITE.INC ; ••Output Print File: ONSITE.OUT
••Detailed Error/Message File: ONSITE.ERR
Volume VII External Review Draft
Appendix VH-4 Do Not Cite or Quote
-------
•** 1SCOMDEP VERSION 94227 ••* •** W7I Storage Tank Ripture. Screen Modeling -- ONSITE ORG. TANK
*** 1 Point source; 26 receptors ip to 50KM away; Vapor.
*** MODELING OPTIONS USED: CONC RURAL' H6V GRDRIS NOSTD
*** POINT SOURCE DATA ***
NUMBER EMISSION RATE BASE STACK STACK STACK STACK BUILDING EMISSION RATI
SOURCE . PART. (GRAMS/SEC) X Y ELEV. HEIGHT TEMP. EXIT VEL. DIAMETER EXISTS SCALAR VARY
ID CATS. (METERS) (METERS) (METERS) (METERS) (DEG.K) (M/SEC) (METERS) BY
ONSITE 0 0.10000E+01 186.4 105.4 212.1 23.00 997.00 0.22 15.14 YES
Volume VII External Review Draft
Appendix VH-4 Do Not Cite or Quote
-------
*** ISCOMDEP VERSION 94227 *** *** WTI Storage Tank Rupture, Screen Modeling - ONSITE ORG. TANK
*** 1 Point source; 26 receptors up to 50KM away; Vapor.
*** MODELING OPTIONS USED: CONC RURAL "1LEV GRDRIS NOSTD
•** SOURCE IDs DEFINING SOURCE GROUPS
GROUP ID SOURCE IDs
ALL ONSITE ,
Volume VII External Review Draft
Appendix VU-4 Do Not Cite or Quote
-------
*** ISCONDEP VERSION 94227 *** *** WTI Storage Tank Rupture, Screen Modeling - ONSITE ORG. TANK
*** 1 Point source; 26 receptors up to 50KM away; Vapor.
•** MODELING OPTIONS USED: CONC "RURAL "KIEV GRDRIS NOSTD
**• SOURCE PARTICULATE/GAS DATA ***
*** SOURCE ID * ONSITE ; SOURCE TYPE = POINT •** ' •
SCAV COEF [LIQJ 1/(S-MM/HR)=
O.OOE+00.
SCAV COEF [ICE] 1/(S-NM/HR)>
O.OOE+00,
Volume VII External Review Draft
Appendix VIM Do Not Cite or Quote
-------
ISCOMDEP VERSION 94227
WTI Storage Tank Rupture, Screen Model ing •• ONSITE ORG.
1 Point source; 26 receptors up to 50KM away; Vapor.
TANK
*** MODELING OPTIONS USED: CONC RURAL ~ELE~V
GRDRIS NOSTD
DIRECTION SPECIFIC BUILDING DIMENSIONS
SOURCE ID: ONSITE
IFV BH BW UAK
1 17.4, 18.2, 0
7 17.4, 18.2, 0.
13 17.4, 18.2, 0
19 17.4, 18.2, 0
25 17.4, 18.2, 0
31 17.4, 18.2, 0
IFV
2
8
14
20
26
32
BH
17.4,
17.4,
17.4,
17.4,
17.4,
17.4,
BW UAK
18.2, 0
18.2, 0
18.2, 0
18.2, 0
18.2, 0
18.2, 0
IFV
3
9
15
21
27
33
BN
17.4,
17.4,
17.4,
17.4,
17.4,
17.4,
BW UAK
18.2, 0
18.2, 0
18.2, 0
18.2, 0
18.2, 0
18.2, 0
IFV
4
10
16
22
28
34
BH
17.4,
17.4,
17.4,
17.4,
17.4,
17.4,
BW UAK
18.2, 0
18.2, 0
18.2, 0
18.2, 0
18.2, 0
18.2, 0
IFV
5
11
17
23
29
35
BN
17.4.
17.4.
17.4,
17.4.
17.4.
17.4,
BW UAK
18.2, 0
18.2, 0
18.2. 0
18.2, 0
18.2, 0
18.2, 0
IFV
6
12
18
24
30
36
Volume VII
Appendix VTJ-4
External Review Draft
Do Not Cite or Quote
-------
ISCOMDEP VERSION 94227 *•* *** WT1 Storage Tank Rupture, Screen Modeling — ONSITE ORG. TANK
*** 1 Point source; 26 receptors up to 50KM away; Vapor.
MODELING OPTIONS USED: CONC RURAL ~E1EV
GRDRIS NOSTD
*** DISCRETE CARTESIAN RECEPTORS **
(X-COORD, Y-COORD, ZELEV, ZFLAG)
(METERS)
( 100.0,
( 300.0,
( 500.0,
( 700.0,
( 900.0,
( 1250.0,
( 1750.0,
( 2250.0,
( 3000.0,
( 5000.0,
( 10000.0,
( 20000.0,
( 40000.0,
0.0,
0.0,
0.0,
0.0.
o.o.
0.0,
0.0,
0.0,
0.0.
o.o,
o.o.
0.0,
0.0,
213.4,
231.6,
268.2,
323.1,
353.6,
359.7,
365.8,
384.0,
408.4,
415.4,
426.7,
420.0,
420.0,
0.0);
0.0);
0.0);
0.0);
0.0);
0.0);
0.0);
0.0);
0.0);
0.0);
0.0);
0.0);
0.0);
( 200.0,
( 400.0,
( 600.0,
( 800.0,
( 1000.0,
( 1500.0,
( 2000.0,
( 2500.0.
( 4000.0,
( 7500.0,
( 15000.0,
( 30000.0,
( 50000.0,
0.0.
0.0.
0.0,
o.o.
o.o.
0.0,
0.0,
o.o.
0.0,
o.o.
0.0.
0.0.
0.0,
225.6,
231.6,
304.8,
353.6,
353.6,
365.8,
371.9,
384.0,
420.6,
408.4,
420.0,
420.0.
420.0,
0.0);
0.0);
0.0);
0.0);
0.0);
0.0);
0.0);
0.0);
0.0);
0.0);
0.0);
0.0);
0.0);
Volume VH
Appendix VII-4
External Review Draft
Do Not Cite or Quote
-------
*•* 1SCOMDEP VERSION 94227 *** •**
UTI Storage Tank Rupture, Screen Modeling — ONSITE ORG. TANK
1 Point source; 26 receptors up to 50KN away; Vapor.
*** MODELING OPTIONS USED: CONC ROR>1~~ ItEV
GRORIS NOSTD
METEOROLOGICAL DAYS SELECTED FOR PROCESSING
(1-YES; 0-NO)
1 1
1 1
1 1
1 1
1 1
1 1
1 1
1 1
I
1 1
1
1
1
1
1
4
1
1
1
1
1
1
l.<
1 '
1 1 1
I 111
1 1 1
1 1 1
1 1 1
1 1 1
1 1 1
1 1 1
1 1 1
I 1 1
1 1
1 1
1 1
1 1
1 1 1
1 1
1 1 1
1 1 1
1 1 1
1 1 1
1 1 1
1 1 1
1 1 1
^ 1
1
m
«
«
«
1
1
1 1
«
-------
ISCOMDEP VERSION 94227
UTI Storage Tank Rupture. Screen Modeling - ONSITE ORG. TANK
1 Point source; 26 receptors up to 50KM away; Vapor.
**« MODELING OPTIONS USED: CONC RDWkC H.BV
GRDRIS NOSTD
THE FIRST 24 HOURS OF METEOROLOGICAL DATA
FILE: SCREEN.MET
SURFACE STATION NO.: 94823
NAME:-UNKNOWN
YEAR: 1993
FORMAT: (4I2,2F9.4,F6.1,I2,2F7.1,f9.4,f10.1.f8.4,f5.1,i4,f7.2J
UPPER AIR STATION NO.: 94823
NAME: UNKNOWN
YEAR: 1993
YEAR
93
93
93
93
93
93
93
93
93
93
93
93
93
93
93
93
93
93
93
93
93
93
93
93
MONTH DAY HOUR
1 1 1
1 1 2
1 1 3
1 1 4
1 15
1 1 6
1 1 7
1 1 8
1 1 9
1 1 10
*
1
«
1
1
1
•
1
1
1
1
1
1
1
11
12
13
14
15
16
17
18
19
20
21
22
23
24
FLOW
VECTOR
90.0
90.0
90.0
90.0
90.0
90.0
90.0
90.0
90.0
90.0
90.0
90.0
90.0
90.0
90.0
90.0
90.0
90.0
90.0
90.0
90.0
90.0
90.0
90.0
SPEED
(N/S)
1.00
1.50
2.00
2.50
3.00
1.00
1.50
2.00
2.50
3.00
3.50
4.00
4.50
5.00
1.00
1.50
2.00
2.50
3.00
3.50
4.00
4.50
5.00
8.00
TEMP STAB
(K) CLASS
293.1 1
293.1 1
293.1 . 1
293.1 1
293.1 1
293.1 2
293.1 2
293.1 2
293.1 2
293.1 2
293.1 2
293.1 2
293.1 2
293.
293.
293.
293.
293.
293.
293.
293.
293.
293.
293.
2
3
3
3
3
3
3
3
3
3
3
NIXING HEIGHT (M)
RURAL URBAN
320.0
480.0
640.0
800.0
960.0
320.0
480.0
640.0
800.0
960.0
1120.0
1280.0
1440.0
1600.0
320.0
480.0
640.0
800.0
960.0
1120.0
1280.0
1440.0
1600.0
2560.0
320.0
480.0
640.0
800.0
960.0
320.0
480.0
640.0
800.0
960.0
1120.0
1280.0
1440.0
1600.0
320.0
480.0
640.0
800.0
960.0
1120.0
1280.0
1440.0
1600.0
2560.0
USTAR M-0
(M/S) (
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
LENGTH
M)
0.0
0.0
0.0
0.0
0.0
0.0
0.0
0.0
0.0
0.0
0.0
0.0
0.0
0.0
0.0
0.0
0.0
0.0
0.0
0.0
0.0
0.0
0.0
0.0
Z-0 Zd
(M) (M)
0.0000 0.
0.0000 0.
0.0000 0.
0.0000 0.
0.0000 0.
0.0000 0.
0.0000 0.
0.0000 0.
0.0000 0.
0.0000 0.
0.0000 0.
0.0000 0.
O.OOOP^ "*"
o.ooc
0.0000
0.0000 0.
0.0000 0.
0.0000 0.
0.0000 0.
0.0000 0.
0.0000 0.
0.0000 0.
0.0000 0.
0.0000 0.
NOTES: STABILITY CLASS 1«A, 2«B, 3=C, 4=0, 5«E AND 6=F.
FLOW VECTOR IS DIRECTION TOWARD WHICH WIND IS BLOWING.
Volume VJJ
Appendix VII-4
External Review Draft
Do Not Cite or Quote
-------
ISCOMDEP VERSION 94227
UTI Storage Tank Rupture, Screen Modeling -- ONSITE ORG. TANK
1 Point source; 26 receptors up to 50KM away; Vapor.
*** MODELING OPTIONS USED: CONC KDRAL "ELEV
GRORIS NOSTD
CONCURRENT 1-HR AVERAGE CONCENTRATION
FOR SOURCE CROUP: ALL
INCLUDING SOURCE(S): ONSITE ,
VALUES ENDING WITH HOUR 1 FOR DAY 1
DISCRETE CARTESIAN RECEPTOR POINTS
** CONC OF FUGITIVE IN NICROGRAMS/M**3
X-COORD (M) Y-COORD (M)
CONC
X-COORD (M) Y-COORD (M)
CONC
100.00
300.00
500.00
700.00
900.00
1250.00
1750.00
2250.00
3000.00
5000.00
10000.00
20000.00
40000.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00000
0.00000
0.00000
0.00000
0.00000
0.00000
0.00000
0.00000
0.00000
0.00000
0.00000
0.00000
0.00000
200.00
400.00
600.00
800.00
1000.00
1500.00
2000.00
2500.00
4000.00
7500.00
15000.00
30000.00
50000.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00000
0.00000
0.00000
0.00000
0.00000
0.00000
0.00000
0.00000
0.00000
0.00000
0.00000
0.00000
0.00000
Volume VII
Appendix VD-4
External Review Draft
Do Not Cite or Quote
-------
ISCOMDEP VERSION 94227
UTI Storage Tank Rupture, Screen Model in* •• ONSITE ORG.
1 Point source; 26 receptors up to 50KN auay; Vapor.
TANK
MODELING OPTIONS USED: CONC RURAL" ELEV
GRDRIS NOSTD
CONCURRENT 1-HR AVERAGE CONCENTRATION VALUES ENDING WITH HOUR 2 FOR DAY 1
FOR SOURCE GROUP: ALL
INCLUDING SOURCE(S): ONSITE ,
•** DISCRETE CARTESIAN RECEPTOR POINTS ***
** CONC OF FUGITIVE IN MICROGRAMS/M**3 **
X-COORD (M) Y-COORD (M)
CONC
X-COORD (M) Y-COORD (M)
CONC
100.00
300.00
500.00
700.00
900.00
1250.00
1750.00
2250.00
3000.00
5000.00
10000.00
20000.00
40000.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00000
0.00000
0.02293
1.03664
3.49966
3.11532
2.12897
1.61470
1.18499
0.69296
0.34380
0.19011
0.10656
200.00
400.00
600.00
800.00
1000.00
1500.00
2000.00
2500.00
4000.00
7500.00
15000.00
30000.00
50000.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00000
0.00067
0.15725
3.76290
3.62576
2.53176
1.83657
1.44060
0.87455
0.45615
0.24271
0.13527
0.08872
Volume VII
Appendix VTJ-4
External Review Draft
Do Not Cite or Quote
-------
ISCOMDEP VERSION 94227
UTI Storage Tank Rupture, Screen Modeling •- ONSITE ORG. TANK
1 Point source; 26 receptors up to SOW away; Vapor.
*** MODELING OPTIONS USED: CONC RUR>L~ ElEV
GRDRIS NOSTD
CONCURRENT 1-HR AVERAGE CONCENTRATION
FOR SOURCE GROUP: ALL
INCLUDING SOURCE(S): ONSITE ,
VALUES ENDING WITH HOUR 3 FOR DAY 1
DISCRETE CARTESIAN RECEPTOR POINTS
** CONC OF FUGITIVE IN MICROGRANS/M**3
X-COORD (M) Y-COORD (M)
CONC
X-COORD (N) Y-COORD (N)
CONC
100.00
300.00
500.00
700.00
900.00
1250.00
1750.00
2250.00
3000.00
5000.00
10000.00
20000.00
40000.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00000
0.00055
0.45269
2.14537
3.61482
1.81360
1.19755
0.90827
0.66656
0.38979
0.19339
0.10694
0.05994
200.00
400.00
600.00
800.00
1000.00
1500.00
2000.00
2500.00
4000.00
7500.00
15000.00
30000.00
50000.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00000
0.07051
1.03694
4.73459
2.93018
1.42457
1.03307
0.81034
0.49193
0.25658
0.13653
0.07609
0.04990
Volume VII
Appendix VII-4
External Review Draft
Do Not Cite or Quote
-------
ISCOMDEP VERSION 94227
WTI Storage Tank Rupture. Screen Modeling — ONSITE ORG.
1 Point source; 26 receptor* up to 50KM away; Vapor.
TANK
*** MODELING OPTIONS USED: CONC KOHL' -£LEV
GRDRIS NOSTD
CONCURRENT 1-HR AVERAGE CONCENTRATION
FOR SOURCE GROUP: ALL
INCLUDING SOURCE(S): ONSITE .
VALUES ENDING WITH HOUR 4 FOR DAY 1
DISCRETE CARTESIAN RECEPTOR POINTS
** CONC OF FUGITIVE IN MICROGRAMS/M**3
X-COORD (M) Y-COORD (N)
CONC
X-COORD (N) Y-COORD CM)
CONC
100.00
300.00
500.00
700.00
900.00
1250.00
1750.00
2250.00
3000.00
5000.00
10000.00
20000.00
40000.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00000
0.01101
1.53512
2.69253
3.50190
1.33560
0.76647
0.58129
0.42660
0.24947
0.12377
0.06844
0.03836
200.00
400.00
600.00
800.00
1000.00
1500.00
2000.00
2500.00
4000.00
7500.00
15000.00
30000.00
50000.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00000
0.49471
2.18574
4.93815
2.63131
0.92004
0.66117
0.51862
0.31484
0.16421
0.08738
0.04870
0.03194
Volume VII
Appendix VIM
External Review Draft
Do Not Cite or Quote
-------
ISCOMDEP VERSION 94227
UTI Storage Tank nurture, Screen Modeling -- ONSITE ORG.
1 Point source; 26 receptors up to 50KM away; Vapor.
TANK
MODELING OPTIONS USED: COHC RMttT
GRDRIS NOSTD
CONCURRENT 1-HR AVERAGE CONCENTRATION
FOR SOURCE GROUP: ALL
INCLUDING SOURCE(S): ONSITE ,
VALUES ENDING WITH HOUR 5 FOR DAY 1
DISCRETE CARTESIAN RECEPTOR POINTS
CONC OF FUGITIVE IN M1CROGRANS/M**3
X-COORD (N) Y-COORD (M)
CONC
X-COORD (N> Y-COORD (N)
CONC
100.00
300.00
500.00
700.00
900.00
1250.00
1750.00
2250.00
3000.00
5000.00
10000.00
20000.00
40000.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00000
0.04468
2.70007
2.83874
3.23863
1.10840
0.53284
0.40367
0.29625
0.17324
0.08499
0.04210
0.02095
200.00
400.00
600.00
800.00
1000.00
1500.00
2000.00
2500.00
4000.00
7500.00
15000.00
30000.00
50000.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00000
1.25708
3.02139
4.76561
2.33644
0.66585
0.45914
0.36015
0.21864
0.11404
0.05631
0.02798
0.01674
Volume VII
Appendix VD-4
External Review Draft
Do Not Cite or Quote
-------
ISCOMDEP VERSION 94227 **•
MODELING OPTIONS USED: CONC MHOkL" EtEV
*** WTI Storage Tank Rupture, Screen Modeling -- ONSITE ORG. TANK
*** 1 Point source; 26 receptors up to 50KM away; Vapor.
GRDRIS NOSTD
CONCURRENT 1-HR AVERAGE CONCENTRATION
FOR SOURCE GROUP: ALL
INCLUDING SOURCE(S): ONSITE .
VALUES ENDING WITH HOUR 6 FOR DAY 1 ***
DISCRETE CARTESIAN RECEPTOR POINTS
CONC OF FUGITIVE IN MICROGRAMS/M**3
X-COORD (M) Y-COORD (M)
CONC
X-COORD (M) Y-COORD (M)
CONC
100.00
300.00
500.00
700.00
900.00
1250.00
1750.00
2250.00
3000.00
5000.00
10000.00
20000.00
40000.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00000
0.00000
0.00000
0.00000
0.00000
0.00000
0.00000
0.00000
0.00000
0.00000
0.00000
0.00000
0.00000
200.00
400.00
600.00
800.00
1000.00
1500.00
2000.00
2500.00
4000.00
7500.00
15000.00
30000.00
50000.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00000
0.00000
0.00000
0.00000
0.00000
0.00000
0.00000
0.00000
0.00000
0.00000
0.00000
0.00000
0.00000
Volume VII
Appendix VTJ-4
External Review Draft
Do Not Cite or Quote
-------
ISCOHDEP VERSION 94227
*** WTI Storage Tank Rupture, Screen Modeling " ONSITE ORG. TANK
*** 1 Point source; 26 receptors up to 50KM away; Vapor.
*** MODELING OPTIONS USED: CONC RTWDkl" ELEV
GRDRIS NOSTD
*•* CONCURRENT 1-HR AVERAGE CONCENTRATION VALUES ENDING KITH HOUR 7 FOR DAY 1
FOR SOURCE GROUP: ALL
INCLUDING SOURCE(S): ONSITE ,
*** DISCRETE CARTESIAN RECEPTOR POINTS ***
** CONC OF FUGITIVE IN NICROGRANS/M**3 *•
X-COORD (N) Y-COORD (N)
CONC
X-COORD (N) Y-COORD (N)
CONC
100.00
300.00
500.00
700.00
900.00
1250.00
1750.00
2250.00
3000.00
5000.00
10000.00
20000.00
40000.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00000
0.00000
0.00000
0.00009
0.71572
1.07642
1.33757
1.33976
1.17236
0.83007
0.45067
0.24677
0.13666
200.00
400.00
600.00
800.00
1000.00
1500.00
2000.00
2500.00
4000.00
7500.00
15000.00
30000.00
50000.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00000
0.00000
0.00001
0.91164
0.80047
1.27402
1.35620
1.27164
1.00197
0.58033
0.31644
0.17439
0.11328
Volume VH
Appendix VU-4
External Review Draft
Do Not Cite or Quote
-------
ISCOMDEP VERSION 94227
*** UTI Storage Tank Rupture, Screen Modeling - ONSITE ORG. TANK
*** 1 Point source; 26 receptors up to 50KM away; Vapor.
*** MODELING OPTIONS USED: CONC RURAL' ELEV
GRDRIS NOSTD
CONCURRENT 1-HR AVERAGE CONCENTRATION
FOR SOURCE GROUP: ALL
INCLUDING SOURCE(S): ONSITE ,
VALUES ENDING WITH HOUR 8 FOR DAY 1
DISCRETE CARTESIAN RECEPTOR POINTS
** CONC OF FUGITIVE IN MICROGRAMS/K**3
X-COORD (M) Y-COORD (N>
CONC
X-COORD (N) Y-COORD (M)
CONC
100.00
300.00
500.00
700.00
900.00
1250.00
1750.00
2250.00
3000.00
5000.00
10000.00
20000.00
40000.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00000
0.00000
0.00173
0.02279
1.51803
1.88640
1.69324
1.30812
0.85239
0.47050
0.25350
0.13881
0.07687
200.00
400.00
600.00
800.00
1000.00
1500.00
2000.00
2500.00
4000.00
7500.00
15000.00
30000.00
50000.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00000
0.00007
0.00922
1.95133
1.63705
1.87892
1.49577
1.11492
0.59448
0.32644
0.17800
0.09810
0.06372
Volume VH
Appendix VU-4
External Review Draft
Do Not Cite or Quote
-------
ISCOMDEP VERSION 94227
WTI Storage Tank Rupture, Screen Modeling — ONSITE ORG. TANK
1 Point source; 26 receptors i*> to SOKM sway; Vapor.
*** MODELING OPTIONS USED: CONC RURAL EIEV
GRDRIS NOSTD
CONCURRENT 1-HR AVERAGE CONCENTRATION
FOR SOURCE GROUP: ALL
INCLUDING SOURCE(S): ONSITE ,
VALUES ENDING WITH HOUR 9 FOR DAY 1
DISCRETE CARTESIAN RECEPTOR POINTS
CONC OF FUGITIVE IN HICROGRANS/M**3
X-COORD (M) Y-COORD (N)
CONC
X-COORD (N) Y-COORD (N)
CONC
100.00
300.00
500.00
700.00
900.00
1250.00
1750.00
2250.00
3000.00
5000.00
10000.00
20000.00
40000.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00000
0.00001
0.05687
0.24646
2.51236
2.48588
1.78864
1.22950
0.74597
0.32248
0.16224
0.08884
0.04920
200.00
400.00
600.00
800.00
1000.00
1500.00
2000.00
2500.00
4000.00
7500.00
15000.00
30000.00
50000.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00000
0.00548
0.15452
3.28459
2.54448
2.17235
1.47789
1.01387
0.45586
0.20913
0.11392
0.06278
0.04078
Volume VH
Appendix VH-4
External Review Draft
Do Not Cite or Quote
-------
ISCOMDEP VERSION 94227
*•* UTI Storage Tank Rupture, Screen Modeling •- ONSITE ORG. TANK
*** 1 Point source; 26 receptors up to 50KM away; Vapor.
*** MODELING OPTIONS USED: CONC RDfiL" tLEV
CRDRIS NOSTD
CONCURRENT 1-HR AVERAGE CONCENTRATION
FOR SOURCE GROUP: ALL
INCLUDING SOURCE(S): ONSITE ,
VALUES ENDING WITH HOUR 10 FOR DAY 1
DISCRETE CARTESIAN RECEPTOR POINTS
** CONC OF FUGITIVE IN MICROGRANS/M**3
X-COORD (M) Y-COORD (M)
CONC
X-COORD (M) Y-COORD (M)
CONC
100.00
300.00
500.00
700.00
900.00
1250.00
1750.00
2250.00
3000.00
5000.00
10000.00
20000.00
40000.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00000
0.00009
0.32378
0.80167
3.44999
2.80136
1.73919
1.11581
0.65630
0.21649
0.08500
0.04210
0.02095
200.00
400.00
600.00
800.00
1000.00
1500.00
2000.00
2500.00
4000.00
7500.00
15000.00
30000.00
50000.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00000
0.04954
0.62452
4.58698
3.28362
2.23532
1.38067
0.90402
0.34305
0.14669
0.05631
0.02798
0.01674
Volume Vn
Appendix VIM
External Review Draft
Do Not Cite or Quote
-------
ISCOMDEP VERSION 94227
VTI Storage Tank Rupture, Screen Modeling — ONSITE ORG.
1 Point source; 26 receptors up to 50m away; Vapor.
TANK
*** MODELING OPTIONS USED: CONC RURAL ~ELEV
GRDRIS NOSTD
CONCURRENT 1-HR AVERAGE CONCENTRATION
FOR SOURCE GROUP: ALL
INCLUDING SOURCE(S): ONSITE ,
VALUES ENDING WITH HOUR 11 FOR DAY 1
DISCRETE CARTESIAN RECEPTOR POINTS
CONC OF FUGITIVE IN MICROGRAMS/M**3
X-COORD (M) Y-COORD (N)
CONC
X-COORD (M) r-COORD CM)
CONC
100.00
300.00
500.00
700.00
900.00
1250.00
1750.00
2250.00
3000.00
5000.00
10000.00
20000.00
40000.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00000
0.00027
0.83423
1.51564
4.17008
2.90179
1.63359
1.00419
0.54820
0.18369
0.06255
0.03093
0.01539
200.00
400.00
600.00
800.00
1000.00
1500.00
2000.00
2500.00
4000.00
7500.00
15000.00
30000.00
50000.00
0.00
. 0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00000
0.16448
1.33047
5.61981
3.76749
2.17656
1.26494
0.80930
0.29583
0.08777
0.04137
0.02055
0.01230
Volume Vn
Appendix VII-4
External Review Draft
Do Not Cite or Quote
-------
ISCOMDEP VERSION 94227
UTI Storage Tank Rupture, Screen Modelino -• ONSITE ORG.
1 Point source; 26 receptors up to 50KM away; Vapor.
TANK
*** MODELING OPTIONS USED: CONC RURAL "ELEV
GRDRIS NOSTD
CONCURRENT 1-HR AVERAGE CONCENTRATION
FOR SOURCE GROUP: ALL
INCLUDING SOURCE(S): ONSITE ,
VALUES ENDING WITH HOUR 12 FOR DAY 1
DISCRETE CARTESIAN RECEPTOR POINTS
** CONC OF FUGITIVE IN MICROGRANS/M**3
X-COORD (N) Y-COORD (N)
CONC
X-COORD (N) Y-COORD (M)
CONC
100.00
300.00
500.00
700.00
900.00
1250.00
1750.00
2250.00
3000.00
5000.00
10000.00
20000.00
40000.00
0.00
0.00
0.00
0.00
0.00
. 0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00000
0.00047
1.43619
2.17457
4.63402
2.87154
1.51347
0.89720
0.48388
0.16075
0.04823
0.02368
0.01178
200.00
400.00
600.00
800.00
1000.00
1500.00
2000.00
2500.00
4000.00
7500.00
15000.00
30000.00
50000.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00000
0.32855
2.04795
6.30585
4.01892
2.06444
1.15155
0.71627
0.26002
0.07152
0.03167
0.01574
0.00942
Volume YE
Appendix VTJ-4
External Review Draft
Do Not Cite or Quote
-------
ISCOMDEP VERSION 94227
UTI Storage Tank Rupture, Screen Modeling -• ONSITE ORG. TANK
1 Point source; 26 receptors up to 50KM away; Vapor.
MODELING OPTIONS USED: CONC RURAL "ELEV
GRDRIS NOSTD
CONCURRENT 1-HR AVERAGE CONCENTRATION
FOR SOURCE GROUP: ALL
INCLUDING SOURCE(S): ONSITE .
VALUES ENDING VITH HOUR 13 FOR DAY 1
*** DISCRETE CARTESIAN RECEPTOR POINTS
** CONC OF FUGITIVE IN NICROGRANS/M**3
X-COORD (N) Y-COORD (H)
CONC
X-COORD (M) Y-COORD (M)
CONC
100.00
300.00
500.00
700.00
900.00
1250.00
1750.00
2250.00
3000.00
5000.00
10000.00
20000.00
40000.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00000
0.00064
1.97899
2.67886
4.87513
2.74288
1.38101
0.80696
0.43274
0.14312
0.03882
0.01871
0.00931
200.00
400.00
600.00
800.00
1000.00
1500.00
2000.00
2500.00
4000.00
7500.00
15000.00
30000.00
50000.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00000
0.49603
2.63484
6.27253
4.09815
1.90441
1.03949
0.64261
0.23186
0.06134
0.02503
0.01243
0.00744
Volume VII
Appendix VD-4
External Review Draft
Do Not Cite or Quote
-------
ISCOMDEP VERSION 94227
UTI Storage Tank Rupture. Screen Modeling -- ONSITE ORG.
1 Point source; 26 receptors up to 50KM away; Vapor.
TANK
*** MODELING OPTIONS USED: CONC RURAL EIEV
GRDRIS NOSTD
CONCURRENT 1-HR AVERAGE CONCENTRATION
FOR SOURCE GROUP: ALL
INCLUDING SOURCE(S): ONSITE ,
VALUES ENDING WITH HOUR 14 FOR DAY 1
DISCRETE CARTESIAN RECEPTOR POINTS
CONC OF FUGITIVE IN MICROGRAMS/M**3
X-COORD (M) Y-COORD (M)
CONC
X-COORD (N) Y-COORD (N)
CONC
100.00
300.00
500.00
700.00
900.00
1250.00
1750.00
2250.00
3000.00
5000.00
10000.00
20000.00
40000.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00000
0.00075
2.39320
0.00000
4.70917
2.55091
1.26213
0.73255
0.39120
0.12898
0.03251
0.01516
0.00754
200.00
400.00
600.00
800.00
1000.00
1500.00
2000.00
2500.00
4000.00
7500.00
15000.00
30000.00
50000.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00000
0.63576
3.05156
6.05986
3.91382
1.75178
0.94617
0.58227
0.20915
0.05437
0.02028
0.01007
0.00603
Volume VII
Appendix VTJ-4
External Review Draft
Do Not Cite or Quote
-------
1SCOMDEP VERSION 94227
UTI Storage Tank Ripture. Scraan Modeling -• ONSITE ORG.
1 Point source; 26 receptors ip to 50KM away; Vapor.
TANK
*** MODELING OPTIONS USED: CONC RURAL" E1EV
GRORIS NOSTD
CONCURRENT 1-HR AVERAGE CONCENTRATION VALUES ENDING WITH HOUR 15 FOR DAY
FOR SOURCE GROUP: ALL
INCLUDING SOURCE(S): ONSITE ,
*** DISCRETE CARTESIAN RECEPTOR POINTS ***
** CONC OF FUGITIVE IN MICROGRAMS/N**3 **
X-COORD (M) Y-COORD (N>
CONC
X-COORD (N) Y-COORD (N)
CONC
100.00
300.00
500.00
700.00
900.00
1250.00
1750.00
2250.00
3000.00
5000.00
10000.00
20000.00
40000.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00000
0.00000
0.00000
0.00000
0.00000
0.00000
0.00000
0.00000
0.00000
0.00000
0.00000
0.00000
0.00000
200.00
400.00
600.00
800.00
1000.00
1500.00
2000.00
2500.00
4000.00
7500.00
15000.00
30000.00
50000.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00000
0.00000
0.00000
0.00000
0.00000
0.00000
0.00000
0.00000
0.00000
0.00000
0.00000
0.00000
0.00000
Volume VII
Appendix VIJ-4
External Review Draft
Do Not Cite or Quote
-------
ISCOMDEP VERSION 94227
MODELING OPTIONS USED: CONC
VTl Storage Tank Rupture, Screen Modeling — ONSITE ORG. TANK
1 Point source; 26 receptors up to 50KM away; Vapor.
EtEV
GRDRIS NOSTD
CONCURRENT 1-HR AVERAGE CONCENTRATION VALUES ENDING WITH HOUR 16 FOR DAY 1
FOR SOURCE GROUP: ALL
INCLUDING SOURCE(S): ONSITE ,
*** DISCRETE CARTESIAN RECEPTOR POINTS ***
** CONC OF FUGITIVE IN NICROGRANS/M**3 **
X-COORD (M) Y-COORD (M)
CONC
X-COORD (N) Y-COORD (M)
CONC
100.00
300.00
500.00
700.00
900.00
1250.00
1750.00
2250.00
3000.00
5000.00
10000.00
20000.00
40000.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00000
0.00000
0.00000
0.00000
0.35516
0.41352
0.53806
0.69374
0.79637
0.85563
0.62321
0.33855
0.18407
200.00
400.00
600.00
800.00
1000.00
1500.00
2000.00
2500.00
4000.00
7500.00
15000.00
30000.00
50000.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00000
0.00000
0.00000
0.49781
0.35542
0.48755
0.60959
0.71369
0.78297
0.76923
0.43689
0.23681
0.15156
Volume VH
Appendix VTJ-4
External Review Draft
Do Not Cite or Quote
-------
ISCOMDEP VERSION 94227
UTI Storage Tank Rupture, Screen Modeling — ONSITE ORG. TANK
1 Point source; 26 receptors up to 50KM away; Vapor.
MODELING OPTIONS USED: CONC KURA'L "ELEV
GRDRIS NOSTD
*** CONCURRENT 1-HR AVERAGE CONCENTRATION
FOR SOURCE GROUP: ALL
INCLUDING SOURCE(S): ONSITE ,
VALUES ENDING WITH HOUR 17 FOR DAY 1
**• DISCRETE CARTESIAN RECEPTOR POINTS
** CONC OF FUGITIVE IN NICROGRANS/MM3
X-COORD (M) Y-COORD (M)
CONC
X-COORD (N) Y-COORD (M)
CONC
100.00
300.00
500.00
700.00
900.00
1250.00
1750.00
2250.00
3000.00
5000.00
10000.00
20000.00
40000.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00000
0.00000
0.0000*1
0.00004
0.73275
0.89115
1.06070
1.16173
1.06167
0.83088
0.36598
0.19044
0.10354
200.00
400.00
600.00
800.00
1000.00
1500.00
2000.00
2500.00
4000.00
7500.00
15000.00
30000.00
50000.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00000
0.00000
0.00002
1.03478
0.74956
1.01917
1.11316
1.10945
0.99398
0.51434
0.24610
0.13321
0.08525
V
Volume VII
Appendix VIM
External Review Draft
Do Not Cite or Quote
-------
ISCOMDEP VERSION 94227
*** VTI Storage Tank Rupture, Screen Modeling -- ONSITE ORG. TANK
*** 1 Point source; 26 receptors up to 50KH away; Vapor.
MODELING OPTIONS USED: CONC RDR>L~ ELEV
GRORIS NOSTD
CONCURRENT 1-HR AVERAGE CONCENTRATION
FOR SOURCE GROUP: ALL
INCLUDING SOURCE(S): ONSITE ,
VALUES ENDING WITH HOUR 18 FOR DAY 1 •**
DISCRETE CARTESIAN RECEPTOR POINTS
•* CONC OF FUGITIVE IN NICROGRAMS/M**3
X-COORD (M) Y-COORD (N)
CONC
X-COORD (M) Y-COORD (N)
CONC
100.00
.300.00
500.00
700.00
900.00
1250.00
1750.00
2250.00
3000.00
5000.00
10000.00
20000.00
40000.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00000
0.00000
0.00109
0.00519
1.34148
1.54328
1.56730
1.46576
1.28568
0.78552
0.27513
0.12207
0.06627
200.00
400.00
600.00
800.00
1000.00
1500.00
2000.00
2500.00
4000.00
7500.00
15000.00
30000.00
50000.00
0.00
. 0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00000
0.00003
0.00315
1 .90220
1.36445
1.63103
1.51727
1.32860
1.02595
0.43262
0.16141
0.08525
0.05456
Volume VH
Appendix VII-4
External Review Draft
Do Not Cite or Quote
-------
*** ISCOMDEP VERSION 94227
WTI Storage Tank Rupture, Screen Modeling -• ONSITE ORG. TANK
1 Point source; 26 receptors up to 50KM away; Vapor.
MODELING OPTIONS USED: CONC IflRAL "ELHV
GRDRIS NOSTD
CONCURRENT 1-HR AVERAGE CONCENTRATION
FOR SOURCE GROUP: ALL
INCLUDING SOURCE(S): ONSITE ,
VALUES ENDING WITH HOUR 19.FOR DAY 1
DISCRETE CARTESIAN RECEPTOR POINTS
** CONC OF FUGITIVE IN NICROGRAMS/M**3
X-COORD (N) Y-COORD CM)
CONC
X-COORD (M) Y-COORD (M)
CONC
100.00
300.00
500.00
700.00
900.00
1250.00
1750.00
2250.00
3000.00
5000.00
10000.00
20000.00
40000.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00000
0.00000
0.01364
0.06040
2.15941
2.23041
1.92986
1.59504
1.35129
0.45928
0.12558
0.04174
0.02043
200.00
400.00
600.00
800.00
1000.00
1500.00
2000.00
2500.00
4000.00
7500.00
15000.00
30000.00
50000.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00000
0.00032
0.03899
3.06808
2.14426
2.15893
1.74974
1.53797
0.68513
0.37539
0.06134
0.02729
0.01633
Volume YE
Appendix VI1-4
External Review Draft
Do Not Cite or Quote
-------
ISCOMDEP VERSION 94227
WTI Storage Tank Ripture, Screen Modeling -- ONSITE ORG. TANK
1 Point source; 26 receptors up to 50KM away; Vapor.
*** MODELING OPTIONS USED: CONC RURAL
GRDRIS NOSTD
CONCURRENT T-HR AVERAGE CONCENTRATION
FOR SOURCE GROUP: ALL
INCLUDING SOURCE(S): ONSITE ,
VALUES ENDING WITH HOUR 20 FOR DAY 1
DISCRETE CARTESIAN RECEPTOR POINTS
** CONC OF FUGITIVE IN N1CROGRAMS/M**3
X-COORD (M) Y-COORD OO
CONC
X-COORD (N) Y-COORD (M)
CONC
100.00
300.00
500.00
700.00
900.00
1250.00
1750.00
2250.00
3000.00
5000.00
10000.00
20000.00
40000.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00000
0.00000
0.05467
0.23898
3.09171
2.82183
2.13019
1.72940
1.00826
0.40216
0.10814
0.03198
0.01501
200.00
400.00
600.00
800.00
1000.00
1500.00
2000.00
2500.00
4000.00
7500.00
15000.00
30000.00
50000.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00000
0.00127
0.15805
4.39351
2.97184
2.52382
1.83901
1.59844
0.60614
0.18731
0.05051
0.02007
0.01200
Volume VH
Appendix VJJ-4
External Review Draft
Do Not Cite or Quote
-------
ISCOMDEP VERSION 94227
UTI Storage Tank Rupture, Screen Model ing - ONSITE ORG. TANK
1 Point source; 26 receptors up to 50KM away; Vapor.
*** MODELING OPTIONS USED: CONC RURAL " ELEV
GRDRIS NOSTD
CONCURRENT 1-HR AVERAGE CONCENTRATION
FOR SOURCE GROUP: ALL
INCLUDING SOURCE(S): ONSITE ,
VALUES ENDING WITH HOUR 21 FOR DAY 1 ***
DISCRETE CARTESIAN RECEPTOR POINTS
** CONC OF FUGITIVE IN NICROGRAMS/M**3
X-COORD (N) Y-COORD (N)
CONC
X-COORD (N) Y-COORD (M)
CONC
100.00
300.00
500.00
700.00
900.00
1250.00
1750.00
2250.00
3000.00
5000.00
10000.00
20000.00
40000.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00000
0.00000
0.12281
0.54328
4.01496
3.25340
2.20377
1.49681
0.91395
0.35694
0.09500
0.02627
0.01150
200.00
400.00
600.00
800.00
1000.00
1500.00
2000.00
2500.00
4000.00
7500.00
15000.00
30000.00
50000.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00000
0.00281
0.36200
5.69707
3.73007
2.72637
1.80828
1.25509
0.54180
0.16501
0.04370
0.01546
0.00919
Volume Vn
Appendix VTJ-4
External Review Draft
Do Not Cite or Quote
-------
ISCOMDEP VERSION 94227
WT1 Storage Tank Rupture, Screen Modeling — ONSITE ORG. TANK
1 Point source; 26 receptors up to 50KM away; Vapor.
*** MODELING OPTIONS USED: CONC RURAL' "CLEV
GRDRIS NOSTD
CONCURRENT 1-HR AVERAGE CONCENTRATION
FOR SOURCE GROUP: ALL
INCLUDING SOURCE(S): ONSITE ,
VALUES ENDING WITH HOUR 22 FOR DAY 1 ***
*** DISCRETE CARTESIAN RECEPTOR POINTS
** CONC OF FUGITIVE IN NICROGRANS/M**3
X-COORD (M) Y-COORD (M)
CONC
X-COORO (M) Y-COORD (N)
CONC
100.00
300.00
500.00
700.00
900.00
1250.00
1750.00
2250.00
3000.00
5000.00
10000.00
20000.00
40000.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00000
0.00000
0.20044
0.90601
4.73503
3.35772
2.09344
1.38672
0.83313
0.32048
0.08468
0.02267
0.00909
200.00
400.00
600.00
800.00
1000.00
1500.00
2000.00
2500.00
4000.00
7500.00
15000.00
30000.00
50000.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00000
0.00450
0.60350
5.82435
4.29039
2.63454
1.69019
1.15494
0.48890
0.14738
0.03877
0.01241
0.00726
Volume VH
Appendix VI1-4
External Review Draft
Do Not Cite or Quote
-------
ISCOMDEP VERSION 94227
WTI Storage Tank Rupture, Scretn Modeling -• ONSITE ORG.
1 Point source; 26 receptors up to 50KN away; Vapor.
TANK
*** MODELING OPTIONS USED: CONC RDAIT ftEV
GRORIS NOSTD
CONCURRENT 1-HR AVERAGE CONCENTRATION
FOR SOURCE GROUP: ALL
INCLUDING SOURCE(S): ONSITE ,
VALUES ENDING WITH HOUR 23 FOR DAY 1
DISCRETE CARTESIAN RECEPTOR POINTS
*• CONC OF FUGITIVE IN NICROGRANS/M**3
X-COORD (M) Y-COORD (M)
CONC
X-COORD (M) Y-COORD (M)
CONC
100.00
300.00
500.00
700.00
900.00
1250.00
1750.00
2250.00
3000.00
5000.00
10000.00
20000.00
40000.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00000
0.00000
0.27120
0.00000
4.76468
3.26694
1.97521
1.28731
0.76391
0.29055
0.07636
0.02017
0.00739
200.00
400.00
600.00
800.00
1000.00
1500.00
2000.00
2500.00
4000.00
7500.00
15000.00
30000.00
50000.00
0.00
. 0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00000
0.00600
0.83344
5.87911
4.27394
2.51800
1.57989
1.06657
0.44490
0.13310
0.03491
0.01036
0.00588
Volume VII
Appendix VTJ-4
External Review Draft
Do Not Cite or Quote
-------
ISCOMDEP VERSION 94227
VTI Storage Tank Rupture, Screen Modeling -- ONSITE ORG. TANK
1 Point source; 26 receptors up to 50KM away; Vapor.
MODELING OPTIONS USED: CONC WSRf EtEV
GRDRIS NOSTD
CONCURRENT 1-HR AVERAGE CONCENTRATION VALUES ENDING WITH HOUR 24 FDR DAY 1
FOR SOURCE GROUP: ALL
INCLUDING SOURCE(S): ONSITE ,
*** DISCRETE CARTESIAN RECEPTOR POINTS ***
** CONC OF FUGITIVE IN MICROGRAMS/M**3 **
X-COORD (M) Y-COORD (M)
CONC
X-COORD (M) Y-COORD (M)
CONC
100.00
300.00
500.00
700.00
900.00
1250.00
1750.00
2250.00
3000.00
5000.00
10000.00
20000.00
40000.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00000
0.00000
0.40590
0.00000
4.38890
2.60410
1.41706
0.87845
0.50281
0.18527
0.04799
0.01255
0.00341
200.00
400.00
600.00
800.00
1000.00
1500.00
2000.00
2500.00
4000.00
7500.00
15000.00
30000.00
50000.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00000
0.00851
0.00000
5.51516
3.74987
1.88435
1.10085
0.71670
0.28662
0.08397
0.02187
0.00575
0.00242
Volume VII
Appendix VII-4
External Review Draft
Do Not Cite or Quote
-------
ISCOMDEP VERSION 94227
VTI Storage Tank Rupture. Screen Modeling -- ONSITE ORG.
1 Point source; 26 receptors up to 50KM away; Vapor.
TANK
MODELING OPTIONS USED: CONC RDM' ELEV
GRDRIS NOSTD
CONCURRENT 1-HR AVERAGE CONCENTRATION
FOR SOURCE GROUP: ALL
INCLUDING SOURCE(S): ONSITE ,
VALUES ENDING WITH HOUR 1 FOR DAY 2
*** DISCRETE CARTESIAN RECEPTOR POINTS
** CONC OF FUGITIVE IN NICROGRAMS/N**3
X-COORD (N) Y-COORD (N)
CONC
X-COORD (N) Y-COORD (M)
CONC
100.00
300.00
500.00
700.00
900.00
1250.00
1750.00
2250.00
3000.00
5000.00
10000.00
20000.00
40000.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00000
0.00000
0.00000
0.00000
3.96872
2.23194
1.17603
0.71894
0.40758
0.14896
0.03845
0.01004
0.00265
200.00
400.00
600.00
800.00
1000.00
1500.00
2000.00
2500.00
4000.00
7500.00
15000.00
30000.00
50000.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00000
0.00767
0.00000
5.02992
3.32493
1.58334
0.90612
0.58414
0.23105
0.06734
0.01751
0.00459
0.00177
Volume YE
Appendix VTJ-4
External Review Draft
Do Not Cite or Quote
-------
ISCOMDEP VERSION 94227
WTI Storage Tank Rupture, Screen Modeling — ONSITE ORG.
1 Point source; 26 receptors up to 50KM away; Vapor.
TANK
*** MODEL ING OPTIONS USED: CONC RURAL" "ELEV
GRORIS NOSTD
0
J
CONCURRENT 1-HR AVERAGE CONCENTRATION
FOR SOURCE GROUP: ALL
INCLUDING SOURCE(S): ONSITE ,
VALUES ENDING WITH HOUR 2 FOR DAY 2
DISCRETE CARTESIAN RECEPTOR POINTS
*• CONC OF FUGITIVE IN MICROGRANS/M**3
X-COORD (M) Y-COORD (M)
CONC
X-COORD (M) Y-COORD (M)
CONC
100.00
300.00
500.00
700.00
900.00
1250.00
1750.00
2250.00
3000.00
5000.00
10000.00
20000.00
40000.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00000
0.00000
0.00000
0.00000
0.00000
0.00000
0.00000
0.00000
0.00000
0.00000
0.00000
0.00000
0.00000
200.00
400.00
600.00
800.00
1000.00
1500.00
2000.00
2500.00
4000.00
7500.00
15000.00
30000.00
50000.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00000
0.00000
0.00000
0.00000
0.00000
0.00000
0.00000
0.00000
0.00000
0.00000
0.00000
0.00000
0.00000
Volume VII
Appendix VIJ-4
External Review Draft
Do Not Cite or Quote
-------
*** ISCOMDEP VERSION 94227
WTI Storage Tank Rupture, Screen Modeling -• ONSITE ORG. TANK
1 Point source; 26 receptors up to SOKM away; Vapor.
MODELING OPTIONS USED: CONC RTJ8U. ECET
GRDRIS NOSTD
CONCURRENT 1-HR AVERAGE CONCENTRATION
FOR SOURCE GROUP: ALL
INCLUDING SOURCE(S): ONSITE .
VALUES ENDING WITH HOUR 3 FOR DAY
DISCRETE CARTESIAN RECEPTOR POINTS
CONC OF FUGITIVE IN MICROGRAMS/M**3
X-COORD (M) Y-COORD (N)
CONC
X-COORO (N) Y-COORD (M)
CONC
100.00
300.00
500.00
700.00
900.00
1250.00
1750.00
2250.00
3000.00
5000.00
10000.00
20000.00
40000.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00000
0.00000
0.00000
0.00000
0.24351
0.21284
0.19563
0.22522
0.27371
0.26191
0.22724
0.27180
0.22390
200.00
400.00
600.00
800.00
1000.00
1500.00
2000.00
2500.00
4000.00
7500.00
15000.00
30000.00
50000.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00000
0.00000
0.00000
0.35852
0.22329
0.20912
0.20175
0.21971
0.28663
0.22854
0.24962
0.25534
0.19725
Volume V7J
Appendix VTJ-4
External Review Draft
Do Not Cite or Quote
-------
ISCOMDEP VERSION 94227
UTI Storage Tank Ri^ture, Screen Modeling -- ONSITE ORG. TANK
1 Point source; 26 receptors up to 50KM away; Vapor.
*** MODELING OPTIONS USED: CONC RURAL "ELEV
GRDRIS NOSTD
CONCURRENT 1-HR AVERAGE CONCENTRATION
FOR SOURCE GROUP: ALL
INCLUDING SOURCE(S): ONSITE ,
VALUES ENDING WITH HOUR 4 FOR DAY
DISCRETE CARTESIAN RECEPTOR POINTS
CONC OF FUGITIVE IN NtCROGRAMS/M**3
X-COORD (M) Y-COORD (M)
CONC
X-COORD (N) Y-COORD (N)
CONC
100.00
300.00
500.00
700.00
900.00
1250.00
1750.00
2250.00
3000.00
5000.00
10000.00
20000.00
40000.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00000
0.00000
0.00000
0.00000
0.44539
0.42104
0.41134
0.49127
0.59055
0.50098
0.44014
0.35949
0.19203
200.00
400.00
600.00
800.00
1000.00
1500.00
2000.00
2500.00
4000.00
7500.00
15000.00
30000.00
50000.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00000
0.00000
0.00000
0.67296
0.41629
0.43064
0.43323
0.47949
0.58230
0.37728
0.42043
0.25632
0.15120
Volume YE
Appendix VIM
External Review Draft
Do Not Cite or Quote
-------
ISCOMDEP VERSION 94227
WTI Storage Tank Rijjture, Screen Modeling -• ONSITE ORG. TANK
1 Point source; 26 receptors ip to 50KN away; Vapor.
*** MODELING OPTIONS USED: CONC RtftAV ~ELEV
GRDRIS NOSTD
CONCURRENT 1-HR AVERAGE CONCENTRATION
FOR SOURCE GROUP: ALL
INCLUDING SOURCE(S): ONSITE .
VALUES ENDING WITH HOUR 5 FOR DAY 2
DISCRETE CARTESIAN RECEPTOR POINTS
** CONC OF FUGITIVE IN MICROGRAMS/M**3
X-COORD (N) Y-COORD (M)
CONC
X-COORD (N) Y-COORD (M)
CONC
100.00
300.00
500.00
700.00
900.00
1250.00
1750.00
2250.00
3000.00
5000.00
10000.00
20000.00
40000.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00000
0.00000
0.00000
0.00000
0.77806
0.76749
0.75712
0.88218
0.98070
0.70690
0.62717
0.37444
0.17358
200.00
400.00
600.00
800.00
1000.00
1500.00
2000.00
2500.00
4000.00
7500.00
15000.00
30000.00
50000.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00000
0.00000
0.00000
1.19561
0.73619
0.79396
0.79138
0.84609
0.87820
0.65976
0.48507
0.24213
0.13257
Volume Vn
Appendix VIM
External Review Draft
Do Not Cite or Quote
-------
ISCOMDEP VERSION 94227
UTI storage Tank Rupture, Screen Modeling -• ONSITE ORG. TANK
1 Point source; 26 receptors up to 50KN away; Vapor.
*** MODELING OPTIONS USED: CONC RDTOlL " EtEr
CRDRIS NOSTD
CONCURRENT 1-HR AVERAGE CONCENTRATION
FOR SOURCE GROUP: ALL
INCLUDING SOURCE(S): ONSITE ,
VALUES ENDING WITH HOUR 6 FOR DAY
*** DISCRETE CARTESIAN RECEPTOR POINTS
** CONC OF FUGITIVE IN MICROGRAMS/M**3
X-COORD (M) Y-COORD (N)
CONC
X-COORD (N) Y-COORD (N)
CONC
100.00
300.00
500.00
700.00
900.00
1250.00
1750.00
2250.00
3000.00
5000.00
10000.00
20000.00
40000.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00000
0.00000
0.00002
0.00028
1.28131
1.27019
1.21409
1.33047
1.28757
0.78507
0.34188
0.13225
0.04838
200.00
400.00
600.00
800.00
1000.00
1500.00
2000.00
2500.00
4000.00
7500.00
15000.00
30000.00
50000.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00000
0.00000
0.00016
1.98682
1.21696
1.29693
1.23642
1.24433
0.98699
0.49276
0.19830
0.07330
0.03495
Volume Vn
Appendix. V1I-4
External Review Draft
Do Not Cite or Quote
-------
ISCOMDEP VERSION 94227
VTI Storage Tank Ripture, Screen Modeling — ONSITE ORG.
1 Point source; 26 receptors if> to 50KN away; Vapor.
TANK
*** MODELING OPTIONS USED: CONC SOttl" tlEV
GRDRIS NOSTD
CONCURRENT 1-HR AVERAGE CONCENTRATION VALUES ENDING UITH HOUR 7 FOR DAY 2
FOR SOURCE GROUP: ALL
INCLUDING SOURCE(S): ONSITE ,
*** DISCRETE CARTESIAN RECEPTOR POINTS ***
•* CONC OF FUGITIVE IN MICROGRAMS/M**3 *•
X-COORD (M) Y-COORD (N)
CONC
X-COORD (N) Y-COORD (N)
CONC
100.00
300.00
500.00
700.00
900.00
1250.00
1750.00
2250.00
3000.00
5000.00
10000.00
20000.00
40000.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00000
0.00000
0.00013
0.00374
1.97610
1.90724
1.72141
1.67589
1.30014
0.75753
0.31235
0.11705
0.04213
200.00
400.00
600.00
800.00
1000.00
1500.00
2000.00
2500.00
4000.00
7500.00
15000.00
30000.00
50000.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00000
0.00000
0.00162
3.07187
I •BoBBo
1.89053
1.69353
1.53326
0.97189
0.45942
0.17744
0.06415
0.03033
Volume VB
Appendix VIJ-4
External Review Draft
Do Not Cite or Quote
-------
ISCOMDEP VERSION 94227
UTI Storage Tank Rupture, Screen Modeling -• ONSITE ORG.
1 Point source; 26 receptors i*> to SOW away; Vapor.
TANK
*** MODELING OPTIONS USED: CONC ROSXl" ILEV
GRDRIS NOSTD
CONCURRENT 1-HR AVERAGE CONCENTRATION
FOR SOURCE GROUP: ALL
INCLUDING SOURCE(S): ONSITE ,
VALUES ENDING WITH HOUR 8 FOR DAY 2
DISCRETE CARTESIAN RECEPTOR POINTS
CONC OF FUGITIVE IN NICROGRANS/M**3
X-COORD (M) Y-COORD (M)
CONC
X-COORD (M) Y-COORD (M)
CONC
100.00
300.00
500.00
700.00
900.00
1250.00
1750.00
2250.00
3000.00
5000.00
10000.00
20000.00
40000.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00000
0.00000
0.00040
0.01807
2.85100
2.61905
2.09878
1.70063
1.29080
0.72241
0.28562
0.10465
0.03725
200.00
400.00
600.00
800.00
1000.00
1500.00
2000.00
2500.00
4000.00
7500.00
15000.00
30000.00
50000.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00000
0.00000
0.00646
3.99830
2.66761
2.36116
1.88289
1.54437
0.94286
0.42647
0.15986
0.05692
0.02677
Volume Vn
Appendix VI1-4
External Review Draft
Do Not Cite or Quote
-------
ISCO»EP VERSION 94227
VTI Storage Tank Ri?ture, Screen Modeling -• ONSITE ORG. TANK
1 Point source; 26 receptor* i*> to 50KM away; Vapor.
*** MODELING OPTIONS USED: CONC RTJftL" EtEr
GRDRIS NOSTD
CONCURRENT 1-HR AVERAGE CONCENTRATION VALUES ENDING WITH HOUR 9 FOR DAY
FOR SOURCE GROUP: ALL
INCLUDING SCURCE(S): ONSITE ,
*** DISCRETE CARTESIAN RECEPTOR POINTS ***
** CONC OF FUGITIVE IN MICROGRANS/M**3 •*
X-COORD (N) Y-COORD (N)
CONC
X-COORD (N) Y-COORD (N)
CONC
100.00
300.00
500.00
700.00
900.00
12SO.OO
1750.00
2250.00
3000.00
5000.00
10000.00
20000.00
40000.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00000
0.00000
0.00079
0.04941
3.38335
2.77191
2.13556
1.70400
1.26625
0.68469
0.26206
0.09446
0.03336
200.00
400.00
600.00
800.00
1000.00
1500.00
2000.00
2500.00
4000.00
7500.00
15000.00
30000.00
50000.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00000
0.00000
0.01543
4.06616
3.17512
2.41854
1 .90135
1.53582
0.90637
0.39574
0.14508
0.05110
0.02393
Volume VH
Appendix VTJ-4
External Review Draft
Do Not Cite or Quote
-------
ISCOMDEP VERSION 94227
WTI Storage Tank Ripture, Screen Modeling -- ONSITE ORG.
1 Point source; 26 receptors i*> to SOKM away; Vapor.
TANK
*** MODELING OPTIONS USED: CONC «DR>L" ftEV
GRORIS NOSTO
•** CONCURRENT 1-HR AVERAGE CONCENTRATION
FOR SOURCE GROUP: ALL
INCLUDING SOURCE(S): ONSITE ,
VALUES ENDING WITH HOUR 10 FOR DAY
*** DISCRETE CARTESIAN RECEPTOR POINTS
CONC OF FUGITIVE IN MICROGRANS/M**3
X-COORD (M) Y-COORD (M)
CONC
X-COORD (M) Y-COORD
-------
ISCOMDEP VERSION 94227
UTI Storage Tank Rupture, Screen Modeling — ONSITE ORG. TANK
1 Point source; 26 receptors up to 50KN away; Vapor.
*** MOOELIMG OPTIONS USED: CONC HOWL' -EtEV
GRDRIS NOSTD
CONCURRENT 1-HR AVERAGE CONCENTRATION VALUES ENDING WITH HOUR 11 FOR DAY 2
FOR SOURCE GROUP: ALL
INCLUDING SOURCE(S): ONSITE ,
•** DISCRETE CARTESIAN RECEPTOR POINTS •**
** CONC OF FUGITIVE IN NICROGRANS/M**3 **
X-COORD (N) Y-COORD (N)
CONC
X-COORD (N) Y-COORD (M)
CONC
100.00
300.00
500.00
700.00
900.00
1250.00
1750.00
2250.00
3000.00
5000.00
10000.00
20000.00
40000.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00000
0.00000
0.00235
0.00000
3.77197
2.90088
2.00120
1.45757
0.98236
0.46696
0.16122
0.05541
0.01914
200.00
400.00
600.00
800.00
1000.00
1500.00
2000.00
2500.00
4000.00
7500.00
15000.00
30000.00
50000.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00000
0.00000
0.00000
4.50307
3.50857
2.39218
1.69724
1.26581
0.64977
0.25199
0.08645
0.02952
0.01368
Volume VH
Appendix VTJ-4
External Review Draft
Do Not Cite or Quote
-------
ISCOHDEP VERSION 94227
*** UTI Storage Tank Rupture, Screen Modeling -- ONSITE (KG. TANK
*** 1 Point source; 26 receptors up to 50KN away; Vapor.
MODELING OPTIONS USED: CONC TKJRAL ~El£V
GRDRIS NOSTD
CONCURRENT 1-HR AVERAGE CONCENTRATION
FOR SOURCE GROUP: ALL
INCLUDING SOURCE(S): ONSITE .
VALUES ENDING WITH HOUR 12 FOR DAY 2
DISCRETE CARTESIAN RECEPTOR POINTS
CONC OF FUGITIVE IN NICROGRANS/ir**3
X-COORD (M) Y-COORD (M)
CONC
X-COORD (M) Y-COORD (M>
CONC
100.00
300.00
500.00
700.00
900.00
1250.00
1750.00
2250.00
3000.00
5000.00
10000.00
20000.00
40000.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00000
0.00000
0.00000
0.00000
3.80947
2.76574
1.81722
1.28412
0.84217
0.38823
0.13118
0.04468
0.01537
200.00
400.00
600.00
800.00
1000.00
1500.00
2000.00
2500.00
4000.00
7500.00
15000.00
30000.00
50000.00
0.00
. 0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00000
0.00000
0.00000
4.56569
3.48282
2.21922
1.51549
1.10311
0.54633
0.20646
0.06991
0.02373
0.01098
Volume VH
Appendix VU-4
External Review Draft
Do Not Cite or Quote
-------
ISCONDEP VERSION 94227
VT! Storage Tank nurture, Screen Modeling — ONSITE ORG. TANK
1 Point source; 26 receptors 143 to 50KM away; Vapor.
»** MODELING OPTIONS USED: CONC ItifiAL tLEV
GRORIS NOSTD
CONCURRENT 1-HR AVERAGE CONCENTRATION
FOR SOURCE GROUP: ALL
INCLUDING SOURCE(S): ONSITE ,
VALUES ENDING WITH HOUR 13 FOR DAY 2
DISCRETE CARTESIAN RECEPTOR POINTS
CONC OF FUGITIVE IN NICROGRANS/M**3
X-COORD Y-COORD (M)
CONC
X-COORD (M) Y-COORD (N)
CONC
100.00
300.00
500.00
700.00
900.00
1250.00
1750.00
2250.00
3000.00
5000.00
10000.00
20000.00
40000.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00000
0.00000
0.00000
0.00000
3.53466
2.30460
1.40978
0.95736
0.60710
0.27001
0.08907
0.03003
0.01029
200.00
400.00
600.00
800.00
1000.00
1500.00
2000.00
2500.00
4000.00
7500.00
15000.00
30000.00
50000.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00000
0.00000
0.00000
4.28782
3.11489
1.77414
1.14957
0.81127
0.38493
0.14126
0.04715
0.01591
0.00734
Volume VH
Appendix VIJ-4
External Review Draft
Do Not Cite or Quote
-------
ISCGMDEP VERSION 94227
UTI Storage Tank Rupture, Screen Modeling -- ONSITE ORG. TANK
1 Point source; 26 receptors up to 50KM away; Vapor.
MODELING OPTIONS USED: CONC RURAL "ELEV
GRDRIS NOSTD
CONCURRENT 1-HR AVERAGE CONCENTRATION
FOR SOURCE GROUP: ALL
INCLUDING SOURCE(S): ONSITE .
VALUES ENDING WITH HOUR U FOR DAY
*** DISCRETE CARTESIAN RECEPTOR POINTS
*» CONC OF FUGITIVE IN MICROGRANS/M**3
X-COORD (M) Y-COORD (M)
CONC
X-COORD (N) Y-COORD (M)
CONC
100.00
300.00
500.00
700.00
900.00
1250.00
1750.00
2250.00
3000.00
5000.00
10000.00
20000.00
40000.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
o.ooooo
0.00000
0.00000
0.00000
3.11636
1.90977
1.12801
0.75230
0.47013
0.20598
0.06729
0.02260
0.00773
200.00
400.00
600.00
800.00
1000.00
1500.00
2000.00
2500.00
4000.00
7500.00
15000.00
30000.00
50000.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00000
0.00000
0.00000
3.81524
2.68416
1.43998
0.91036
0.63368
0.29522
0.10705
0.03552
0.01195
0.00551
Volume VH
Appendix VH-4
External Review Draft
Do Not Cite or Quote
-------
ISCOHDEP VERSION 94227
UT1 Storage Tank Rupture, Screen Modeling -• ONSITE ORG. TANK
1 Point source; 26 receptors up to 50KN away; Vapor.
*** MODELING OPTIONS USED: CONC RURAL TLEV
GRDRIS NOSTD
CONCURRENT 1-HR AVERAGE CONCENTRATION
FOR SOURCE GROUP: ALL
INCLUDING SOURCE(S): ONSITE ,
VALUES ENDING WITH HOUR 15 FOR DAY
*** DISCRETE CARTESIAN RECEPTOR POINTS
** CONC OF FUGITIVE IN MICROGRAMS/M**3
X-COORD (N) Y-COORD (M)
CONC
X-COORD (M) Y-COORD (N)
CONC
100.00
300.00
500.00
700.00
900.00
1250.00
1750.00
2250.00
3000.00
5000.00
10000.00
20000.00
40000.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00000
0.00000
0.00000
0.00002
53.02272
33.15455
20.53589
13.78308
8.62315
4.10184
1.47648
0.56104
0.21901
200.00
400.00
600.00
800.00
1000.00
1500.00
2000.00
2500.00
4000.00
7500.00
15000.00
30000.00
50000.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00000
0.00000
0.00000
62.57232
45.74073
25.41248
16.78118
11.90994
5.52872
2.35653
0.84673
0.32372
0.16437
Volume VH
Appendix VD-4
External Review Draft
Do Not Cite or Quote
-------
ISCOMDEP VERSION 94227
UTI Storage Tank Rupture, Screen Hotel ing — ONSITE ORG.
1 Point source; 26 receptors up to 50KM away; Vapor.
TANK
*** MODELING OPTIONS USED: CONC RURAL fUV
GRDRIS NOSTD
CONCURRENT 1-HR AVERAGE CONCENTRATION
FOR SOURCE GROUP: ALL
INCLUDING SOURCE(S): ONSITE ,
VALUES ENDING WITH HOUR 16 FOR DAY
DISCRETE CARTESIAN RECEPTOR POINTS
** CONC OF FUGITIVE IN MICROGRAMS/N**3
X-COORD (N) Y-COORD (N)
CONC
X-COORD (M) Y-COORD (N)
CONC
100.00
300.00
500.00
700.00
900.00
1250.00
1750.00
2250.00
3000.00
5000.00
10000.00
20000.00
40000.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00000
0.00000
0.00000
0.00024
37.69915
23.13220
14.12651
9.36406
5.77875
2.70237
0.95701
0.36093
0.14030
200.00
400.00
600.00
800.00
1000.00
1500.00
2000.00
2500.00
4000.00
7500.00
15000.00
30000.00
50000.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00000
0.00000
0.00001
44.66874
32.39180
17.59253
11.47166
8.05933
3.66254
1.53952
0.54635
0.20770
0.10522
Volume VH
Appendix VTJ-4
External Review Draft
Do Not Cite or Quote
-------
*** ISCONDEP VERSION 94227
UTI Storage Tank Rupture, Screen Modeling -- ONSITE ORG. TANK
1 Point source; 26 receptors up to 50KM away; Vapor.
*** MODELING OPTIONS USED: CONC RURAL tLEV
GRDRIS NOSTD
CONCURRENT 1-HR AVERAGE CONCENTRATION
FOR SOURCE GROUP: ALL
INCLUDING SOURCE(S): ONSITE ,
VALUES ENDING WITH HOUR 17 FOR DAY 2
DISCRETE CARTESIAN RECEPTOR POINTS
** CONC OF FUGITIVE IN NICROGRAMS/M**3
X-COORD (M) Y-COORD (M)
CONC
X-COORD (N) Y-COORD (M)
CONC
100.00
300.00
500.00
700.00
900.00
1250.00
1750.00
2250.00
3000.00
5000.00
10000.00
20000.00
40000.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00000
0.00000
0.00000
0.00081
29.41492
17.86273
10.79750
7.09592
4.33881
2.00681
0.70355
0.26419
0.10245
200.00
400.00
600.00
800.00
1000.00
1500.00
2000.00
2500.00
4000.00
7500.00
15000.00
30000.00
50000.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00000
0.00000
0.00002
34.96268
25.19619
13.50803
8.73002
6.09073
2.72924
1.13742
0.40062
0.15179
0.07680
Volume VH
Appendix VD-4
External Review Draft
Do Not Cite or Quote
-------
*** ISCOMDEP VERSION 94227 *** ***
WTI Storage Tank Rupture, Screen Modeling — ONSITE ORG.
1 Point source; 26 receptors up to 50KM away; Vapor.
TANK
MODELIKG OPTIONS USED: CONC RURAL "ELEV
GRDRIS NOSTD
CONCURRENT 1-HR AVERAGE CONCENTRATION VALUES ENDING WITH HOUR 18 FOR DAY
FOR SOURCE GROUP: ALL
INCLUDING SOURCE(S): ONSITE ,
*** DISCRETE CARTESIAN RECEPTOR POINTS ***
** CONC OF FUGITIVE IN MICROGRAMS/M**3 **
X-COORD (M) Y-COORD (N)
CONC
X-COORD (M) Y-COORO (N)
CONC
100.00
300.00
500.00
700.00
900.00
1250.00
1750.00
2250.00
3000.00
5000.00
10000.00
20000.00
40000.00
0.00
0.00
0.00
0.00
0.00
. 0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00000
0.00000
0.00000
0.00168
24.22348
14.58888
8.74911
5.71267
3.46935
1.59211
0.55426
0.20753
0.08035
200.00
400.00
600.00
800.00
1000.00
1500.00
2000.00
2500.00
4000.00
7500.00
15000.00
30000.00
50000.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00000
0.00000
0.00004
28.86622
20.69772
10.98368
7.05054
4.89363
2.17046
0.89920
0.31507
0.11912
0.06021
Volume VH
Appendix VTJ-4
External Review Draft
Do Not Cite or Quote
-------
ISCGMDEP VERSION 94227
UTI Storage Tank Rupture, Screen Modeling -- ONSITE ORG. TANK
1 Point source; 26 receptors up to 50KM away; Vapor.
MODELING OPTIONS USED: CONC RURAL ~ELEV
GRDRIS NOSTD
*** CONCURRENT 1-HR AVERAGE CONCENTRATION VALUES ENDING WITH HOUR 19 FOR DAY 2
FOR SOURCE GROUP: ALL
INCLUDING SOURCE(S): ONSITE ,
*•* DISCRETE CARTESIAN RECEPTOR POINTS ***
** CONC OF FUGITIVE IN MICROGRAMS/M**3 **
X-COORD (M) Y-COORD (M)
CONC
X-COORD (M) Y-COORD (N)
CONC
100.00
300.00
500.00
700.00
900.00
1250.00
1750.00
2250.00
3000.00
5000.00
10000.00
20000.00
40000.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00000
0.00000
0.00000
0.00000
20.64429
12.34844
7.35844
4.78015
2.88771
1.31730
0.45619
0.17047
0.06592
200.00
400.00
600.00
800.00
1000.00
1500.00
2000.00
2500.00
4000.00
7500.00
15000.00
30000.00
50000.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00000
0.00000
0.00008
24.65439
17.60280
9.26369
5.91436
4.08844
1.79905
0.74207
0.25902
0.09777
0.04939
Volume YE
Appendix VTJ-4
External Review Draft
Do Not Cite or Quote
-------
ISCOMDEP VERSION 94227
UTI Storage Tank Rupture, Screen NodeI ins -- ONSITE ORG. TANK
1 Point source; 26 receptors up to 50KM away; Vapor.
MODELING OPTIONS USED: CONC RURAL ~~ELEV
GRORIS NOSTD
CONCURRENT 1-HR AVERAGE CONCENTRATION
FOR SOURCE GROUP: ALL
INCLUDING SOURCE(S): ONSITE ,
VALUES ENDING WITH HOUR 20 FOR DAY 2
DISCRETE CARTESIAN RECEPTOR POINTS
CONC OF FUGITIVE IN NICROGRANS/M**3
X-COORO (N) Y-COORD (N)
CONC
X-COORO (N) Y-COORD (N)
CONC
100.00
300.00
500.00
700.00
900.00
1250.00
1750.00
2250.00
3000.00
5000.00
10000.00
20000.00
40000.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00000
0.00000
0.00000
0.00000
18.01745
10.71480
6.35123
4.10867
2.47146
1.12210
0.38700
0.14439
0.05579
200.00
400.00
600.00
800.00
1000.00
1500.00
2000.00
2500.00
4000.00
7500.00
15000.00
30000.00
50000.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00000
0.00000
0.00011
21.55747
15.33563
8.01418
5.09389
3.50971
1.53460
0.63085
0.21953
0.08276
0.04179
Volume VH
Appendix VTJ-4
External Review Draft
Do Not Cite or Quote
-------
ISCOMDEP VERSION 94227
VT1 Storage Tank Rupture, Screen Modeling — ONSITE ORG. TANK
1 Point source; 26 receptors up to 50KM away; Vapor.
*** MODELING OPTIONS USED: CONC RURAL
GRDRIS NOSTD
CONCURRENT 1-HR AVERAGE CONCENTRATION
FOR SOURCE GROUP: ALL
INCLUDING SOURCE(S): ONSITE .
VALUES ENDING WITH HOUR 21 FOR DAY 2
DISCRETE CARTESIAN RECEPTOR POINTS
** CONC OF FUGITIVE IN MICROGRANS/M**3
X-COORD (N) Y-COORD (M)
CONC
X-COORD (N) Y-COORD (M)
CONC
100.00
300.00
500.00
700.00
900.00
1250.00
1750.00
2250.00
3000.00
5000.00
10000.00
20000.00
40000.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00000
0.00000
0.00000
0.00000
16.00237
9.46883
5.58749
3.60198
2.15899
0.97645
0.33565
0.12508
0.04829
200.00
400.00
600.00
800.00
1000.00
1500.00
2000.00
2500.00
4000.00
7500.00
15000.00
30000.00
50000.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00000
0.00000
0.00014
19.17776
13.59941
7.06426
4.47329
3.07368
1.33690
0.54809
0.19027
0.07166
0.03617
Volume Vn
Appendix VTJ-4
External Review Draft
Do Not Cite or Quote
-------
ISCOMDEP VERSION 94227
VTI Storage Tank Rupture. Screen Modeling •• ONSITE ORG. TANK
1 Point source; 26 receptors up to SOKM away; Vapor.
MODELING OPTIONS USED: CONC SURAL "EtEV
GRORIS NOSTD
CONCURRENT 1-HR AVERAGE CONCENTRATION
FOR SOURCE GROUP: ALL
INCLUDING SOURCE(S): ONSITE ,
VALUES ENDING WITH HOUR 22 FOR DAY 2
DISCRETE CARTESIAN RECEPTOR POINTS
•* CONC OF FUGITIVE IN MICROGRAMS/M**3
X-COORD (M) Y-COORD (N)
CONC
X-COORD (M) Y-COORD (M)
CONC
100.00
300.00
500.00
700.00
900.00
1250.00
1750.00
2250.00
3000.00
5000.00
10000.00
20000.00
40000.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00000
0.00000
0.00000
0.00000
14.40475
8.48609
4.98817
3.20603
1.91587
0.86369
0.29608
0.11022
0.04253
200.00
400.00
600.00
800.00
1000.00
1500.00
2000.00
2500.00
4000.00
7500.00
15000.00
30000.00
50000.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00000
0.00000
0.00000
17.28809
12.22498
6.31715
3.98734
2.73339
1.18362
0.48416
0.16774
0.06313
0.03185
Volume VH
Appendix VTJ-4
External Review Draft
Do Not Cite or Quote
-------
ISCOMDEP VERSION 94227 ***
MODELING OPTIONS USED: CONC RURAT -£LEV
*•* UTI Storage Tank Rupture, Screen Modeling -- ONSITE ORG. TANK
*** 1 Point source; 26 receptors up to 50KM away; Vapor.
GRORIS NOSTD
•** CONCURRENT 1-HR AVERAGE CONCENTRATION VALUES ENDING WITH HOUR 23 FOR DAY
FOR SOURCE GROUP: ALL
INCLUDING SOURCE(S): ONSITE ,
•** DISCRETE CARTESIAN RECEPTOR POINTS ***
** CONC OF FUGITIVE IN NICROGRAMS/M**3 **
X-COORD (N) Y-COORD (M)
CONC
X-COORD (N) Y-COORD (N)
CONC
100.00
300.00
500.00
700.00
900.00
1250.00
1750.00
2250.00
3000.00
5000.00
10000.00
20000.00
40000.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00000
0.00000
0.00000
0.00000
13.10529
7.69050
4.50517
2.88809
1.72138
0.77388
0.26467
0.09845
0.03797
200.00
400.00
600.00
800.00
1000.00
1500.00
2000.00
2500.00
4000.00
7500.00
15000.00
30000.00
50000.00
0.00
. 0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00000
0.00000
0.00000
15.74889
11.10862
5.71383
3.59643
2.46045
1.06137
0.43334
0.14988
0.05637
0.02844
Volume VII
Appendix Vfl-4
External Review Draft
Do Not Cite or Quote
-------
ISCOMDEP VERSION 94227
VTI Storage Tank Rupture, Screen Modeling -- ONSITE ORG.
1 Point source; 26 receptors up to 50KM away; Vapor.
TANK
MODELING OPTIONS USED: CONC RURAL* tLEV
GRDRIS NOSTD
CONCURRENT 1-HR AVERAGE CONCENTRATION
FOR SOURCE GROUP: ALL
INCLUDING SOURCE(S): ONSITE .
VALUES ENDING WITH HOUR 24 FOR DAY 2
DISCRETE CARTESIAN RECEPTOR POINTS
CONC OF FUGITIVE IN NICROGRAM$/M**3
X-COORD (N) Y-COORD (H)
CONC
X-COORD (N) Y-COORD (M)
CONC
100.00
300.00
500.00
700.00
900.00
1250.00
1750.00
2250.00
3000.00
5000.00
10000.00
20000.00
40000.00
0.00
0.00
0.00
0.00
0.00
. 0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00000
0.00000
0.00000
0.00000
54.02040
34.35207
21.72369
14.79566
9.42373
4.73324
1.82605
0.75322
0.31324
200.00
400.00
600.00
800.00
1000.00
1500.00
2000.00
2500.00
4000.00
7500.00
15000.00
30000.00
50000.00
0.00
. 0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00000
0.00000
0.00000
63.41436
46.92068
26.60357
17.90035
12.89174
6.23338
2.82689
1.08768
0.44796
0.23723
Volume YE
Appendix VTJ-4
External Review Draft
Do Not Cite or Quote
-------
ISCOMDEP VERSION 94227
UTI Storage Tank Rupture, Screen Modeling -- ONSITE ORG. TANK
1 Point source; 26 receptors up to 50KM away; Vapor.
MODELING OPTIONS USED: CONC RURAL* *ELEV
GRDRIS NOSTD
CONCURRENT 1-HR AVERAGE CONCENTRATION
FOR SOURCE GROUP: ALL
INCLUDING SOURCE(S): ONSITE ,
VALUES ENDING WITH HOUR 1.FOR DAY 3 •**
DISCRETE CARTESIAN RECEPTOR POINTS
CONC OF FUGITIVE IN NICROGRAMS/N**3
X-COORD (N) Y-COORD (N)
CONC
X-COORD (N) Y-COORD (N)
CONC
100.00
300.00
500.00
700.00
900.00
1250.00
1750.00
2250.00
3000.00
5000.00
10000.00
20000.00
40000.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00000
0.00000
0.00000
0.00000
38.46748
24.23649
15.15639
10.21285
6.42609
3.17854
1.20517
0.49244
0.20355
200.00
400.00
600.00
800.00
1000.00
1500.00
2000.00
2500.00
4000.00
7500.00
15000.00
30000.00
50000.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00000
0.00000
0.00000
45.28408
33.32661
18.65625
12.42282
8.86820
4.20866
1.88087
0.71349
0.29169
0.15394
Volume Vn
Appendix Vfl-4
External Review Draft
Do Not Cite or Quote
-------
ISCOMDEP VERSION 94227
WTI Storage Tank Rupture, Screen Modeling — ONSITE ORG.
1 Point source; 26 receptors up to 50KM away; Vapor.
TANK
*** MODELING OPTIONS USED: CONC RURAL *ELEV
GRDRIS NOSTD
CONCURRENT 1-HR AVERAGE CONCENTRATION
FOR SOURCE GROUP: ALL
INCLUDING SOURCE(S): ONSITE ,
VALUES ENDING WITH HOUR 2 FOR DAY
DISCRETE CARTESIAN RECEPTOR POINTS
** CONC OF FUGITIVE IN NICROGRAMS/M**3
X-COORD (M) Y-COORD (N)
CONC
X-COORD (M) Y-COORD (N)
CONC
100.00
300.00
500.00
700.00
900.00
1250.00
1750.00
2250.00
3000.00
5000.00
10000.00
20000.00
40000.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00000
0.00000
0.00000
0.00000
30.14240
18.86021
11.69847
7.82353
4.88164
2.39006
0.89624
0.36412
0.14997
200.00
400.00
600.00
800.00
1000.00
1500.00
2000.00
2500.00
4000.00
7500.00
15000.00
30000.00
50000.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00000
0.00000
0.00000
35.56019
26.06351
14.45353
9.55245
6.77720
3.17590
1.40597
0.52865
0.21517
0.11332
Volume VII
Appendix VII-4
External Review Draft
Do Not Cite or Quote
-------
ISCOMDEP VERSION 94227
UTI Storage Tank Rupture, Screen Modeling — ONSITE ORG. TANK
1 Point source; 26 receptors up to 50KM away; Vapor.
*** MODELING OPTIONS USED: CONC RlKXL itEIT
GRDRIS NOSTD
CONCURRENT 1-HR AVERAGE CONCENTRATION
FOR SOURCE GROUP: ALL
INCLUDING SOURCE(S): ONSITE ,
VALUES ENDING WITH HOUR 3 FOR DAY
DISCRETE CARTESIAN RECEPTOR POINTS
** CONC OF FUGITIVE IN MICROGRAMS/M**3
X-COORD (N) Y-COORD (M)
CONC
X-COORD (M> Y-COORD (M)
CONC
100.00
300.00
500.00
700.00
900.00
1250.00
1750.00
2250.00
3000.00
5000.00
10000.00
20000.00
40000.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00000
0.00000
0.00000
0.00000
24.89685
15.49300
9.54912
6.34959
3.93725
1.91335
0.71187
0.28810
0.11837
200.00
400.00
600.00
800.00
1000.00
1500.00
2000.00
2500.00
4000.00
7500.00
15000.00
30000.00
50000.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00000
0.00000
0.00000
29.42244
21 .49452
11.83207
7.77493
5.49047
2.54896
1.12086
0.41885
0.16997
0.08939
Volume Vn
Appendix VIJ-4
External Review Draft
Do Not Cite or Quote
-------
ISCOMDEP VERSION 94227
UTI Storage Tank nurture, Screen Modeling -- ONSITE ORG.
1 Point source; 26 receptors up to 50KK away; Vapor.
TANK
MODELING OPTIONS USED: CONC RURAL "ELEV
GRDRIS NOSTD
CONCURRENT 1-HR AVERAGE CONCENTRATION
FOR SOURCE GROUP: ALL
INCLUDING SOURCE(S): ONSITE ,
VALUES ENDING WITH HOUR 4 FOR DAY 3
DISCRETE CARTESIAN RECEPTOR POINTS
CONC OF FUGITIVE IN NICROGRANS/M**3
X-COORD (M) Y-COORD (M)
CONC
X-COORD (N) r-COORD (M)
CONC
100.00
300.00
500.00
700.00
900.00
1250.00
1750.00
2250.00
3000.00
5000.00
10000.00
20000.00
40000.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00000
0.00000
0.00000
0.00000
21.26514
13.17389
8.07817
5.34702
3.29930
1.59413
0.58959
0.23793
0.09758
200.00
400.00
600.00
800.00
1000.00
1500.00
2000.00
2500.00
4000.00
7500.00
15000.00
30000.00
50000.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00000
0.00000
0.00000
25.16628
16.33578
10.03277
6.56213
4.61697
2.12784
0.93093
0.34627
0.14021
0.07367
Volume Vn
Appendix VIM
External Review Draft
Do Not Cite or Quote
-------
ISCOMDEP VERSION 94227
UTI Storage Tank Rijsture, Screen Modeling •- ONSITE ORG. TANK
1 Point source; 26 receptors ip to 50KM away; Vapor.
*** MODELING OPTIONS USED: CONC MftAL TLEV
GRDRIS NOSTD
CONCURRENT 1-HR AVERAGE CONCENTRATION
FOR SOURCE GROUP: ALL
INCLUDING SOURCE(S): ONSITE ,
VALUES ENDING WITH HOUR 5 FOR DAY 3
DISCRETE CARTESIAN RECEPTOR POINTS
** CONC OF FUGITIVE IN MICROGRAMS/M**3
X-COORD (N> Y-COORD (N)
CONC
X-COORD (N) Y-COORD (N)
CONC
100.00
300.00
500.00
700.00
900.00
1250.00
1750.00
2250.00
3000.00
5000.00
10000.00
20000.00
40000.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00000
0.00000
0.00000
0.00000
18.59078
11.47395
7.00580
4.61983
2.83919
1.36549
0.50267
0.20241
0.08290
200.00
400.00
600.00
800.00
1000.00
1500.00
2000.00
2500.00
4000.00
7500.00
15000.00
30000.00
50000.00
0.00
. 0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00000
0.00000
0.00000
22.02755
16.01270
8.71776
5.68021
3.98441
1.82547
0.79545
0.29480
0.11917
0.06256
Volume VH
Appendix VII-4
External Review Draft
Do Not Cite or Quote
-------
ISCOMDEP VERSION 94227
WTI Storage Tank Ripture, Screen Modeling -• ONSITE ORG. TANK
1 Point source; 26 receptors up to 50KM away; Vapor.
*** MODEL ING OPTIONS USED: CONC W&AL "ELEV
GRDRIS NOSTD
CONCURRENT 1-HR AVERAGE CONCENTRATION
FOR SOURCE GROUP: ALL
INCLUDING SOURCE(S): ONSITE ,
VALUES ENDING WITH HOUR 6 FOR DAY
DISCRETE CARTESIAN RECEPTOR POINTS
** CONC OF FUGITIVE IN NICROGRAMS/M**3
X-COORD (M) Y-COORD (M)
CONC
X-COORD (M) Y-COORD (M)
CONC
100.00
300.00
500.00
700.00
900.00
1250.00
1750.00
2250.00
3000.00
5000.00
10000.00
20000.00
40000.00
0.00
0.00
0.00
0.00
0.00
. 0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00000
0.00000
0.00000
0.00000
16.53356
10.17163
6.18814
4.06775
2.49154
1.19372
0.43776
0.17597
0.07199
200.00
400.00
600.00
800.00
1000.00
1500.00
2000.00
2500.00
4000.00
7500.00
15000.00
30000.00
50000.00
0.00
. 0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00000
0.00000
0.00000
19.60995
14. 22777
7.71292
5.00922
3.50485
1.59786
0.69400
0.25645
0.10352
0.05432
Volume Vn
Appendix VTJ-4
External Review Draft
Do Not Cite or Quote
-------
ISCOWEP VERSION 94227
UTI Storage Tank Rupture, Screen Modeling -- ONSITE ORG.
1 Point source; 26 receptors up to SOKM away; Vapor.
TANK
*** MODELING OPTIONS USED: CONC RuHAL~ TLEV
GRORIS NOSTD
THE 1ST HIGHEST 1-HR AVERAGE CONCENTRATION
INCLUDING SOURCE(S): ONSITE ,
VALUES FOR SOURCE GROUP: ALL
DISCRETE CARTESIAN RECEPTOR POINTS
CONC OF FUGITIVE IN NICROGRAMS/M**3
X-COORD (M> Y-COORD (N)
CONC
(YYMMDDHH)
X-COORD (N) Y-COORD (H)
CONC
100.00
300.00
500.00
700.00
900.00
1250.00
1750.00
2250.00
3000.00
5000.00
10000.00
20000.00
40000.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00000
0.04468
2.70007
2.83874
54.02040
34.35207
21.72369
14.79566
9.42373
4.73324
1.82605
0.75322
0.31324
( 0)
(93010105)
(93010105)
(93010105)
(93010224)
(93010224)
(93010224)
(93010224)
(93010224)
(93010224)
(93010224)
(93010224)
(93010224)
200.00
400.00
600.00
800.00
1000.00
1500.00
2000.00
2500.00
4000.00
7500.00
15000.00
30000.00
50000.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00000
1.25708
3.05156
63.41436
46.92068
26.60357
17.90035
12.89174
6.23338
2.82689
1.08768
0.44796
0.23723
(
(93010
(93010
(93010:
(93010
(93010
(93010
(93010
(93010
(93010
(93010
(93010
(93010
Volume Vn
Appendix VJJ-4
External Review Draft
Do Not Cite or Quote
-------
ISCOMDEP VERSION 94227
WTI Storage Tank Rupture, Screen Modeling - ONSITE ORG.
1 Point source; 26 receptors up to 50KM away; Vapor.
TANK
MODELING OPTIONS USED: CONC RURAL' TLEV
GRDRIS NOSTD
THE 2ND HIGHEST 1-HR AVERAGE CONCENTRATION
INCLUDING SOURCE(S): ONSITE ,
VALUES FOR SOURCE GROUP: ALL
DISCRETE CARTESIAN RECEPTOR POINTS
** CONC OF FUGITIVE IN MICROGRAMS/W**3
X-COORD (M) Y-COORD (M)
CONC
(YYMMDDHH)
X-COORD (M) Y-COORD (M)
CONC
(YYmDDN
100.00
300.00
500.00
700.00
900.00
1250.00
1750.00
2250.00
3000.00
5000.00
10000.00
20000.00
40000.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
o.oo
0.00
0.00
0.00
0.00
0.00
0.00000
0.01101
2.39320
2.69253
53.02272
33.15455
20.53589
13.78308
8.62315
4.10184
1.47648
0.56104
0.22390
( 0)
(93010104)
(93010114)
(93010104)
(93010215)
(93010215)
(93010215)
(93010215)
(93010215)
(93010215)
(93010215)
(93010215)
(93010203)
200.00
400.00
600.00
800.00
1000.00
1500.00
2000.00
2500.00
4000.00
7500.00
15000.00
30000.00
50000.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00000
0.63576
3.02139
62.57232
45.74073
25.41248
16.78118
11.90994
5.52872
2.35653
0.84673
0.32372
0.19725
(
(9301011
(9301010
(9301021
(9301021
(9301021
(9301021
(9301021
(9301021
(9301021
(930102'
(930102'
(9301021
Volume VII
Appendix VTJ-4
External Review Draft
Do Not Cite or Quote
-------
ISCONDEP VERSION 94227
VTI Storage Tank Rupture, Screen Modeling — ONSITE ORG. TANK
1 Point source; 26 receptors up to 50KM away; Vapor.
MODELING OPTIONS USED: CONC RWftL * EIEVT
GRDRIS NOSTD
RANK
THE MAXIMUM 50 1-HR AVERAGE CONCENTRATION VALUES FOR SOURCE GROUP: ALL
INCLUDING SOURCE(S): ONSITE ,
** CONC OF FUGITIVE IN MICROGRAMS/M**3
CONC (YYMMDDHH) AT
RECEPTOR (XR.YR) OF TYPE RANK
CONC (YYMMDDHH) AT
RECEPTOR TYPES: GC * GRIDCART
GP * GRIDPOLR
DC = DISCCART
DP - DISCPOLR
BO - BOUNDARY
RECEPTOR (XR
1.
2.
3.
4.
5.
6.
7.
8.
9.
10.
11.
12.
13.
14.
15.
16.
17.
18.
19.
20.
21.
22.
23.
24.
25.
63.41436
62.57232
54.02040
53.02272
46.92068
45.74073
45.28408
44.66874
38.46748
37.69915
35.56019
34.96268
34.35207
33.32661
33.15455
32.39180
30.14240
29.42244
29.41492
28.86622
26.60357
26.06351
25.41248
25.19619
25.16628
(93010224)
(93010215)
(93010224)
(93010215)
(93010224)
(93010215)
(93010301)
(93010216)
(93010301)
(93010216)
(93010302)
(93010217)
(93010224)
(93010301)
(93010215)
(93010216)
(93010302)
(93010303)
(93010217)
(93010218)
(93010224)
(93010302)
(93010215)
(93010217)
(93010304)
AT {
AT (
AT (
AT (
AT (
AT (
AT (
AT (
AT (
AT (
AT (
AT (
AT (
AT (
AT (
AT (
AT (
AT (
AT (
AT (
AT (
AT (
AT (
AT (
AT (
800.00,
800.00,
900.00,
900.00,
1000.00,
1000.00,
800.00,
800.00,
900.00,
900.00,
800.00,
800.00,
1250.00,
1000.00.
1250.00,
1000.00,
900.00,
800.00,
900.00,
800.00,
1500.00,
1000.00,
1500.00,
1000.00,
800.00,
0.00)
0.00)
0.00)
0.00)
0.00)
0.00)
0.00)
0.00)
0.00)
0.00)
0.00)
0.00)
0.00)
0.00)
0.00)
0.00)
0.00)
0.00)
0.00)
0.00)
0.00)
0.00)
0.00)
0.00)
0.00)
DC
DC
oc
DC
DC
DC
DC
DC
DC
DC
DC
DC
DC
DC
DC
DC
DC
DC
DC
DC
DC
DC
DC
DC
DC
26.
27.
28.
29.
30.
31.
32.
33.
34.
35.
36.
37.
38.
39.
40.
41.
42.
43.
44.
45.
46.
47.
48.
49.
50.
24.89685
24.65439
24.23649
24.22348
23.13220
22.02755
21.72369
21.55747
21.49452
21.26514
20.69772
20.64429
20.53589
19.60995
19.17776
18.86021
18.65625
18.59078
18.33578
18.01745
17.90035
17.86273
17.60280
17.59253
17.28809
(93010303)
(93010219)
(93010301)
(93010218)
(93010216)
(93010305)
(93010224)
(93010220)
(93010303)
(93010304)
(93010218)
(93010219)
(93010215)
(93010306)
(93010221)
(93010302)
(93010301)
(93010305)
(93010304)
(93010220)
(93010224)
(93010217)
(93010219)
(93010216)
(93010222)
AT (
AT (
AT {
AT (
AT (
AT (
AT (
AT (
AT (
AT (
AT (
AT (
AT (
AT (
AT (
AT (
AT (
AT (
AT (
AT (
AT (
AT (
AT (
AT {
AT (
900.00,
800.00,
1250.00,
900.00,
1250.00,
800.00,
1750.00,
800.00,
1000.00,
900.00,
1000.00,
900.00,
1750.00,
800.00,
800.00,
1250.00,
1500.00,
900.00,
1000.00,
900.00,
2000.00,
1250.00,
1000.00,
1500:00,
800.00,*
Volume YE
Appendix VTJ-4
External Review Draft
Do Not Cite or Quote
-------
*** ISCOHDEP VERSION 94227 *** *** WTI Storage Tank Rupture, Screen Model ins •- ONSITE ORG. TANK •** 0
**• 1 Point source; 26 receptors up to 50KM way; Vapor. *•* ^ ~-4
*** MODELING OPTIONS USED: CONC RUSXlT ECET GRDRIS NOSTD
*** THE SUMMARY OF HIGHEST 1-HR RESULTS **•
** CONC OF FUGITIVE IN MICROGRAMS/M**3 **
DATE NE
GROUP ID AVERAGE CONC (YYNNDDHH) RECEPTOR (XR, YR. ZELEV, ZFLAG) OF TYPE Gt
ALL HIGH 1ST HIGH VALUE IS 63.41436 ON 93010224: AT ( 800.00. 0.00, 353.60, 0.00) DC
HIGH 2ND HIGH VALUE IS 62.57232 ON 93010215: AT ( 800.00, 0.00, 353.60, 0.00) DC
*** RECEPTOR TYPES: GC = GRIDCART
GP - GRIDPOLR
DC * DISCCART
DP * DISCPOLR
BO * BOUNDARY
Volume VH External Review Draft
Appendix VH-4 Do Not cite or Quote
-------
*** ISCONDEP VERSION 94227 *** **» WTI Storage Tank Rupture, Screen Modeling •• ONSITE ORG. TANK
*** 1 Point source; 26 receptors up to 50KN away; Vapor.
*** MODELING OPTIONS USED: CONC RURAL" "ELEV GRDRIS NOSTD
*** Message Summary : ISCOMDEP Model Execution **•
Summary of Total Messages
A Total of 0 Fatal Error Message(s)
A Total of 0 Warning Nessage(s)
A Total of 0 Informational Message(s)
FATAL ERROR MESSAGES
•** NONE ***
WARNING MESSAGES
*** NONE ***
«>««•«««««>•««««««>•>««»*»«•••>«>•»«•
*** ISCOMDEP Finishes Successfully ***
Volume VH c . . D . _ ^
A .. ._ . External Review Draft
Appendix VD-4 n VT _. _
. Do Not Cite or Quote
-------
B. Off-Site Fire Scenario
Volume VII External Review Draft
Appendix VII-4 Do Not Cite or Quote
-------
>0 STARTING
TITLEONE
x TITLETWO
MGOELOPT
AVERTIME
POLLUTID
TERRHGTS
ELEVUNIT
RUNORNOT
ERRORFIU
CO FINISHED
UTI Truck Accident Off-Site, Screen Modeling - OFFSITE
1 Point source; 26 receptors up to"50 HT abay; Vapor.
GRDRIS NOSTD RURAL CONC
1
Fugitive
ELEV
NETERS
RUN
OFFSITE.ERR
SO STARTING
LOCATION OFFSITE POINT 0.0 0.0 216.4
** Point Source OS HS TS VS OS
** Parameters: "
SO SRCPARAM OFFSITE 1.0 38.0 997. 0.225 30.59
** SO SRCPARAM OFFSITE 1.0 38.0 997. 0.075 52.98
SO SRCGROUP
SO FINISHED
RE STARTING
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
*E DISCCART
(E DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE FINISHED
ME STARTING
ME INPUTFIL
ME ANEMHGHT
ME SURFDATA
ME UAIRDATA
ALL
100.00000
200.00000
300.00000
400.00000
500.00000
600.00000
700.00000
800.00000
900.00000
1000.00000
1250.00000
1500.00000
1750.00000
2000.00000
2250.00000
2500.00000
3000.00000
4000.00000
5000.00000
7500.00000
10000.00000
15000.00000
20000.00000
30000.00000
40000.00000
50000.00000
screen. met
10.0 METERS
94823 1993
94823 1993
0.00000
0.00000
0.00000
0.00000
0.00000
0.00000
0.00000
0.00000
0.00000
0.00000
0.00000
0.00000
0.00000
0.00000
0.00000
0.00000
0.00000
0.00000
0.00000
0.00000
0.00000
0.00000
0.00000
• 0.00000
0.00000
0.00000
292.6
304.8
328.0
347.5
359.7
359.7
356.6
359.7
359.7
371.9
361.5
359.7
359.7
365.8
371.9
408.4
408.4
420.6
415.4
408.4
426.7
420.0
420.0
420.0
420.0
420.0
** ME PROFFILE TEMPS ISC_TEMP.STK
** ME PROFFILE WINDS ISC.UIND.STK
** DAYRANGE 1/3
IE FINISHED
TG STARTING
Volume VH
Appendix VD-4
External Review Draft
Do Not Cite or Quote
-------
** IMPUTFIL
** LOCATION
TG FINISHED
UtHOOk.OUt
538.4 4497.8 km
OU STARTING
RECTABLE ALLAVE FIRST
DAYTABLE1 ALLAVE
NAXTABLE ALLAVE 50
** NAXIFILE 3 ALL 30.0
** NAXIFILE 24 ALL 10.0
** POSTFILE
** POSTFILE
NAXIALL.FIL 25
NAXIALL.FIL 25
1 ALL INOIV POST2C.BIN 20
PERIOD ALL PLOT PSTANALL.FIL 21
** Note that the following two input cards generate PLOTFILEs with the file
** unit dynamically allocated by the ISCST2 program. When porting the model
** to another computer system, the user nay need to specify the file units
** as is done on the previous four input cards.
** PLOTFILE 3 ALL 2ND PLT03ALL.FIL
*• PLOTFILE 24 ALL 2ND PLT24ALL.FIL
OU PLOTFILE 1 ALL FIRST OFFSITE.PLT
*" OU PLOTFILE 1 ALL FIRST OFFSITE.PLT
OU FINISHED
*** Message Sutmary For ISC2 Nodel Setup •**
Summary of Total Messages —
A Total of
A Total of
A Total of
0 Fatal Error Nessage(s)
1 Warning Hessage(s)
0 Informational Nessage(s)
FATAL ERROR MESSAGES
*** NONE ***
******** WARNING MESSAGES •***•***
SO W320 17 PPARN : Source Parameter Nay Be Out-of-Range for Parameter OS
SETUP Finishes Successfully
Volume VII
Appendix VI1-4
External Review Draft
Do Not Cite or Quote
-------
..P^*** ISCOMDEP VERSION 94227 *** *** UTI Truck Accident Off-Site, Screen Modeling -- OFFSITE "* 09/U/9
,' *** 1 Point source; 26 receptors up to 50 KM away; Vapor. •" 12:59:4
V / _ PAGE
•** MODELING OPTIONS USED: CONC RURAL ELEV ~* GRDRIS NOSTD
*" MODEL SETUP OPTIONS SUMMARY ***
«
"Intermediate Terrain Processing is Selected
"Model Is Setup For Calculation of Average Concentration Values.
-- SCAVENGING/DEPOSITION LOGIC —
••Model Uses NO DRY DEPLETION. DDPLETE * F
"Model Uses NO WET DEPLETION. UDPLETE * F
"NO WET SCAVENGING Data Provided.
"Model Does NOT Use GRIDDED TERRAIN Data for Depletion Calculations
"Model Uses RURAL Dispersion.
"Model Uses User-Specified Options:
1. Gradual Plume Rise.
2. Not Use Stack-tip Dounuash.
3. Buoyancy-induced Dispersion.
4. Calms Processing Routine.
5. Not Use Missing Data Processing Routine.
6. Default Wind Profile Exponents.
7. Default Vertical Potential Temperature Gradients.
Accepts Receptors on ELEV Terrain.
"Model Assumes No FLAGPOLE Receptor Heights.
"Model Calculates 1 Short Term Average(s) of: 1-HR
"This Run Includes: 1 Source(s); 1 Source Group(s); and 26 Receptor(s)
"The Model Assumes A Pollutant Type of: FUGITIVE
"Model Set To Continue RUNning After the Setup Testing.
"Output Options Selected:
Model Outputs Tables of Highest Short Term Values by Receptor (RECTABLE Keyword)
Model Outputs Tables of Overall Maximum Short Term Values (NAXTABLE Keyword)
Model Outputs Tables of Concurrent Short Term Values by Receptor for Each Day Processed (DAYTABLE Keyword)
Model Outputs External File(s) of High Values for Plotting (PLOTFILE Keyword)
"NOTE: The Following Flags May Appear Following CONC Values: c for Calm^Hours
m for Missing Hours
b for Both Calm and Missing Hours
"Misc. Inputs: Anew. Hgt. (•) « 10.00 ; Decay Coef. « 0.0000 ; Rot. Angle - 0.0
Emission Units « GRANS/SEC ; Emission Rate Unit Factor - 0.10000E+07
Output Units - NICROGRAMS/M"3
"Input Runstream File: offaite.inp ; "output Print File: off site. 1st
"Detailed Error/Message File: OFFSITE.ERR
Volume VH External Review Draft
Appendix VH-4 Do Not Cite or Quote
-------
ISCOMDEP VERSION 94227
*** UTI Truck Accident Off-Site. Screen Modeling -- OFFSITE
*** 1 Point source; 26 receptors up to 50 KM way; Vapor.
_
*** MODELING OPTIONS USED: COMC RURAL ELEV"" --
09/14/95
12:7'~-*
PA(
GRORIS NOSTD
POINT SOURCE DATA
NUMBER EMISSION RATE BASE STACK STACK STACK STACK BUILDING EMISSION RATE
SOURCE PART. (GRAMS/SEC) X Y ELEV. HEIGHT TEMP. EXIT VEL. DIAMETER EXISTS SCALAR VARY
ID CATS. (METERS) (METERS) (METERS) (METERS) (DEG.K) (M/SEC) (METERS) BY
OFFSITE
0 0.10000E+01
0.0
0.0 216.4 38.00 997.00
0.22 30.59
NO
Volume VII
Appendix VD-4
External Review Draft
Do Not Cite or QuOte
-------
* ISCOMDEP VERSION 94227 *** *** Iff I Truck Accident Off-Site, Screen Modeling - OFFSITE •** 09/14/95
*** 1 Point source; 26 receptors up to SO KM away; Vapor. *** 12:59:4f
_ PACE 3
'*** MODELING OPTIONS USED: CONC RURAL ELETT GRDRIS NOSTD
*** SOURCE IDs DEFINING SOURCE GROUPS
GROUP ID SOURCE IDs
ALL OFFSITE ,
External Review Draft
Append* VD^ Do Not Cite or Quote
-------
*** ISCOMDiP VERSION 94227 •** *** UTI Truck Accident Off-Site. Screen Modeling -- OFFSITE •** 09/14/95
*** 1 Point source; 26 receptors up to 50 KM away; Vapor. •••
PI
*** MODELING OPTIONS USED: COMC RURAL EtEV" GRDR1S NOSTD
*** SOURCE PARTICULATE/6AS DATA ***
*** SOURCE ID * OFFSITE ; SOURCE TYPE = POINT
SCAV COEF [LIQ] 1/»
O.OOE+00,
SCAV COEF [ICE] 1/(S-MM/HR)=
O.OOE+00,
Volume VII External Review Draft
Appendix VII-4 Do Not Cite or Quote
-------
ISCOMDEP VERSION 94227
WTI Truck Accident Off-Site, Screen Model ins — OFFSITE
1 Point source; 26 receptors up to 50 KM away; Vapor.
*** MODELING OPTIONS USED: CONC RURAL f[ffl"
GRDRIS NOSTD
*• DISCRETE CARTESIAN RECEPTORS **
(X-COORD, Y-COORD, ZELEV, ZFLAC)
(METERS)
100.0,
300.0,
500.0,
700.0,
900.0,
1250.0,
1750.0,
2250.0,
3000.0,
5000.0,
10000.0,
20000.0,
40000.0,
0.0,
0.0,
0.0.
0.0,
0.0,
0.0.
0.0,
0.0,
0.0,
0.0,
0.0.
0.0,
0.0.
292.6,
328.0,
359.7,
356.6,
359.7.
361.5,
359.7,
371.9,
408.4,
415.4,
426.7.
420.0.
420.0.
0.0);
0.0);
0.0);
0.0);
0.0);
0.0);
0.0);
0.0);
0.0);
0.0);
0.0);
0.0);
0.0);
200.0,
400.0,
600.0.
800.0.
1000.0,
1500.0.
2000.0,
2500.0,
4000.0,
7500.0.
15000.0,
30000.0.
50000.0.
0.0.
0.0.
0.0.
0.0.
0.0.
0.0.
o.o.
0.0.
0.0.
0.0.
0.0,
0.0,
0.0.
304.8,
347.5,
359.7,
359.7,
371.9,
359.7,
365.8,
408.4.
420.6,
408.4,
420.0,
420.0,
420.0,
0.0);
0.0);
0.0);
0.0);
0.0);
0.0);
0.0);
0.0);
0.0);
0.0);
0.0);
0.0);
0.0);
Volume
Appendix VIM
External Review Draft
Do Not Cite or Quote
-------
ISCONDEP VERSION 94227
UTI Truck Accident Off-Site, Screen Modeling — OFFSITE
1 Point source; 26 receptors up to 50 KM away; Vapor.
*** MODELING OPTIONS USED: CONC RURAL ELEV
GRDRIS NOSTD
09/14/95
12:5P<~'~\
PAr
METEOROLOGICAL DATS SELECTED FOR PROCESSING
(1'YES; 0«NO>
1111
1111
1111
1111
1111
1111
1111
1111
11111
11111
11111
11111
11111
11111
11111
11111
I
11 1
1 1
1 1
1 1
1 1
1 1
1 1
1 1
.
1
*
«
A
1
1
1
I '
1
1
1
1 1 1
1 1 1
1 1 1
1 1 1
1 1 1
1 1 1
1 1 1
1111 11
1111 11
1111 11
1111 11
1111 11
11111 11
11111 11
1
1111
1111
1111
1111
1111
11111
11111
1 1111111111
1 11-11111111
1 1111111111
1 1111111111
1 1111111111
1 1111111111
1 1111111111
NOTE: METEOROLOGICAL DATA ACTUALLY PROCESSED WILL ALSO DEPEND ON WHAT IS INCLUDED IN THE DATA FILE.
UPPER BOUND OF FIRST THROUGH FIFTH WIND SPEED CATEGORIES
(METERS/SEC)
1.54. 3.09. 5.14, 8.23. 10.80.
WIND PROFILE EXPONENTS
STABILITY
CATEGORY
A
B
C
D
E
F
WIND SPEED CATEGORY
1
.70000E-01
.70000E-01
.10000E+00
.15000E+00
.35000E+00
.55000E+00
2
.70000E-01
.70000E-01
.10000E+00
.15000E+00
.350005*00
.55000E+00
3
.7DOOOE-01
.70000E-01
.10000E+00
.15000E+00
.350006*00
.55000E*00
4
.70000E-01
.70000E-01
.10000E+00
,15000E*00
.350006*00
.55000E*00 *
5
.70000E-01
.70000E-01
.10000E+00
.15000E+00
.350006*00
.55000E+00
6
.70000E-01
.700006-01
.100006*00
.150006+00
.350006+00
.550006*00
VERTICAL POTENTIAL TEMPERATURE GRADIENTS
(DEGREES KELVIN PER METER)
STABILITY
CATEGORY
A
B
C
D
E
F
WIND SPEED CATEGORY
1
.OOOOOE+00
.OOOOOE+00
.OOOOOE+00
.OOOOOE+00
.20000E-01
.35000E-01
2
.OOOOOE+00
.OOOOOE+00
.OOOOOE+00
.OOOOOE+00
.200006-01
.35000E-01
3
.OOOOOE+00
.OOOOOE+00
.OOOOOE+00
.OOOOOE+00
.200006-01
.35000E-01
4
t. OOOOOE+00
.OOOOOE+00
.OOOOOE+00
.OOOOOE+00
.200006-01
.35000E-01
5
.OOOOOE+00
.OOOOOE+00
.OOOOOE+00
.OOOOOE+00
.20000E-01
.35000E-01
6
.OOOOOE+00
.OOOOOE+00
.OOOOOE+00
.OOOOOE+00
.20000E-01
.35000E-01
Volume VH
Appendix VII-4
External Review Draft
Do Not Cite or Quote
-------
1SCOMDEP VERSION 94227
VTI Truck Accident Off-Site, Screen Modeling •- OFFSITE
1 Point source; 26 receptors up to 50 KM way; Vapor.
*** MODELING OPTIONS USED: CONC RURAL ELEV
GRDRIS NOSTD
THE FIRST 24 HOURS OF METEOROLOGICAL DATA
FILE: screen.net .
SURFACE STATION NO.: 94823
NAME: UNKNOWN
YEAR: 1993
FORMAT: <4I2,2F9.4,F6.1,I2,2F7.1,f9.4,f10.1,f8.4,f5.1,i4,f7.2>
UPPER AIR STATION NO.: 94823
NAME: UNKNOWN
YEAR: 1993
YEAR MONTH DAY HOUR
FLOW SPEED TEMP
VECTOR (M/S) (K)
STAB MIXING HEIGHT (M)
CLASS RURAL URBAN
USTAR M-0 LENGTH Z-0 Zd IPCOD
(M/S) (M) (M) (M)
93 1 1
93 1 1
93 1 1
93 1 1
93 1 1
93 1 1
93 1 1
93 1 1
93 1
93 1
93 1
93 1
93 1
93 1
93 1
93 1
93 1
93 1
93 1
93 1
93 1
93 1
93 1
93 1 1
1
2
3
4
5
6
7
8
9
10
11
12
13
14
15
16
17
18
19
20
21
22
23
24
90.0 1.00 293.1 1 320.0 320.0 0.0000 0.0 0.0000 0.0 0
90.0 1.50 293.1 1 480.0 480.0 0.0000 0.0 0.0000 0.0 0
90.0 2.00 293.1 1 640.0 640.0 0.0000 0.0 0.0000 0.0 0
90.0 2.50 293.1 1 800.0 800.0 0.0000 0.0 0.0000 0.0 0
90.0 3.00 293.1 1 960.0 960.0 0.0000 0.0 0.0000 0.0 0
90.0 1.00 293.1 2 320.0 320.0 0.0000 0.0 0.0000 0.0 0
90.0 1.50 293. 2 480.0 480.0 0.0000 0.0 0.0000 0.0 0
90.0 2.00 293. 2 640.0 640.0 0.0000 0.0 0.0000 0.0 0
90.0 2.50 293. 2 800.0 800.0 0.0000 0.0 0.0000 0.0 0
90.0 3.00 293. 2 960.0 960.0 0.0000 0.0 0.0000 0.0 0
90.0 3.50 293. 2 1120.0 1120.0 0.0000 0.0 0.0000 0.0 0
90.0 4.00 293. 2 1280.0 1280.0 0.0000 0.0 0.0000 0.0 0
90.0 4.50 293. 2 1440.0 1440.0 0.0000 0.0 0.0000 0.0 0
90.0 5.00 293. 2 1600.0 1600.0 0.0000 0.0 0.0000 0.0 0
90.0 1.00 293.1 3 320.0 320.0 0.0000 0.0 0.0000 0.0 0
90.0 1.50 293.1 3 480.0 480.0 0.0000 0.0 0.0000 0.0 0
90.0 2.00 293.1 3 640.0 640.0 0.0000 0.0 0.0000 0.0 0
90.0 2.50 293. 3 800.0 800.0 0.0000 0.0 0.0000 0.0 0
90.0 3.00 293. 3 960.0 960.0 0.0000 0.0 0.0000 0.0 0
90.0 3.50 293. 3 1120.0 1120.0 0.0000 0.0 0.0000 0.0 0
90.0 4.00 293. 3 1280.0 1280.0 0.0000 0.0 0.0000 0.0 0
90.0 4.50 293. 3 1440.0 1440.0 0.0000 0.0 0.0000 0.0 0
90.0 5.00 293. 3 1600.0 1600.0 0.0000 0.0 0.0000 0.0 0
90.0 8.00 293.1 3 2560.0 2560.0 0.0000 0.0 0.0000 0.0 0
NOTES: STABILITY CLASS 1«A, 2*B, 3=C, 44, 5*E AND 6»F.
FLOW VECTOR IS DIRECTION TOWARD WHICH WIND IS BLOWING.
Volume VH
Appendix VTJ-4
External Review Draft
Do Not Cite or Quote
-------
ISCONDEP VERSION 94227
UTI Truck Accident Off-Site, Screen Nodeling — OFFSITE
1 Point source; 26 receptors up to 50 KM away; Vapor.
NODELING OPTIONS USED: CONC RURAL ELEV
GRORIS NOSTD
09/14/95
12:^-'8
PA
CONCURRENT 1-HR AVERAGE CONCENTRATION
FOR SOURCE GROUP: ALL
INCLUDING SOURCE(S): OFFSITE ,
VALUES ENDING WITH HOUR 1 FOR DAY 1
*** DISCRETE CARTESIAN RECEPTOR POINTS
CONC OF FUGITIVE IN MICROGRAMS/M**3
X-COORD (H) Y-COORD (N>
CONC
X-COORD (N) Y-COORD (N)
CONC
100.00
300.00
500.00
700.00
900.00
1250.00
1750.00
2250.00
3000.00
5000.00
10000.00
20000.00
40000.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.81890
0.00000
0.00000
0.00000
0.00000
0.00000
0.00000
0.00000
0.00000
0.00000
0.00000
0.00000
0.00000
200.00
400.00
600.00
800.00
1000.00
1500.00
2000.00
2500.00
4000.00
7500.00
15000.00
30000.00
50000.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00000
0.00000
0.00000
0.00000
0.00000
0.00000
0.00000
0.00000
0.00000
0.00000
0.00000
0.00000
0.00000
Volume Vn
Appendix VII-4
External Review Draft
Do Not Cite or Quote
-------
ISCOMDEP VERSION 94227
WTI Truck Accident Off-Site, Screen Modeling — OFFSITE
1 Point source; 26 receptors up to 50 KM away; Vapor.
*** MODELING OPTIONS USED: CONC RURAL ELEV
GRORIS NOSTD
09/14/S
12:59:4
PAGE
CONCURRENT 1-HR AVERAGE CONCENTRATION
FOR SOURCE GROUP: ALL
INCLUDING SOURCE(S): OFFSITE ,
VALUES ENDING WITH HOUR 2 FOR DAY 1 »**
DISCRETE CARTESIAN RECEPTOR POINTS
CONC OF FUGITIVE IN NICROGRANS/M**3
X-COORD (M) Y-COORD (M)
CONC
X-COORD (M) r-COORD (M)
CONC
100.00
300.00
500.00
700.00
900.00
1250.00
1750.00
2250.00
3000.00
5000.00
10000.00
20000.00
40000.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
1.09211
0.59055
0.75027
0.00000
0.00000
0.00000
0.00000
0.00000
0.00000
0.00000
0.00000
0.00000
0.00000
200.00
400.00
600.00
800.00
1000.00
1500.00
2000.00
2500.00
4000.00
7500.00
15000.00
30000.00
50000.00
0.00
0.00.
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.62507
0.61457
0.00000
0.00000
0.00000
0.00000
0.00000
0.00000
0.00000
0.00000
0.00000
0.00000
0.00000
Volume VIJ
Appendix VTJ-4
External Review Draft
Do Not Cite or Quote
-------
ISCOMDEP VERSION 94227
UTI Truck Accident Off-Site, Screen Modeling -- OFFSITE
1 Point source; 26 receptors up to 50 KM euay; Vapor.
*** MODELING OPTIONS USED: CONC RURAL ETEv"
GRDRIS NOSTD
09/14/95
P/
CONCURRENT 1-HR AVERAGE CONCENTRATION
FOR SOURCE GROUP: ALL
INCLUDING SOURCE(S): OFFSITE .
VALUES ENDING WITH HOUR 3 FOR DAY . 1
DISCRETE CARTESIAN RECEPTOR POINTS
** CONC OF FUGITIVE IN NICROGRAMS/M**3
X-COORD (M) Y-COORD (M)
CONC
X-COORD (M) Y-COORD (M)
CONC
100.00
300.00
500.00
700.00
900.00
1250.00
1750.00
2250.00
3000.00
5000.00
10000.00
20000.00
40000.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
1.55244
1.17569
1.46886
1.62981
1.62013
0.00000
0.00000
0.00000
0.00000
0.00000
0.00000
0.00000
0.00000
200.00
400.00
600.00
800.00
1000.00
1500.00
2000.00
2500.00
4000.00
7500.00
15000.00
30000.00
50000.00
0.00
O.OQ
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
1.08747
1.29777
1.62803
1.60347
1.64727
0.00000
0.00000
0.00000
0.00000
0.00000
0.00000
0.00000
0.00000
Volume VII
Appendix VII-4
External Review Draft
Do Not Cite or Quote
-------
ISCOHDEP VERSION 94227
UTI Truck Accident Off-Site, Screen Modeling - OFFSITE
1 Point source; 26 receptors up to SO KM away; Vapor.
*** MODELING OPTIONS USED: CONC RURAL El£V '
GRDRIS NOSTO
09/14/
12:59:
PAGE
CONCURRENT 1-HR AVERAGE CONCENTRATION
FOR SOURCE GROUP: ALL
INCLUDING SOURCE(S): OFFSITE ,
VALUES ENDING WITH HOUR 4 FOR DAY 1
*** DISCRETE CARTESIAN RECEPTOR POINTS
** CONC OF FUGITIVE IN MICROGRAMS/M**3
X-COORD (M) Y-COORD (M)
CONC
X-COORD (N) Y-COORD (M)
CONC
100.00
300.00
500.00
700.00
900.00
1250.00
1750.00
2250.00
3000.00
5000.00
10000.00
20000.00
40000.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
2.27503
2.10901
2.37484
2.02377
1.41099
0.92261
0.66265
0.51540
0.38655
0.23193
0.11740
0.06552
0.03689
200.00
400.00
600.00
800.00
1000.00
1500.00
2000.00
2500.00
4000.00
7500.00
15000.00
30000.00
50000.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
1 .84501
2.28176
2.29886
1.71558
1.19607
0.77306
0.57982
0.46386
0.28991
0.15462
0.08340
0.04676
0.03074
Volume YE
Appendix VTJ-4
External Review Draft
Do Not Cite or Quote
-------
ISCOMDEP VERSION 94227
UTI Truck Accident Off-Site, Screen Modeling -- OFFSITE
1 Point source; 26 receptors up to 50 KM away; Vapor.
09/14/95
12-48
*** MODELING OPTIONS USED: CONC RURAL ELEV
GRDRIS NOSTD
CONCURRENT 1-HR AVERAGE CONCENTRATION
FOR SOURCE GROUP: ALL
INCLUDING SOURCE(S): OFFSITE ,
VALUES ENDING WITH HOUR 5 FOR DAY 1 ***
DISCRETE CARTESIAN RECEPTOR POINTS
** CONC OF FUGITIVE IN MICR06RAMS/M**3
X-COORO (M) Y-COORD (M)
CONC
X-COORD (N) Y-COORD (M)
CONC
100.00
300.00
500.00
700.00
900.00
1250.00
1750.00
2250.00
3000.00
5000.00
10000.00
20000.00
40000.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
3.34302
3.35501
3.20150
2.20528
1.35652
0.66945
0.46018
0.35791
0.26844
0.16106
0.08163
0.04552
0.02562
200.00
400.00
600.00
800.00
1000.00
1500.00
2000.00
2500.00
4000.00
7500.00
15000.00
30000.00
50000.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
2.95250
3.40608
2.74879
1 .74341
1.07026
0.53763
0.40265
0.32212
0.20133
0.10737
0.05796
0.03248
0.02135
Volume
Appendix VII-4
External Review Draft
Do Not Cite or Quote
-------
ISCOHDEP VERSION 94227
UTI Truck Accident Off-Site, Screen Modeling — OFFSITE
1 Point source; 26 receptors up to 50 KM away; Vapor.
*** MODELING OPTIONS USED: CONC RURAL ELEV '
GRDRIS NOSTD
09/14/'
12:59:<
PAGE
*** CONCURRENT 1-HR AVERAGE CONCENTRATION VALUES ENDING WITH HOUR 6 FOR DAY 1
FOR SOURCE GROUP: ALL
INCLUDING SOURCE(S): OFFSITE ,
*** DISCRETE CARTESIAN RECEPTOR POINTS ***
** CONC OF FUGITIVE IN MICROGRAMS/M**3 **
X-COORO (M) Y-COORD (M)
CONC
X-COORD (M) Y-COORD (M)
CONC
100.00
300.00
500.00
700.00
900.00
1250.00
1750.00
2250.00
3000.00
5000.00
10000.00
20000.00
40000.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.73782
0.00000
0.00000
0.00000
0.00000
0.00000
0.00000
0.00000
0.00000
0.00000
0.00000
0.00000
0.00000
200.00
400.00
600.00
800.00
1000.00
1500.00
2000.00
2500.00
4000.00
7500.00
15000.00
30000.00
50000.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00000
0.00000
0.00000
0.00000
0.00000
0.00000
0.00000
0.00000
0.00000
0.00000
0.00000
0.00000
0.00000
Volume Vn
Appendix VII-4
External Review Draft
Do Not Cite or Quote
-------
ISCOMDEP VERSION 94227
UTI Truck Accident Off-Site, Screen Modeling •- OFFSITE
1 Point source; 26 receptors up to 50 KM away; Vapor.
*** MODELING OPTIONS USED: CONC RURAL ELEV
GRORIS NOSTD
09/14/95
12:
PAf
CONCURRENT 1-HR AVERAGE CONCENTRATION
FOR SOURCE GROUP: ALL
INCLUDING SOURCE(S): OFFSITE ,
VALUES ENDING WITH HOUR 7 FOR DAY 1
DISCRETE CARTESIAN RECEPTOR POINTS
** CONC OF FUGITIVE IN MICROGRAMS/M**3
X-COORD (M) Y-COORD (M>
CONC
X-COORD (M) Y-COORD (M)
CONC
100.00
300.00
500.00
700.00
900.00
1250.00
1750.00
2250.00
3000.00
5000.00
10000.00
20000.00
40000.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.88183
0.33234
0.21296
0.00000
0.00000
0.00000
0.00000
0.00000
0.00000
0.00000
0.00000
0.00000
0.00000
200.00
400.00
600.00
800.00
1000.00
1500.00
2000.00
2500.00
4000.00
7500.00
15000.00
30000.00
50000.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.42052
0.26377
0.00000
0.00000
0.00000
0.00000
0.00000
0.00000
0.00000
0.00000
0.00000
0.00000
0.00000
Volume VH
Appendix VTJ-4
External Review Draft
Do Not Cite or Quote
-------
*** ISCOMDEP VERSION 94227 *** ***
UTI Truck Accident Off-Site, Screen Modeling -- OFFSITE
1 Point source; 26 receptors up to SO KM away; Vapor.
*** MODELING OPTIONS USED: CONC RURAL ELEV ' '
GRDRIS NOSTD
09/U/9!
12:59:4)
PAGE 1!
CONCURRENT 1-HR AVERAGE CONCENTRATION
FOR SOURCE GROUP: ALL
INCLUDING SOURCE(S): OFFSITE ,
VALUES ENDING WITH HOUR 8 FOR DAY 1
DISCRETE CARTESIAN RECEPTOR POINTS
** CONC OF FUGITIVE IN MICROGRAMS/M**3
X-COORD (M) Y-COORD (M)
CONC
X-COORD (N) Y-COORD (M)
CONC
100.00
300.00
500.00
700.00
900.00
1250.00
1750.00
2250.00
3000.00
5000.00
10000.00
20000.00
40000.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
1.10912
0.55083
0.38747
0.23023
0.17402
0.00000
0.00000
0.00000
0.00000
0.00000
0.00000
0.00000
0.00000
200.00
400.00
600.00
800.00
1000.00
1500.00
2000.00
2500.00
4000.00
7500.00
15000.00
30000.00
50000.00
0.00
0.00 .
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.61332
0.46774
0.29377
0.20016
0.16905
0.00000
0.00000
0.00000
0.00000
0.00000
0.00000
0.00000
0.00000
Volume Vn
Appendix VII-4
External Review Draft
Do Not Cite or Quote
-------
ISCOMDEP VERSION 94227
¥71 Truck Accident Off-Site, Screen Modeling — OFFSITE
1 Point source; 26 receptors up to SO KM away; Vapor.
*** MODELING OPTIONS USED: CONC RURAL ELEV "
GRDRIS NOSTD
09/H/95
12;^-A«
P/
CONCURRENT 1-HR AVERAGE CONCENTRATION
FOR SOURCE GROUP: ALL
INCLUDING SOURCE(S): OFFSITE ,
VALUES ENDING WITH HOUR 9 FOR DAY . 1 •**
DISCRETE CARTESIAN RECEPTOR POINTS
** CONC OF FUGITIVE IN MICROGRAMS/M**3
X-COORD (M) Y-COORD (M)
CONC
X-COORD (M) Y-COORD (M)
CONC
100.00
300.00
500.00
700.00
900.00
1250.00
1750.00
2250.00
3000.00
5000.00
10000.00
20000.00
40000.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
1.44608
0.90330
0.68065
0.40882
0.31138
0.22177
0.31509
0.36427
0.35387
0.27006
0.15368
0.08501
0.04730
200.00
400.00
600.00
800.00
1000.00
1500.00
2000.00
2500.00
4000.00
7500.00
15000.00
30000.00
50000.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.91202
0.80214
0.51961
0.35741
0.30266
0.27135
0.34855
0.38863
0.30555
0.19640
0.10865
0.06027
0.03924
Volume VII
Appendix VII-4
External Review Draft
Do Not Cite or Quote
-------
ISCOMDEP VERSION 94227
UT1 Truck Accident Off-Site, Screen Modeling — OFFSITE
1 Point source; 26 receptors up to 50 KM way; Vapor.
09/U/
12:59:
PAGE
*** MODELING OPTIONS USED: COHC RURAL ELEV
GRDRIS NOSTD
CONCURRENT 1-HR AVERAGE CONCENTRATION VALUES ENDING WITH HOUR 10 FOR DAY
FOR SOURCE GROUP: ALL
INCLUDING SOURCE(S): OFFSITE ,
*** DISCRETE CARTESIAN RECEPTOR POINTS ***
** CONC OF FUGITIVE IN MICROGRAMS/M**3 **
X-COORD (M) y-COORD (M)
CONC
X-COORD (N) Y-COORD (M)
CONC
100.00
300.00
500.00
700.00
900.00
1250.00
1750.00
2250.00
3000.00
5000.00
10000.00
20000.00
40000.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
1.92557
1.42867
1.10621
0.65979
0.49681
0.34430
0.42503
0.42845
0.35660
0.20341
0.10695
0.05907
0.03285
200.00
400.00
600.00
800.00
1000.00
1500.00
2000.00
2500.00
4000.00
7500.00
15000.00
30000.00
50000.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
1.35182
1.29651
0.84213
0.57385
0.47862
0.39451
0.43721
0.42889
0.26007
0.13720
0.07553
0.04187
0.02726
Volume VII
Appendix VII-4
External Review Draft
Do Not Cite or Quote
-------
ISCOHDEP VERSION 94227
WTI Truck Accident Off-Site, Screen Modeling — OFFSITE
1 Point source; 26 receptors up to 50 KM amy; Vapor.
09/14/95
12./^--
PA
MODELING OPTIONS USED: CONC RURAL ELEV
GRDRIS NOSTD
*** CONCURRENT 1-HR AVERAGE CONCENTRATION VALUES ENDING WITH HOUR 11 FOR DAY
FOR SOURCE GROUP: ALL
INCLUDING SOURCE(S): OFFSITE ,
*** DISCRETE CARTESIAN RECEPTOR POINTS ***
** CONC OF FUGITIVE IN MICROGRAMS/M**3 **
X-COORD (M) Y-COORD (M)
CONC
X-COORD (N) Y-COORD (N)
CONC
100.00
300.00
500.00
700.00
900.00
1250.00
1750.00
2250.00
3000.00
5000.00
10000.00
20000.00
40000.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
2.58426
2.14864
1.65292
0.96723
0.71214
0.47503
0.50958
0.46113
0.34819
0.17370
0.07873
0.04342
0.02414
200.00
400.00
600.00
800.00
1000.00
1500.00
2000.00
2500.00
4000.00
7500.00
15000.00
30000.00
50000.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
1.96470
1.95449
1.24624
0.83159
0.67593
0.50657
0.49384
0.44104
0.24054
0.10298
0.05553
0.03076
0.02003
Volume VH
Appendix Vn-4
External Review Draft
Do Not Cite or Quote
-------
ISCOMDEP VERSION 94227
UTI Truck Accident Off-Site, Screen Nodeling -- OFFSITE
1 Point source; 26 receptors up to 50 KM away; Vapor.
09/K/'
12:59:
PAGE
*** MODELING OPTIONS USED: CONC RURAL ELEV
GRDRIS NOSTD
CONCURRENT 1-HR AVERAGE CONCENTRATION
FOR SOURCE GROUP: ALL
INCLUDING SOURCE(S): OFFSITE ,
VALUES ENDING WITH HOUR 12 FOR DAY . 1
DISCRETE CARTESIAN RECEPTOR POINTS
CONC OF FUGITIVE IN NICROGRAMS/H**3
X-COORD (M> Y-COORD (M)
CONC
X-COORD (N) Y-COORD (M)
CONC
100.00
300.00
500.00
700.00
900.00
1250.00
1750.00
2250.00
3000.00
5000.00
10000.00
20000.00
40000.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
3.45842
3.05698
2.28199
1.30217
0.93335
0.59801
0.56611
0.47128
0.33303
0.15583
0.06060
0.03325
0.01848
200.00
400.00
600.00
800.00
1000.00
1500.00
2000.00
2500.00
4000.00
7500.00
15000.00
30000.00
50000.00
0.00
o.oo.
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
2.77124
2.74778
1.69778
1.10362
0.87100
0.59625
0.52340
0.43575
0.22346
0.08284
0.04253
0.02356
0.01533
Volume Vn
Appendix VTJ-4
External Review Draft
Do Not Cite or Quote
-------
*** ISCOMDEP VERSION 94227 *** ***
UT! Truck Accident Off-Site, Screen Modeling — OFFSITE
1 Point source; 26 receptors up to 50 KM away; Vapor.
09/H/9!
12/-T"^
P/
*** MODELING OPTIONS USED: CONC RURAL ELEV
GRDRIS NOSTD
CONCURRENT 1-HR AVERAGE CONCENTRATION
FOR SOURCE GROUP: ALL
INCLUDING SOURCE(S): OFFSITE ,
VALUES ENDING WITH HOUR 13 FOR DAY 1
DISCRETE CARTESIAN RECEPTOR POINTS
CONC OF FUGITIVE IN MICROGRAMS/M**3
X-COORD OO Y-COORD (M)
CONC
X-COORD (N) Y-COORD (N)
CONC
100.00
300.00
500.00
700.00
900.00
1250.00
1750.00
2250.00
3000.00
5000.00
10000.00
20000.00
40000.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
4.57867
4.11814
2.94028
1.63354
1.13951
0.70301
0.59867
0.46740
0.31939
0.14195
0.04858
0.02628
0.01461
200.00
400.00
600.00
800.00
1000.00
1500.00
2000.00
2500.00
4000.00
7500.00
15000.00
30000.00
50000.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
3.77421
3.62343
2.15603
1.36412
1.04568
0.66094
0.53355
0.42131
0.20724
0.07053
0.03362
0.01861
0.01212
Volume Vn
Appendix VII-4
External Review Draft
Do Not Cite or Quote
-------
ISCONDEP VERSION 94227
UTI Truck Accident Off-Site, Screen Modeling - OFFSITE
1 Point source; 26 receptors up to 50 KM away; Vapor.
09/14/5
12:59:<
PAGE 2
*** MODELING OPTIONS USED: CONC RURAL ELEV
GRORIS NOSTD
CONCURRENT 1-HR AVERAGE CONCENTRATION
FOR SOURCE GROUP: ALL
INCLUDING SOURCE(S): OFFSITE ,
VALUES ENDING WITH HOUR 14 FOR DAY 1
DISCRETE CARTESIAN RECEPTOR POINTS
** CONC OF FUGITIVE IN N1CROGRAHS/M**3
X-COORD (M) Y-COORD (M)
CONC
X-COORD (M) Y-COORD (N)
CONC
100.00
300.00
500.00
700.00
900.00
1250.00
1750.00
2250.00
3000.00
5000.00
10000.00
20000.00
40000.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
5.96480
5.27547
3.57619
1.93669
1.31723
0.78588
0.61309
0.45548
0.30380
0.13020
0.04047
0.02129
0.01183
200.00
400.00
600.00
800.00
. 1000.00
1500.00
2000.00
2500.00
4000.00
7500.00
15000.00
30000.00
50000.00
0.00
0.00 .
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
4.95626
4.51893
2.58555
1.59475
1.19007
0.70301
0.53095
0.40264
0. 19232
0.06240
0.02724
0.01508
0.00981
Volume VH
Appendix VB-4
External Review Draft
Do Not Cite or Quote
-------
*** ISCOHDEP VERSION 94227
WTI Truck Accident Off-Site, Screen Modeling — OFFSITE
1 Point source; 26 receptors up to 50 KM away; Vapor.
09/14/9!
*** MODELING OPTIONS USED: CONC RURAL ELEV "
GRDRIS NOSTD
CONCURRENT 1-HR AVERAGE CONCENTRATION
FOR SOURCE GROUP: ALL
INCLUDING SOURCE(S): OFFSITE ,
VALUES ENDING WITH HOUR 15 FOR DAY 1 ***
DISCRETE CARTESIAN RECEPTOR POINTS ***
** CONC OF FUGITIVE IN MICROGRAMS/M**3
X-COORD (M) Y-COORD (M)
CONC
X-COORD (M) Y-COORD (N)
CONC
100.00
300.00
500.00
700.00
900.00
1250.00
1750.00
2250.00
3000.00
5000.00
10000.00
20000.00
40000.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.68894
0.00000
0.00000
0.00000
0.00000
0.00000
0.00000
0.00000
0.00000
0.00000
0.00000
0.00000
0.00000
200.00
400.00
600.00
800.00
1000.00
1500.00
2000.00
2500.00
4000.00
7500.00
15000.00
30000.00
50000.00
0.00
0.00.
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00000
0.00000
0.00000
0.00000
0.00000
0.00000
0.00000
0.00000
0.00000
0.00000
0.00000
0.00000
0.00000
Volume VII
Appendix VII-4
External Review Draft
Do Not Cite or Quote
-------
ISCOMDEP VERSION 94227
WTI Truck Accident Off-Site, Screen Model ing — OFFSITE
1 Point source; 26 receptors up to SO KM away; Vapor.
09/U/
12:59:
PAGE
MODELING OPTIONS USED: CONC RURAL ELEV
GRDRIS NOSTD
CONCURRENT 1-HR AVERAGE CONCENTRATION
FOR SOURCE GROUP: ALL
INCLUDING SOURCE(S): OFFSITE .
VALUES ENDING WITH HOUR 16 FOR DAY 1
DISCRETE CARTESIAN RECEPTOR POINTS
*» CONC OF FUGITIVE IN NICROGRAMS/M**3
X-COORD (M) Y-COORD (M)
CONC
X-COORD (M) Y-COORD (M)
CONC
100.00
300.00
500.00
700.00
900.00
1250.00
1750.00
2250.00
3000.00
5000.00
10000.00
20000.00
40000.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.76179
0.26741
0.15277
0.00000
0.00000
0.00000
0.00000
0.00000
0.00000
0.00000
0.00000
0.00000
0.00000
200.00
400.00
600.00
800.00
1000.00
1500.00
2000.00
2500.00
4000.00
7500.00
15000.00
30000.00
50000.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.34938
0.20527
0.00000
0.00000
0.00000
0.00000
0.00000
0.00000
0.00000
0.00000
0.00000
0.00000
0.00000
Volume VII
Appendix VH.-4
External Review Draft
Do Not Cite or Quote
-------
ISCCMDEP VERSION 94227
WTI Truck Accident Off-Site, Screen Modeling — OFFSITE
1 Point source; 26 receptors up to SO KM away; Vapor.
*** MODELING OPTIONS USED: CONC RURAL ELEV
GRDRIS NOSTD
CONCURRENT 1-HR AVERAGE CONCENTRATION
FOR SOURCE GROUP: ALL
INCLUDING SOURCE(S): OFFSITE ,
VALUES ENDING WITH HOUR 17 FOR DAY 1
DISCRETE CARTESIAN RECEPTOR POINTS
«* CONC OF FUGITIVE IN NICROGRANS/N**3
X-COORD (M) Y-COORD (M)
CONC
X-COORD (N) Y-COORD (M)
CONC
100.00
300.00
500.00
700.00
900.00
1250.00
1750.00
2250.00
3000.00
5000.00
10000.00
20000.00
40000.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.87063
0.39519
0.24606
0.11893
0.07669
0.04468
0.05217
0.07082
0.11294
0.24819
0.30443
0.17898
0.09797
200.00
400.00
600.00
800.00
1000.00
1500.00
2000.00
2500.00
4000.00
7500.00
15000.00
30000.00
50000.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.45629
0.32323
0.16816
0.09554
0.07120
0.04701
0.06086
0.09477
0.18240
0.32083
0.22927
0.12577
0.08075
Volume VII
Appendix VTJ-4
External Review Draft
Do Not Cite or Quote
-------
•** ISCOMDEP VERSION 94227 *** ***
UTI Truck Accident Off-Site, Screen Modeling — OFFSITE
1 Point source; 26 receptors up to 50 KM away; Vapor.
09/14
12:59
PAGE
MODELING OPTIONS USED: CONC RURAL ELEV
GRDRIS NOSTO
CONCURRENT 1-HR AVERAGE CONCENTRATION
FOR SOURCE GROUP: ALL
INCLUDING SOURCE(S): OFFSITE ,
VALUES ENDING WITH HOUR 18 FOR DAY. 1
DISCRETE CARTESIAN RECEPTOR POINTS
** CONC OF FUGITIVE IN NICROGRAMS/M**3
X-COORD (M) Y-COORD (M)
CONC
X-COORD (M) Y-COORD (M)
CONC
100.00
300.00
500.00
700.00
900.00
1250.00
1750.00
2250.00
3000.00
5000.00
10000.00
20000.00
40000.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
1.02308
0.58794
0.39393
0.18814
0.12210
0.07006
0.08705
0.11957
0.17840
0.23852
0.19646
0.11475
0.06274
200.00
400.00
600.00
800.00
1000.00
1500.00
2000.00
2500.00
4000.00
7500.00
15000.00
30000.00
50000.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.60938
0.50678
0.26789
0.15194
0.11529
0.07642
0.10303
0.16053
0.21262
0.22802
0.14648
0.08056
0.05171
Volume VII
Appendix VTJ-4
External Review Draft
Do Not Cite or Quote
-------
ISCOMDEP VERSION 94227
UTI Truck Accident Off-Site, Screen Modeling — OFFSITE
1 Point source; 26 receptors up to 50 KM away; Vapor.
09/14/9
12s"~~*
Pi'
*** MODELING OPTIONS USED: CONC RURAL ELEV
GRDRIS NOSTD
CONCURRENT 1-HR AVERAGE CONCENTRATION VALUES ENDING WITH HOUR 19 FOR DAY
FOR SOURCE GROUP: ALL
INCLUDING SOURCE(S): OFFSITE ,
*** DISCRETE CARTESIAN RECEPTOR POINTS ***
** CONC OF FUGITIVE IN MICROGRAMS/M**3 . **
X-COORD (M) Y-COORD (M)
CONC
X-COORD (N) Y-COORD (M)
CONC
100.00
300.00
500.00
700.00
900.00
1250.00
1750.00
2250.00
3000.00
5000.00
10000.00
20000.00
40000.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
1.22892
0.86845
0.61432
0.29106
0.18973
0.10954
0.14038
0.18745
0.25285
0.28522
0.16651
0.08018
0.04358
200.00
400.00
600.00
800.00
1000.00
1500.00
2000.00
2500.00
4000.00
7500.00
15000.00
30000.00
50000.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.82335
0.77877
0.41638
0.23590
0.18104
0.12236
0.16482
0.24269
0.28284
0.22481
0.10601
0.05599
0.03592
Volume VH
Appendix VII-4
External Review Draft
Do Not Cite or Quote
-------
ISCOMDEP VERSION 94227
UTI Truck Accident Off-Site, Screen Modeling -- OFFSITE
1 Point source; 26 receptors up to 50 KM away; Vapor.
*** MODELING OPTIONS USED: CONC RURAL ELEV ~~
09/U/
12:59:
PAGE
GRDRIS NOSTD
CONCURRENT 1-HR AVERAGE CONCENTRATION
FOR SOURCE GROUP: ALL
INCLUDING SOURCE(S): OFFSITE ,
VALUES ENDING WITH HOUR 20 FOR DAY 1
*** DISCRETE CARTESIAN RECEPTOR POINTS
** CONC OF FUGITIVE IN MICROGRAMS/M**3
X-COORD (M) Y-COORD (M)
CONC
X-COORD (N) Y-COORD (M)
CONC
100.00
300.00
500.00
700.00
900.00
1250.00
1750.00
2250.00
3000.00
5000.00
10000.00
20000.00
40000.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
1.49998
1.25983
0.92247
0.43443
0.28352
0.16389
0.20759
0.26172
0.31608
0.31119
0.15263
0.06066
0.03203
200.00
400.00
600.00
800.00
1000.00
1500.00
2000.00
2500.00
4000.00
7500.00
15000.00
30000.00
50000.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
1.11479
1.15989
0.62356
0.35259
0.27185
0.18340
0.23761
0.32364
0.33463
0.21949
0.08631
0.04118
0.02639
Volume VII
Appendix VII-4
External Review Draft
Do Not Cite or Quote
-------
ISCOMDEP VERSION 94227
VTI Truck Accident Off-Site, Screen Modeling •- OFFSITE
1 Point source; 26 receptors up to 50 KM away; Vapor.
*** MODELING OPTIONS USED: CONC RURAL ELEV "
D9/K/9!
12
ft
GRDRIS NOSTD
CONCURRENT 1-HR AVERAGE CONCENTRATION
FOR SOURCE GROUP: ALL
INCLUDING SOUftCE(S): OFFSITE ,
VALUES ENDING WITH HOUR 21 FOR DAY 1 ***
DISCRETE CARTESIAN RECEPTOR POINTS
** CONC OF FUGITIVE IN MICROGRAMS/M**3
X-COORD (M) Y-COORD (M)
CONC
X-COORD (M) Y-COORD (M)
CONC
100.00
300.00
500.00
700.00
900.00
1250.00
1750.00
2250.00
3000.00
5000.00
10000.00
20000.00
40000.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
1.84974
1.78126
1.32556
0.62105
0.40456
0.23305
0.28341
0.33334
0.37818
0.32169
0.14082
0.04941
0.02453
200.00
400.00
600.00
800.00
1000.00
1500.00
2000.00
2500.00
4000.00
7500.00
15000.00
30000.00
50000.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
1.50061
1.66318
0.89375
0.50371
0.38794
0.25704
0.31363
0.39338
0.36796
0.20971
0.07525
0.03167
0.02021
Volume VII
Appendix VII-4
External Review Draft
Do Not Cite or Quote
-------
1SCONDEP VERSION 94227
WTI Truck Accident Off-Site, Screen Modeling — OFFSITE
1 Point source; 26 receptors up to 50 KM away; Vapor.
09/H>
12:59:
PAGE
*** MODELING OPTIONS USED: CONC RURAL ELEV
GRDRIS NOSTD
CONCURRENT 1-HR AVERAGE CONCENTRATION
FOR SOURCE GROUP: ALL
INCLUDING SOURCE(S): OFFSITE ,
VALUES ENDING WITH HOUR 22 FOR DAY 1 ***
DISCRETE CARTESIAN RECEPTOR POINTS
** CONC OF FUGITIVE IN MICROGRAMS/M**3
X-COORD (M) Y-COORD (M)
CONC
X-COORD (M) Y-COORD (M)
CONC
100.00
300.00
500.00
700.00
900.00
1250.00
1750.00
2250.00
3000.00
5000.00
10000.00
20000.00
40000.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
2.29270
2.44350
1.81930
0.84845
0.55031
0.31487
0.36142
0.39771
0.42908
0.32217
0.12995
0.04254
0.01940
200.00
400.00
600.00
800.00
1000.00
1500.00
2000.00
2500.00
4000.00
7500.00
15000.00
30000.00
50000.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
1.99603
2.28925
1.22355
0.68656
0.52589
0.33865
0.38574
0.44738
0.38636
0.19825
0.06761
0.02537
0.01597
Volume Vn
Appendix VII-4
External Review Draft
Do Not Cite or Quote
-------
ISCOHDEP VERSION 94227 ***
UTI Truck Accident Off-Site, Screen Modeling -- OFFSITE
1 Point source; 26 receptors up to 50 KM away; Vapor.
09/14/95
12
P/
•** MODELING OPTIONS USED: CONC RURAL ELEV
GRDRIS NOSTD
CONCURRENT 1-HR AVERAGE CONCENTRATION VALUES ENDING WITH HOUR 23 FOR DAY
FOR SOURCE GROUP: ALL
INCLUDING SOURCE(S): OFFSITE ,
•** DISCRETE CARTESIAN RECEPTOR POINTS ***
** CONC OF FUGITIVE IN MICROGRAMS/M**3 **
X-COORD (M) Y-COORD
CONC
X-COORD (N) Y-COORD (M)
CONC
100.00
300.00
500.00
700.00
900.00
1250.00
1750.00
2250.00
3000.00
5000.00
10000.00
20000.00
40000.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
2.84345
3.24546
2.38751
1.10895
0.71502
0.40548
0.43587
0.46577
0.46562
0.31662
0.12017
0.03791
0.01576
200.00
400.00
600.00
800.00
1000.00
1500.00
2000.00
2500.00
4000.00
7500.00
15000.00
30000.00
50000.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
2.61234
3.02450
1.60183
0.89428
0.67926
0.42278
0.44908
0.48530
0.39383
0.18659
0.06156
0.02113
0.01294
Volume VII
Appendix VII-4
External Review Draft
Do Not Cite or Quote
-------
*** ISCOMDEP VERSION 94227 ***
UTI Truck Accident Off-Site, Screen Modeling - OFFSITE
1 Point source; 26 receptors up to 50 KM away; Vapor.
*** MODELING OPTIONS USED: CONC RURAL ELEV"" ~
09/U/1
12:59:.
PAGE i
GRORIS NOSTD
*«* CONCURRENT 1-HR AVERAGE CONCENTRATION VALUES ENDING WITH HOUR 24 FOR DAY
FOR SOURCE GROUP: ALL
INCLUDING SOURCE(S): OFFSITE ,
*** DISCRETE CARTESIAN RECEPTOR POINTS ***
** CONC OF FUGITIVE IN MICROGRAMS/M**} **
X-COORD (M) Y-COORD (M)
CONC
X-COORD (N) Y-COORD (N)
CONC
100.00
300.00
500.00
700.00
900.00
1250.00
1750.00
2250.00
3000.00
5000.00
10000.00
20000.00
40000.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
2.08867
5.49504
3.77290
2.59060
1.68105
0.90328
0.74650
0.65674
0.37322
0.15551
0.04336
0.01167
0.00321
200.00
400.00
600.00
800.00
1000.00
1500.00
2000.00
2500.00
4000.00
7500.00
15000.00
30000.00
50000.00
0.00
0.00 .
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
5.66463
4.60496
3.10751
2.13215
1.52042
0.78533
0.70761
0.49665
0.23038
0.07420
0.02016
0.00540
0.00229
Volume VH
Appendix VTJ-4
External Review Draft
Do Not Cite or Quote
-------
ISCONDEP VERSION 94227
UTI Truck Accident Off-Site, Screen Modeling — OFFSITE
1 Point source; 26 receptors ip to 50 KM away; Vapor.
*** MODELING OPTIONS USED: CONC RURAL ELEV
GRDRIS NOSTD
09/14/95
12'"^*
P/
CONCURRENT 1-HR AVERAGE CONCENTRATION
FOR SOURCE GROUP: ALL
INCLUDING SOURCE(S): OFFSITE ,
VALUES ENDING WITH HOUR 1 FOR DAY
DISCRETE CARTESIAN RECEPTOR POINTS
CONC OF FUGITIVE IN MICROGRAMS/M**3
X-COORD (M) Y-COORD (M)
CONC
X-COORD (M) Y-COORD (M)
CONC
100.00
300.00
500.00
700.00
900.00
1250.00
1750.00
2250.00
3000.00
5000.00
10000.00
20000.00
40000.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
1.59015
5.58536
3.79475
2.55791
1 .81858
1.05858
0.82346
0.50270
0.31392
0.12703
0.03490
0.00935
0.00250
200.00
400.00
600.00
800.00
1000.00
1500.00
2000.00
2500.00
4000.00
7500.00
15000.00
30000.00
50000.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
5.59481
4.67075
3.09618
2.14266
1.56203
0.90184
0.73736
0.42498
0.19008
0.05996
0.01618
0.00431
0.00167
Volume VII
Appendix VB-4
External Review Draft
Do Not Cite or Quote
-------
ISCONDEP VERSION 94227
VTI Truck Accident Off-Site, Screen Modeling — OFFSITE
1 Point source; 26 receptors up to 50 KM away; Vapor.
*** MODELING OPTIONS USED: CONC RURAL ELEV ~ '
09/14/
12:59:
PAGE
GRDRIS NOSTD
CONCURRENT 1-HR AVERAGE CONCENTRATION
FOR SOURCE GROUP: ALL
INCLUDING SOURCE(S): OFFSITE .
VALUES ENDING WITH HOUR 2 FOR DAY 2 ***
DISCRETE CARTESIAN RECEPTOR POINTS
** CONC OF FUGITIVE IN NICROGRAMS/N**3
X-COORD (H) Y-COORD (N)
CONC
X-COORD (M) Y-COORD (N)
CONC
100.00
300.00
500.00
700.00
900.00
1250.00
1750.00
2250.00
3000.00
5000.00
10000.00
20000.00
40000.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.65923
0.00000
0.00000
0.00000
0.00000
0.00000
0.00000
0.00000
0.00000
0.00000
0.00000
0.00000
0.00000
200.00
400.00
600.00
800.00
. 1000.00
1500.00
2000.00
2500.00
4000.00
7500.00
15000.00
30000.00
50000.00
0.00
0.00.
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00000
0.00000
0.00000
0.00000
0.00000
0.00000
0.00000
0.00000
0.00000
0.00000
0.00000
0.00000
0.00000
Volume VII
Appendix VTJ-4
External Review Draft
Do Not Cite or Quote
-------
ISCOMDEP VERSION 94227
UT! Truck Accident Off-Site, Screen Modeling -- OFFSITE
1 Point source; 26 receptors up to 50 KM away; Vapor.
*** MODELING OPTIONS USED: CONC RURAL ELEV " ~
09/14/95
12
P>
GRDRIS NOSTD
CONCURRENT 1-HR AVERAGE CONCENTRATION VALUES ENDING WITH HOUR 3 FOR DAY
FOR SOURCE GROUP: ALL
INCLUDING SOURCE(S): OFFSITE ,
*** DISCRETE CARTESIAN RECEPTOR POINTS *•*
** CONC OF FUGITIVE IN MICROGRAMS/M**3 **
X-COORD (M) Y-COORD (M)
CONC
X-COORD (M) Y-COORD (M)
CONC
100.00
300.00
500.00
700.00
900.00
1250.00
1750.00
2250.00
3000.00
5000.00
10000.00
20000.00
40000.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.69152
0.24032
0.13296
0.00000
0.00000
0.00000
0.00000
0.00000
0.00000
0.00000
0.00000
0.00000
0.00000
200.00
400.00
600.00
800.00
1000.00
1500.00
2000.00
2500.00
4000.00
7500.00
15000.00
30000.00
50000.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.31257
0.18268
0.00000
0.00000
0.00000
0.00000
0.00000
0.00000
0.00000
0.00000
0.00000
0.00000
0.00000
Volume VH
Appendix VH-4
External Review Draft
Do Not Cite or Quote
-------
ISCOMDEP VERSION 94227 ***
UTI Truck Accident Off-Site, Screen Modeling - OFFSITE
1 Point source; 26 receptors up to 50 KM away; Vapor.
MODELING OPTIONS USED: CONC RURAL ELfV '
GRDRIS NOSTD
09/14/
12:59:
PAGE
CONCURRENT 1-HR AVERAGE CONCENTRATION VALUES ENDING WITH HOUR 4 FOR DAT
FOR SOURCE GROUP: ALL
INCLUDING SOURCE(S): OFFSITE ,
*•* DISCRETE CARTESIAN RECEPTOR POINTS ***
** CONC OF FUGITIVE IN MICROGRAMS/M**3 **
X-COORD (M) Y-COORD (M)
CONC
X-COORD (M) Y-COORD (M)
CONC
100.00
300.00
500.00
700.00
900.00
1250.00
1750.00
2250.00
3000.00
5000.00
10000.00
20000.00
40000.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.73755
0.32853
0.19618
0.08585
0.05166
0.02599
0.02054
0.02044
0.02552
0.02434
0.03564
0.05732
0.07235
200.00
400.00
600.00
800.00
1000.00
1500.00
2000.00
2500.00
4000.00
7500.00
15000.00
30000.00
50000.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.37658
0.26505
0.12761
0.06672
0.04744
0.02245
0.02035
0.02721
0.02610
0.02849
0.04756
0.06956
0.07179
Volume Vn
Appendix VII-4
External Review Draft
Do Not Cite or Quote
-------
ISCOMDEP VERSION 94227
WTI Truck Accident Off-Site, Screen Modeling — OFFSITE
1 Point source; 26 receptors up to 50 KM away; Vapor.
*** MODELING OPTIONS USED: CONC RURAL ELEV
GRDRIS NOSTD
09/14/95
12,
ft
CONCURRENT 1-HR AVERAGE CONCENTRATION
FOR SOURCE GROUP: ALL
INCLUDING SOURCE(S): OFFSITE ,
VALUES ENDING WITH HOUR 5 FOR DAY 2
DISCRETE CARTESIAN RECEPTOR POINTS
CONC OF FUGITIVE IN MICROGRANS/M**3
X-COORD (M) Y-CCORD (M)
CONC
X-COORD (N) Y-COORD (N)
CONC
100.00
300.00
500.00
700.00
900.00
1250.00
1750.00
2250.00
3000.00
5000.00
10000.00
20000.00
40000.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.79885
0.45085
0.28827
0.12062
0.07162
0.03507
0.02900
0.03078
0.04230
0.04323
0.06051
0.07844
0.06906
200.00
400.00
600.00
800.00
1000.00
1500.00
2000.00
2500.00
4000.00
7500.00
15000.00
30000.00
50000.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.45966
0.38360
0.18363
0.09339
0.06699
0.03091
0.02971
0.04382
0.04546
0.04929
0.07323
0.07692
0.06145
Volume VII
Appendix VII-4
External Review Draft
Do Not Cite or Quote
-------
ISCOMDEP VERSION 94227
UTI Truck Accident Off-Site, Screen Modeling -• OFFSITE
1 Point source; 26 receptors up to 50 KM away; Vapor.
MODELING OPTIONS USED: CONC RURAL ELEV
GRDRIS NOSTD
09/14/
12:59:
PAGE
CONCURRENT 1-HR AVERAGE CONCENTRATION
FOR SOURCE GROUP: ALL
INCLUDING SOURCE(S): OFFSITE ,
VALUES ENDING WITH HOUR 6 FOR DAY
*** DISCRETE CARTESIAN RECEPTOR POINTS
** CONC OF FUGITIVE IN MICROGRAMS/N**3
X-COORD (M) Y-COORD (M)
CONC
X-COORD (N) Y-COORD (N)
CONC
100.00
300.00
500.00
700.00
900.00
1250.00
1750.00
2250.00
3000.00
5000.00
10000.00
20000.00
40000.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.87742
0.61811
0.41929
0.16910
0.09937
0.04760
0.04111
0.04600
0.06743
0.07031
0.09418
0.10357
0.07610
200.00
400.00
600.00
800.00
1000.00
1500.00
2000.00
2500.00
4000.00
7500.00
15000.00
30000.00
50000.00
0.00
o.oo .
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.56660
0.55069
0.26259
. 0.13057
0.09441
0.04282
0.04332
0.06864
0.07401
0.07954
0.10449
0.09075
0.06436
Volume VH
Appendix VII-4
External Review Draft
Do Not Cite or Quote
-------
ISCOMDEP VERSION 94227
UTI Truck Accident Off-Site, Screen Modeling -• OFFSITE
1 Point source; 26 receptors up to 50 KM away; Vapor.
MODELING OPTIONS USED: CONC RURAL ELEV
GRDRIS NOSTO
09/K/95
12:5° -**
PAf
CONCURRENT 1-HR AVERAGE CONCENTRATION VALUES ENDING WITH HOUR 7 FOR DAY
FOR SOURCE GROUP: ALL
INCLUDING SOURCE(S): OFFSITE ,
*** DISCRETE CARTESIAN RECEPTOR POINTS ***
** CONC OF FUGITIVE IN NICROGRAMS/M**3 •*
X-COORD CM) Y-COORD (N).
CONC
X-COORD (M) Y-COORD (N)
CONC
100.00
300.00
500.00
700.00
900.00
1250.00
1750.00
2250.00
3000.00
5000.00
10000.00
20000.00
40000.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.97568
0.84288
0.60055
0.23522
0.13708
0.06452
0.05782
0.06726
0.10203
0.10425
0.13022
0.12217
0.07838
200.00
400.00
600.00
800.00
1000.00
1500.00
2000.00
2500.00
4000.00
7500.00
15000.00
30000.00
50000.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.70307
0.78041
0.37108
0.18123
0.13194
0.05909
0.06227
0.10328
0.11155
0.11595
0.13193
0.09804
0.06421
Volume VII
Appendix VIW
External Review Draft
Do Not Cite or Quote
-------
ISCOMDEP VERSION 94227
UTI Truck Accident Off-Site, Screen Hotel ins •• OFFSITE
1 Point source; 26 receptors up to SO KM away; Vapor.
*** MODELING OPTIONS USED: CONC RURAL ELEV '
GRDRIS NOSTD
09/14/'
12:59:<
PAGE :
CONCURRENT 1-HR AVERAGE CONCENTRATION
FOR SOURCE GROUP: ALL
INCLUDING SOURCE(S): OFFSITE ,
VALUES ENDING WITH HOUR 8 FOR DAY
*** DISCRETE CARTESIAN RECEPTOR POINTS
** CONC OF FUGITIVE IN MICROGRANS/M**3
X-COORD (M) Y-COORD (N)
CONC
X-COORD (N) Y-COORD (N)
CONC
100.00
300.00
500.00
700.00
900.00
1250.00
1750.00
2250.00
3000.00
5000.00
10000.00
20000.00
40000.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
1.09653
1.13892
0.84357
0.32307
0.18708
0.08681
0.08009
0.09544
0.14590
0.14210
0.16442
0.13420
0.07772
200.00
400.00
600.00
800.00
. 1000.00
1500.00
2000.00
2500.00
4000.00
7500.00
15000.00
30000.00
50000.00
O.QO
0.00.
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.87549
1.08743
0.51595
0.24852
0.18188
0.08069
0.08751
0.14837
0.15600
0.15503
0.15328
0.10067
0.06226
Volume VII
Appendix VTJ-4
External Review Draft
Do Not Cite or Quote
-------
ISCOMDEP VERSION 94227
UTI Truck Accident Off-Site, Screen Model ing -• OFFSITE
1 Point source; 26 receptors up to 50 KM away; Vapor.
*** MODELING OPTIONS USED: CONC RURAL ECEV " '~
GRORIS NOSTO
09/14/95
12:
P/l
CONCURRENT 1-HR AVERAGE CONCENTRATION
FOR SOURCE GROUP: ALL
INCLUDING SOURCE(S): OFFSITE ,
VALUES ENDING WITH HOUR 9 FOR DAY
DISCRETE CARTESIAN RECEPTOR POINTS
CONC OF FUGITIVE IN MICROGRAMS/M**3
X-COORD (M) Y-COORD (M)
CONC
X-COORD (N) Y-COORD (M)
CONC
100.00
300.00
500.00
700.00
900.00
1250.00
1750.00
2250.00
3000.00
5000.00
10000.00
20000.00
40000.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
1.25098
1.52013
1.15857
0.43650
0.25154
0.11549
0.10864
0. 13086
0.19736
0.18034
0.19409
0.14088
0.07549
200.00
400.00
600.00
800.00
1000.00
1500.00
2000.00
2500.00
4000.00
7500.00
15000.00
30000.00
50000.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
1.09092
1.48541
0.70343
0.33535
0.24636
0.10849
0.11962
0.20319
0.20398
0.19337
0.16836
0.10034
0.05948
Volume VH
Appendix VII-4
External Review Draft
Do Not Cite or Quote
-------
ISCOMDEP VERSION 94227
WTI Truck Accident Off-Site, Screen Modeling •• OFFSITE
1 Point source; 26 receptors up to 50 KM away; Vapor.
09/14;
12:59:
PAGE
MODELING OPTIONS USED: CONC RURAL ELEV
GRORIS NOSTD
CONCURRENT 1-HR AVERAGE CONCENTRATION
FOR SOURCE GROUP: ALL
INCLUDING SOURCE(S): OFFSITE ,
VALUES ENDING WITH HOUR 10 FOR DAY 2 ***
*** DISCRETE CARTESIAN RECEPTOR POINTS
CONC OF FUGITIVE IN MICROGRANS/M**3
X-COORD (N) Y-COORD (M)
CONC
X-COORD (M) Y-COORD (N)
CONC
100.00
300.00
500.00
700.00
900.00
1250.00
1750.00
2250.00
3000.00
5000.00
10000.00
20000.00
40000.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
1.53251
1.99924
1.55276
0.57864
0.33223
0.15138
0.14388
0.17309
0.25361
0.21590
0.21807
0.14363
0.07250
200.00
400.00
600.00
800.00
1000.00
1500.00
2000.00
2500.00
4000.00
7500.00
15000.00
30000.00
50000.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
1.35679
1.98495
0.93823
0.44408
0.32693
0.14310
0.15864
0.26570
0.25176
0.22843
0.17798
0.09826
0.05643
Volume
Appendix VII-4
External Review Draft
Do Not Cite or Quote
-------
1SCOMDEP VERSION 94227
WTI Truck Accident Off-Site, Screen Modeling - OFFSITE
1 Point source; 26 receptors up to 50 KM away; Vapor.
09/14/9!
1?,"-""•>.«
Pi
*•* MODELING OPTIONS USED: CONC RURAL ELEV
GRDRIS NOSTD
CONCURRENT 1-HR AVERAGE CONCENTRATION
FOR SOURCE GROUP: ALL
INCLUDING SOURCE(S): OFFSITE ,
VALUES ENDING WITH HOUR 11 FOR DAY 2
DISCRETE CARTESIAN RECEPTOR POINTS
•* CONC OF FUGITIVE IN MICROGRAMS/M**3
X-COORD (M) Y-COORD (M)
CONC
X-COORD (M) Y-COORD (M)
CONC
100.00
300.00
500.00
700.00
900.00
1250.00
1750.00
2250.00
3000.00
5000.00
10000.00
20000.00
40000.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.27107
2.28344
2.00967
1.57371
1.14996
0.52386
0.46164
0.48491
0.47196
0.28626
0.12210
0.04661
0.01694
200.00
400.00
600.00
800.00
1000.00
1500.00
2000.00
2500.00
4000.00
7500.00
15000.00
30000.00
50000.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
1.71777
2.21965
1.78189
1.39321
1.10872
0.48024
0.47766
0.54602
0.36155
0.17751
0.07023
0.02571
0.01222
Volume VH
Appendix VII-4
External Review Draft
Do Not Cite or Quote
-------
ISCOMDEP VERSION 94227
UTI Truck Accident Off-Site, Screen Modeling -- OFFSITE
1 Point source; 26 receptors up to 50 KM away; Vapor.
09/H/
12:59:
PAGE
MODELING OPTIONS USED: CONC RURAL ELEV
GRDRIS NOSTD
CONCURRENT 1-HR AVERAGE CONCENTRATION
FOR SOURCE GROUP: ALL
INCLUDING SOURCE(S): OFFSITE .
VALUES ENDING WITH HOUR 12 FOR DAY.
*** DISCRETE CARTESIAN RECEPTOR POINTS
CONC OF FUGITIVE IN MICROGRANS/M**3
X-COORD (M) Y-COORD (M>
CONC
X-COORD (N) Y-COORD (M)
CONC
100.00
300.00
500.00
700.00
900.00
1250.00
1750.00
2250.00
3000.00
5000.00
10000.00
20000.00
40000.00
0.00
0.00
0.00
0.00
0.00
0.00 .
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.10018
2.06962
2.00171
1.61295
1.28449
0.85233
0.68052
0.59155
0.45701
0.26054
0.10432
0.03851
0.01376
200.00
400.00
600.00
800.00
1000.00
1500.00
2000.00
2500.00
4000.00
7500.00
15000.00
30000.00
50000.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
1.30773
2.14212
1.80676
1.43766
1.15230
0.74482
0.64832
0.54123
0.33781
0.15511
0.05869
0.02100
0.00990
Volume Vn
Appendix VI1-4
External Review Draft
Do Not Cite or Quote
-------
ISCOHDEP VERSION 94227
VTI Truck Accident Off-Site, Screen Modeling -- OFFSITE
1 Point source; 26 receptors up to 50 KM way; Vapor.
09/U/95
12.-""~"^
PA
*** MODELING OPTIONS USED: CONC RURAL ELEV
GRDRIS NOSTD
CONCURRENT 1-HR AVERAGE CONCENTRATION
FOR SOURCE GROUP: ALL
INCLUDING SOURCE(S): OFFSITE ,
VALUES ENDING WITH HOUR 13 FOR DAY 2 ***
DISCRETE CARTESIAN RECEPTOR POINTS
CONC OF FUGITIVE IN NICROGRAMS/M**3
X-COORD (M) Y-COORD (M)
CONC
X-COORD (M) Y-COORD (M)
CONC
100.00
300.00
500.00
700.00
900.00
1250.00
1750.00
2250.00
3000.00
5000.00
10000.00
20000.00
40000.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.02068
1.91570
2.04348
1.67058
1.32693
0.89734
0.68782
0.53873
0.38948
0.20237
0.07482
0.02658
0.00933
200.00
400.00
600.00
800.00
1000.00
1500.00
2000.00
2500.00
4000.00
7500.00
15000.00
30000.00
50000.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.94900
2.12697
1.86491
1.48853
1.18646
0.78286
0.60707
0.48084
0.27228
0.11431
0.04103
0.01431
0.00669
Volume VH
Appendix VH-4
External Review Draft
Do Not Cite or Quote
-------
ISCOMDEP VERSION 94227
*** MODELING OPTIONS USED: CONC
UTI Truck Accident Off-Site. Screen Modeling -- OFFSITE
1 Point source; 26 receptors up to 50 KM way; Vapor.
09/14/
12:59:
PAGE
RURAL ELE"V ~~
GRDRIS NOSTD
CONCURRENT 1-HR AVERAGE CONCENTRATION
FOR SOURCE GROUP: ALL
INCLUDING SOURCE(S): OFFSITE .
VALUES ENDING WITH HOUR U FOR DAY 2
*** DISCRETE CARTESIAN RECEPTOR POINTS
** CONC OF FUGITIVE IN NICROGRAHS/M**3
X-COORD (M) Y-COORD (N)
CONC
X-COORD (N) Y-COORD (N)
CONC
100.00
300.00
500.00
700.00
900.00
1250.00
1750.00
2250.00
3000.00
5000.00
10000.00
20000.00
40000.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00974
1.88919
2.03106
1.63626
1.28060
0.85626
0.62138
0.46826
0.32603
0.16184
0.05779
0.02021
0.00704
200.00
400.00
600.00
800.00
. 1000.00
1500.00
2000.00
2500.00
4000.00
7500.00
15000.00
30000.00
50000.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.86040
2.12054
1.84082
1.44688
1.13748
0.72546
0.53698
0.41185
0.22158
0.08930
0.03136
0.01083
0.00504
Volume VH
Appendix VII-4
External Review Draft
Do Not Cite or Quote
-------
ISCOMDEP VERSION 94227
UT1 Truck Accident Off-Site, Screen Modeling •- OFFSITE
1 Point source; 26 receptors up to 50 KM away; Vapor.
09/14/95
12
PA
*** MODELIMG OPTIONS USED: CONC RURAL ELEV" "
GRDRIS NOSTD
CONCURRENT 1-HR AVERAGE CONCENTRATION VALUES ENDING WITH HOUR 15 FOR DAY . 2
FOR SOURCE GROUP: ALL
INCLUDING SOURCE(S): OFFSITE ,
*•* DISCRETE CARTESIAN RECEPTOR POINTS ***
** CONC OF FUGITIVE IN MICROGRAMS/M**3 •*
X-COORD (M) Y-COORD (M)
CONC
X-COORD (N) Y-COORD (M)
CONC
100.00
300.00
500.00
700.00
900.00
1250.00
1750.00
2250.00
3000.00
5000.00
10000.00
20000.00
40000.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
9.17914
9.78828
17.16070
11.51297
9.90330
7.64272
5.41060
5.34495
5.82222
3.22312
1.33870
0.70805
0.46332
200.00
400.00
600.00
800.00
1000.00
1500.00
2000.00
2500.00
4000.00
7500.00
15000.00
30000.00
50000.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
5.20311
14.86587
14.43324
11.03429
11.80137
6.21791
5.39378
7.21376
4.32489
1.87735
0.77559
0.56321
0.38992
Volume VII
Appendix VII-4
External Review Draft
Do Not Cite or Quote
-------
ISCOMDEP VERSION 94227
UTI Truck Accident Off-Site, Screen Modeling -- OFFSITE
1 Point source; 26 receptors up to 50 KM away; Vapor.
09/14/
12:59:
PAGE
MODELING OPTIONS USED: CONC RURAL ELEV
GRDRIS NOSTO
CONCURRENT 1-HR AVERAGE CONCENTRATION
FOR SOURCE GROUP: ALL
INCLUDING SOURCE(S): OFFSITE ,
VALUES ENDING WITH HOUR 16 FOR DAY
DISCRETE CARTESIAN RECEPTOR POINTS
** CONC OF FUGITIVE IN MICROGRAMS/M**3
X-COORD (M) Y-COORD (M)
CONC
X-COORD (M) Y-COORD (M)
CONC
100.00
300.00
500.00
700.00
900.00
1250.00
1750.00
2250.00
3000.00
5000.00
10000.00
20000.00
40000.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
26.37437
11.20241
18.94490
12.65435
10.64366
7.97805
5.50312
5.06163
4.50767
2.32745
0.89431
0.35126
0.13974
200.00
400.00
600.00
800.00
1000.00
1500.00
2000.00
2500.00
4000.00
7500.00
15000.00
30000.00
50000.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
5.63871
16.90074
15.83704
11.94546
12.06563
6.42436
5.29277
5.65509
3.05915
1.36933
0.52351
0.20522
0.10528
Volume Vn
Appendix VTJ-4
External Review Draft
Do Not Cite or Quote
-------
ISCONOEP VERSION 94227
UTI Truck Accident Off-Site, Screen Modeling — OFFSITE
1 Point source; 26 receptors up to 50 KM away; Vapor.
09/U/95
12s
PAi
*** MODELING OPTIONS USED: CONC RURAL ELEV
GRDRIS NOSTD
CONCURRENT 1-HR AVERAGE CONCENTRATION
FOR SOURCE GROUP: ALL
INCLUDING SOURCE(S): OFFSITE ,
VALUES ENDING WITH HOUR 17 FOR DAY
DISCRETE CARTESIAN RECEPTOR POINTS
CONC OF FUGITIVE IN MICROGRAMS/M**3
X-COORD (M) Y-COORD (M)
CONC
X-COORD (N) Y-COORD (M)
CONC
100.00
300.00
500.00
700.00
900.00
1250.00
1750.00
2250.00
3000.00
5000.00
10000.00
20000.00
40000.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
62.23378
12.35422
19.64951
13.09169
10.76628
7.85987
5.31279
4.59804
3.45930
1.74236
0.65978
0.25701
0.10176
200.00
400.00
600.00
800.00
1000.00
1500.00
2000.00
2500.00
4000.00
7500.00
15000.00
30000.00
50000.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
11.46214
18.18891
16.33002
12.16302
11.60286
6.28158
4.95312
4.36019
2.30037
1.02928
0.38430
0.14970
0.07659
Volume VH
Appendix VII-4
External Review Draft
Do Not Cite or Quote
-------
ISCOMDEP VERSION 94227
UTI Truck Accident Off-Site, Screen Modeling -- OFFSITE
1 Point source; 26 receptors up to 50 KM away; Vapor.
09/14/<
12:59:<
PAGE i
MODELING OPTIONS USED: CONC RURAL ELEV
GRDRIS NOSTD
*** CONCURRENT 1-HR AVERAGE CONCENTRATION
FOR SOURCE GROUP: ALL
INCLUDING SOURCE(S): OFFSITE ,
VALUES ENDING WITH HOUR 18 FOR DAY
*** DISCRETE CARTESIAN RECEPTOR POINTS
CONC OF FUGITIVE IN MICROGRANS/N**3
X-COORD (M) Y-COORD (N)
CONC
X-COORD (N) Y-COORD (M)
CONC
100.00
300.00
500.00
700.00
900.00
1250.00
1750.00
2250.00
3000.00
5000.00
10000.00
20000.00
40000.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
120.40126
15.66378
19.64915
13.08050
10.53259
7.51630
5.00416
4.11389
2.78693
1.38996
0.52080
0.20173
0.07961
200.00
400.00
600.00
800.00
1000.00
1500.00
2000.00
2500.00
4000.00
7500.00
15000.00
30000.00
50000.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
22.42717
18.92721
16.24436
11.96645
10.81345
5.97614
4.54292
3.52548
1.84120
0.81654
0.30231
0.11726
0.05989
Volume VH
Appendix VII-4
External Review Draft
Do Not Cite or Quote
-------
ISCOMDEP VERSION 94227
UTI Truck Accident Off-Site, Screen Modeling -- OFFSITE
1 Point source; 26 receptors up to 50 KM away; Vapor.
09/14/95
12,-'"7^
fl
*** MODELING OPTIONS USED: CONC RURAL ELEV
GRDRIS NOSTD
CONCURRENT 1-HR AVERAGE CONCENTRATION
FOR SOURCE GROUP: ALL
INCLUDING SOURCE(S): OFFSITE ,
VALUES ENDING WITH HOUR 19 FOR DAY
*** DISCRETE CARTESIAN RECEPTOR POINTS
** CONC OF FUGITIVE IN MICROGRAMS/M**3
X-COORD (M) Y-COORD (M)
CONC
X-COORD (M) Y-COORD (M)
CONC
100.00
300.00
500.00
700.00
900.00
1250.00
1750.00
2250.00
3000.00
5000.00
10000.00
20000.00
40000.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
191.37901
25.63425
19.19101
12.78461
10.09808
7.06886
4.65516
3.64354
2.33326
1.15467
0.42914
0.16553
0.06517
200.00
400.00
600.00
800.00
1000.00
1500.00
2000.00
2500.00
4000.00
7500.00
15000.00
30000.00
50000.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
38.04164
19.25438
15.79421
11.52680
9.82507
5.60258
4.13088
2.96026
1.53348
0.67544
0.24847
0.09607
0.04900
Volume VII
Appendix VII-4
External Review Draft
Do Not Cite or Quote
-------
ISCOMDEP VERSION 94227
vri Truck Accident Off-Site, Screen Modeling — OFFSITE
1 Point source; 26 receptors t? to 50 KM away; Vapor.
MODELING OPTIONS USED: CONC RURAL ELEV ~~
09/H/
12:59:
PAGE
GRDRIS NOSTD
CONCURRENT 1-HR AVERAGE CONCENTRATION VALUES ENDING UITH HOUR 20 FOR DAY
FOR SOURCE GROUP: ALL
INCLUDING SOURCE(S): OFFSITE ,
*** DISCRETE CARTESIAN RECEPTOR POINTS •**
** CONC OF FUGITIVE IN MICROGRAMS/M**3 **
X-COORD (M) Y-COORD (M)
CONC
X-COORD (N) Y-COORD (M)
CONC
100.00
300.00
500.00
700.00
900.00
1250.00
1750.00
2250.00
3000.00
5000.00
10000.00
20000.00
40000.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
207.63899
35.42534
18.44327
12.31243
9.55779
6.58382
4.30342
3.19940
2.00631
0.98657
0.36430
0.14006
0.05505
200.00
400.00
600.00
800.00
. 1000.00
1500.00
2000.00
2500.00
4000.00
7500.00
15000.00
30000.00
50000.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
56.09013
23.48624
15.12176
10.95165
8.72180
5.20999
3.71879
2.55168
1.31298
0.57515
0.21052
0.08120
0.04137
Volume Vn
Appendix VTJ-4
External Review Draft
Do Not Cite or Quote
-------
ISCOMDEP VERSION 94227
UTI Truck Accident Off-Site, Screen Modeling — OFFSITE
1 Point source; 26 receptors up to SO KM away; Vapor.
09/U/95
12:f" •-**,
PA
*** HOOELING OPTIONS USED: CONC RURAL ELEV" ~ ~
GRORIS NOSTD
CONCURRENT 1-HR AVERAGE CONCENTRATION
FOR SOURCE GROUP: ALL
INCLUDING SOURCE(S): OFFSITE ,
VALUES ENDING WITH HOUR 21 FOR DAY 2 ***
DISCRETE CARTESIAN RECEPTOR POINTS
** CONC OF FUGITIVE IN MICROGRAMS/M**3
X-COORD (H) Y-COORD (M)
CONC
X-COORD (N) Y-COORD (N)
CONC
100.00
300.00
500.00
700.00
900.00
1250.00
1750.00
2250.00
3000.00
5000.00
10000.00
20000.00
40000.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
189.36391
39.82120
17.61203
11.73672
8.92155
6.01535
3.95109
2.83397
1.75942
0.86056
0.31608
0.12121
0.04757
200.00
400.00
600.00
800.00
1000.00
1500.00
2000.00
2500.00
4000.00
7500.00
15000.00
30000.00
50000.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
72.27760
25.24093
14.23355
10.25074
7.79965
4.80297
3.32376
2.24233
1.14726
0.50029
0.18237
0.07020
0.03574
Volume VH
Appendix VII-4
External Review Draft
Do Not Cite or Quote
-------
ISCOMDEP VERSION 94227
VTI Truck Accident Off-Site, Screen Modeling — OFFSITE
1 Point source; 26 receptors up to 50 KM away; Vapor.
MODELING OPTIONS USED: CONC RURAL ELEV " ~
09/H/9
12:59:4
PAGE 5
GRDRIS NOSTD
CONCURRENT 1-HR AVERAGE CONCENTRATION
FOR SOURCE GROUP: ALL
INCLUDING SOURCE(S): OFFSITE ,
VALUES ENDING WITH HOUR 22 FOR DAY
DISCRETE CARTESIAN RECEPTOR POINTS
CONC OF FUGITIVE IN MICROGRAMS/M**3
X-COORD (M) Y-COORD (M)
CONC
X-COORD (M) Y-COORD (N)
CONC
100.00
300.00
500.00
700.00
900.00
1250.00
1750.00
2250.00
3000.00
5000.00
10000.00
20000.00
40000.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
169.67842
38.22855
16.92746
10.93935
8.14166
5.47144
3.58087
2.53310
1.56636
0.76265
0.27886
0.10671
0.04183
200.00
400.00
600.00
800.00
1000.00
1500.00
2000.00
2500.00
4000.00
7500.00
15000.00
30000.00
50000.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
70.66110
24.09174
13.03526
9.36549
7.03090
4.36030
2.99774
1.99987
1.01821
0.44233
0.16069
0.06176
0.03142
Volume VII
Appendix VTJ-4
External Review Draft
Do Not Cite or Quote
-------
ISCOMDEP VERSION 94227
UTI Truck Accident Off-Site, Screen Modeling -- OFFSITE
1 Point source; 26 receptors up to 50 KM away; Vapor.
09/14/95
12:^—^
PAI
*** MODELING OPTIONS USED: CONC RURAL ELEV
GRDRIS NOSTD
*** CONCURRENT 1-HR AVERAGE CONCENTRATION VALUES ENDING WITH HOUR 23 FOR DAY
FOR SOURCE GROUP: ALL
INCLUDING SOURCE(S): OFFSITE ,
**» DISCRETE CARTESIAN RECEPTOR POINTS ***
** CONC OF FUGITIVE IN MICROGRAMS/M**3 **
X-COORD (M) Y-COORD (N)
CONC
X-COORD (N) Y-COORD (N)
CONC
100.00
300.00
500.00
700.00
900.00
1250.00
1750.00
2250.00
3000.00
5000.00
10000.00
20000.00
40000.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
151.22041
36.17004
16.03088
10.09557
7.49753
5.01292
3.27706
2.29028
1.41124
0.68441
0.24930
0.09523
0.03729
200.00
400.00
600.00
800.00
1000.00
1500.00
2000.00
2500.00
4000.00
7500.00
15000.00
30000.00
50000.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
66.92157
22.82990
12.31160
8.63371
6.40542
3.99640
2.71366
1.80466
0.91491
0.39617
0.14350
0.05508
0.02801
Volume VH
Appendix VTJ-4
External Review Draft
Do Not Cite or Quote
-------
ISCOMDEP VERSION 94227
UTI Truck Accident Off-Site, Screen Modeling -- OFFSITE
1 Point source; 26 receptors up to 50 KM away; Vapor.
09/14/9
12:59:4
PAGE 5
*** MODELING OPTIONS USED: CONC RURAL ELEV
GRDRIS NOSTD
CONCURRENT 1-HR AVERAGE CONCENTRATION
FOR SOURCE GROUP: ALL
INCLUDING SOURCE(S): OFFSITE ,
VALUES ENDING WITH HOUR 24 FOR DAY
*** DISCRETE CARTESIAN RECEPTOR POINTS
•* CONC OF FUGITIVE IN MICROGRAMS/M**3
X-COORD (M) Y-COORD (N)
CONC
X-COORD (N) Y-COORD (M)
CONC
100.00
300.00
500.00
700.00
900.00
1250.00
1750.00
2250.00
3000.00
5000.00
10000.00
20000.00
40000.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
17.67307
22.11532
34.85668
23.24654
19.16001
14.09468
9.60246
8.58492
6.38994
3.45708
1.44461
0.62392
0.26734
200.00
400.00
600.00
800.00
. 1000.00
1500.00
2000.00
2500.00
4000.00
7500.00
15000.00
30000.00
50000.00
0.00
0.00 .
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
10.71785
32.51575
28.97512
. 21.61471
20.69304
11.29400
9.10952
7.88782
4.43724
2.15608
0.88569
0.37837
0.20389
Volume Vn
Appendix VD-4
External Review Draft
Do Not Cite or Quote
-------
ISCOMDEP VERSION 94227
UTI Truck Accident Off-Site, Screen Modeling » OFFSITE
1 Point source; 26 receptors up to 50 KM away; Vapor.
09/U/95
12 ?>*—*«
ft
*** MODELING OPTIONS USED: CONC RURAL ELEV
GRDRIS NOSTD
CONCURRENT 1-HR AVERAGE CONCENTRATION
FOR SOURCE GROUP: ALL
INCLUDING SOURCE(S): OFFSITE ,
VALUES ENDING WITH HOUR 1 FOR DAY
DISCRETE CARTESIAN RECEPTOR POINTS ***
** CONC OF FUGITIVE IN MICROGRAMS/M**3
X-COORD (M) Y-COORD (M)
CONC
X-COORD (M) Y-COORD (M)
CONC
100.00
300.00
500.00
700.00
900.00
1250.00
1750.00
2250.00
3000.00
5000.00
10000.00
20000.00
40000.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
57.56957
25.15523
33.45829
22.60911
18.02194
12.86062
8.68409
6.77120
4.42163
2.35676
0.96494
0.41102
0.17439
200.00
400.00
600.00
800.00
1000.00
1500.00
2000.00
2500.00
4000.00
7500.00
15000.00
30000.00
50000.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
12.13928
34.11783
27.67290
20.43232
16.87412
10.32840
7.75508
5.48719
3.04205
1.45425
0.58639
0.24767
0.13268
Volume VII
Appendix VH-4
External Review Draft
Do Not Cite or Quote
-------
ISCOMDEP VERSION 94227
UTI Truck Accident Off-Site, Screen Modeling — OFFSITE
1 Point source; 26 receptors up to 50 KM away; Vapor.
*** MODELING OPTIONS USED: CONC RURAL ELEV "
09/H/
12:59:
PAGE
GRDRIS NOSTD
CONCURRENT 1-HR AVERAGE CONCENTRATION
FOR SOURCE GROUP: ALL
INCLUDING SOURCE(S): OFFSITE ,
VALUES ENDING WITH HOUR 2 FOR DAY 3
*** DISCRETE CARTESIAN RECEPTOR POINTS
** CONC OF FUGITIVE IN MICROGRAMS/M**3
X-COORD (M) Y-COORD (M)
CONC
X-COORD (M) Y-COORD (M)
CONC
100.00
300.00
500.00
700.00
900.00
1250.00
1750.00
2250.00
3000.00
5000.00
10000.00
20000.00
40000.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
135.07504
27.03052
28.70184
20.08150
15.31101
10.65054
7.24759
5.28539
3.39516
1.79032
0.72288
0.30517
0.12870
200.00
400.00
600.00
800.00
. 1000.00
1500.00
2000.00
2500.00
4000.00
7500.00
15000.00
30000.00
50000.00
0.00
0.00 .
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
24.98931
33.35661
23.68114
17.39954
13.36535
8.66254
6.16188
4.23010
2.32025
1.09660
0.43677
0.18315
0.09777
Volume VH
Appendix Vn-4
External Review Draft
Do Not Cite or Quote
-------
ISCOMDEP VERSION 94227
UTI Truck Accident Off-Site, Screen Modeling -- OFFSITE
1 Point source; 26 receptors up to 50 KM away; Vapor.
*** MOOELIMG OPTIONS USED: COMC RURAL ELEV ' —
09/14/95
12:5P SS
PAf
CRDRIS NOSTD
CONCURRENT 1-HR AVERAGE CONCENTRATION
FOR SOURCE GROUP: ALL
INCLUDING SOURCE(S): OFFSITE ,
VALUES ENDING WITH HOUR 3 FOR DAY
DISCRETE CARTESIAN RECEPTOR POINTS
CONC OF FUGITIVE IN MICROGRANS/N**3
X-COORD (M) Y-COORD (N)
CONC
X-COORD
-------
1SCOMDEP VERSION 94227
VTI Truck Accident Off-Site, Screen Modeling - OFFSITE
1 Point source; 26 receptors up to 50 KM away; Vapor.
MODELING OPTIONS USED: CONC RURAL ELEV ~
D9/14/
12:59:
PAGE
GRDRIS NOSTD
CONCURRENT 1-HR AVERAGE CONCENTRATION
FOR SOURCE GROUP: ALL
INCLUDING SOURCE(S): OFFSITE ,
VALUES ENDING WITH HOUR 4 FOR DAY 3
DISCRETE CARTESIAN RECEPTOR POINTS
•* CONC OF FUGITIVE IN MICROGRANS/M**3
X-COORD (M) Y-COORD (M)
CONC
X-COORD (M) Y-COORD (N)
CONC
100.00
300.00
500.00
700.00
900.00
1250.00
1750.00
2250.00
3000.00
5000.00
10000.00
20000.00
40000.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
193.67424
41.28204
20.87127
14.64603
11.02856
7.58009
5.13345
3.67234
2.32929
1.21004
0.47965
0.20024
0.08382
200.00
400.00
600.00
800.00
1000.00
1500.00
2000.00
2500.00
4000.00
7500.00
15000.00
30000.00
50000.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
71.26071
27.03833
17.17882
12.56148
9.49537
6.16377
4.29847
2.91874
1 .57697
0.73389
0.28773
0.11959
0.06356
Volume VII
Appendix VTJ-4
External Review Draft
Do Not Cite or Quote
-------
ISCOMDEP VERSION 94227
WTI Truck Accident Off-Site, Screen Modeling -- OFFSITE
1 Point source; 26 receptors up to SO KM auay; Vapor.
09/U/95
\Zf ^'
P*
*** MODELING OPTIONS USED: CONC RURAL ELEV
GRDRIS NOSTD
CONCURRENT 1-HR AVERAGE CONCENTRATION
FOR SOURCE GROUP: ALL
INCLUDING SOURCE(S): OFFSITE ,
VALUES ENDING WITH HOUR 5 FOR DAY 3
*** DISCRETE CARTESIAN RECEPTOR POINTS
CONC OF FUGITIVE IN M1CROGRAMS/M**3
X-COORD (M) Y-COORD (M)
CONC
X-COORD (N) Y-COORD (M)
CONC
100.00
300.00
500.00
700.00
900.00
1250.00
1750.00
2250.00
3000.00
5000.00
10000.00
20000.00
40000.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
167.07159
39.38115
18.40491
12.88981
9.68692
6.63757
4.47852
3.19289
2.01554
1.04128
0.41005
0.17054
0.07121
200.00
400.00
600.00
800.00
1000.00
1500.00
2000.00
2500.00
4000.00
7500.00
15000.00
30000.00
50000.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
72.02185
24.94218
15.13344
11.04373
8.32914
5.38715
3.74304
2.53110
1.35980
0.62931
0.24537
0.10169
0.05397
Volume VH
Appendix VII-4
External Review Draft
Do Not Cite or Quote
-------
ISCOMOEP VERSION 94227
VTl Truck Accident Off-Site, Screen Modeling •- OFFSITE
1 Point source; 26 receptors up to 50 KM away; Vapor.
09/14/S
12:59:<
PAGE t
*** MODELING OPTIONS USED: CONC RURAL ELEV
GRDRIS NOSTD
CONCURRENT 1-HR AVERAGE CONCENTRATION
FOR SOURCE GROUP: ALL
INCLUDING SOURCE(S): OFFSITE .
VALUES ENDING WITH HOUR 6 FOR DAY
DISCRETE CARTESIAN RECEPTOR POINTS
CONC OF FUGITIVE IN MICROGRAMS/M**3
X-COORD (M) Y-COORD (M)
CONC
X-COORD (M) Y-COORD (M)
CONC
100.00
300.00
500.00
700.00
900.00
1250.00
1750.00
2250.00
3000.00
5000.00
10000.00
20000.00
40000.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
141.85909
36.88860
16.55301
11.53413
8.65274
5.91276
3.97645
2.82656
1.77700
0.91374
0.35786
0.14837
0.06183
200.00
400.00
600.00
800.00
1000.00
1500.00
2000.00
2500.00
4000.00
7500.00
15000.00
30000.00
50000.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
66.84029
23.47149
13.55362
9.87302
7.43120
4.79085
3.31799
2.23572
1.19531
0.55061
0.21371
0.08836
0.04684
Volume VII
Appendix VTJ-4
External Review Draft
Do Not Cite or Quote
-------
ISCOMDEP VERSION 94227
WTI Truck Accident Off-Site, Screen Modeling — OFFSITE
1 Point source; 26 receptors up to 50 KM away; Vapor.
09/14/95
12:^"^
PA
*** MODELING OPTIONS USED: CONC RURAL ELEV
GRDRIS NOSTD
THE 1ST HIGHEST 1-HR AVERAGE CONCENTRATION
INCLUDING SOURCE(S): OFFSITE ,
VALUES FOR SOURCE GROUP: ALL
DISCRETE CARTESIAN RECEPTOR POINTS
CONC OF FUGITIVE IN MICROGRANS/M**3
X-COORD (M) Y-COORD (M)
CONC
(YYMMDDHH)
X-COORD (N) Y-COORD (M)
CONC
(YYMMDDHH)
100.00
300.00
500.00
700.00
900.00
1250.00
1750.00
2250.00
3000.00
5000.00
10000.00
20000.00
40000.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
218.07961
41.28204
34.85668
23.24654
19.16001
14.09468
9.60246
8.58492
6.38994
3.45708
1.44461
0.70805
0.46332
(93010303)
(93010304)
(93010224)
(93010224)
(93010224)
(93010224)
(93010224)
(93010224)
(93010224)
(93010224)
(93010224)
(93010215)
(93010215)
200.00
400.00
600.00
800.00
1000.00
1500.00
2000.00
2500.00
4000.00
7500.00
15000.00
30000.00
50000.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
72.27760
34.11783
28.97512
21.61471
20.69304
11.29400
9.10952
7.88782
4.43724
2.15608
0.88569
0.56321
0.38992
(93010221 )
(93010301)
(93010224)
(93010224)
(93010224)
(93010224)
(93010224)
(93010224)
(93010224)
(93010224)
(93010224)
(93010215)
(93010215)
Volume VH
Appendix VII-4
External Review Draft
Do Not Cite or Quote
-------
ISCOMDEP VERSION 94227
VTI Truck Accident Off-Site, Screen Modeling — OFFSITE
1 Point source; 26 receptors up to 50 KM away; Vapor.
*** MODELING OPTIONS USED: CONC RURAL ELEV~
GRDRIS NOSTD
RANK
THE MAXIMUM 50 1-HR AVERAGE CONCENTRATION VALUES FOR SOURCE GROUP: ALL
INCLUDING SOURCE(S): OFFSITE ,
CONC (YYMMDDHH) AT
** CONC OF FUGITIVE IN NICROGRAMS/M**3
RECEPTOR (XR,YR) OF TYPE RANK
CONC (YYMMDDHH) AT
RECEPTOR (XR,YR) OF
1.
2.
3.
4.
5.
6.
7.
8.
9.
10.
11.
12.
13.
14.
15.
16.
17.
18.
19.
20.
21.
22.
23.
24.
25.
***
218.07961 (93010303) AT (
207.63899 (93010220) AT (
193.67424 (93010304) AT (
191.37901 (93010219) AT (
189.36391 (93010221) AT (
169.67842 (93010222) AT (
167.07159 (93010305) AT (
151.22041 (93010223) AT (
141.85909 (93010306) AT (
135.07504 (93010302) AT (
120.40126 (93010218) AT (
72.27760 (93010221) AT (
72.02185 (93010305) AT (
71.26071 (93010304) AT (
70.66110 (93010222) AT (
66.92157 (93010223) AT (
66.84029 (93010306) AT (
62.23378 (93010217) AT (
57.56957 (93010301) AT (
56.09013 (93010220) AT (
47.28311 (93010303) AT (
41.28204 (93010304) AT (
39.82120 (93010221) AT (
39.38115 (93010305) AT (
38.22855 (93010222) AT (
RECEPTOR TYPES: GC * GRIDCART
GP * GRIDPOLR
DC * DISCCART
DP - DISCPOLR
BO « BOUNDARY
100.00,
100.00,
100.
00,
100.00,
100.00,
100.
100.
100.
100.
100.
100.
200.
200.
200.
200.
200.
200.
100.
100.
200.
200.
300.
300.
300.
300.
00,
00.
00,
00,
00,
00.
00.
00,
00,
00.
00.
00.
00.
00,
00.
00,
00.
00,
00.
00.
0.00)
0.00)
0.00)
0.00)
0.00)
0.00)
0.00)
0.00)
0.00)
0.00)
0.00)
0.00}
0.00)
0.00)
0.00)
0.00)
0.00)
0.00)
0.00)
0.00)
0.00)
0.00)
0.00)
0.00)
0.00)
DC
DC
DC
DC
DC
DC
DC
DC
DC
DC
DC
DC
DC
DC
DC
DC
DC
DC
DC
DC
DC
DC
DC
DC
DC
26.
27.
28.
29.
30.
31.
32.
33.
34.
35.
36.
37.
38.
39.
40.
41.
42.
43.
44.
45.
46.
47.
48.
49.
50.
38.04164
36.88860
36.17004
35.42534
34.85668
34.11783
33.45829
33.35661
32.51575
31.28687
30.85106
28.97512
28.70184
27.67290
27.03833
27.03052
26.37437
25.63425
25.24093
25.15523
24.98931
24.94218
24.20550
24.09174
23.68114
(93010219)
(93010306)
(93010223)
(93010220)
(93010224)
(93010301)
(93010301)
(93010302)
(93010224)
(93010303)
(93010303)
(93010224)
(93010302)
(93010301)
(93010304)
(93010302)
(93010216)
(93010219)
(93010221)
(93010301)
(93010302)
(93010305)
(93010303)
(93010222)
(93010302)
-
AT (
AT (
AT (
AT (
AT (
AT (
AT (
AT (
AT (
AT (
AT (
AT (
AT (
AT (
AT (
AT (
AT (
AT (
AT (
AT (
AT {
AT (
AT (
AT (
AT (
200.00,
300.00,
300.00,
300.00,
500.00,
400.00,
500.00,
400.00,
400.00,
300.00,
400.00,
600.00,
500.00,
600.00,
400.00,
300.00,
100.00,
300.00,
400.00,
300.00,
200.00,
400.00,
500.00,
400.00,
600.00,
0.00)
0.00)
0.00)
0.00}
0.00)
0.00)
0.00)
0.00)
0.00}
0.00}
0.00)
0.00)
0.00)
0.00)
0.00}
0.00)
0.00)
0.00)
0.00)
0.00)
0.00)
0.00)
0.00)
0.00)
0.00)
Volume VH
Appendix VTJ-4
External Review Draft
Do Not Cite or Quote
-------
*** ISCOMDEP VERSION 94227 •** *** UT1 Truck Accident Off-Site, Screen Modeling — OFFSITE *** 09/14/95
**• 1 Point source; 26 receptors up to 50 KM away; Vapor. *** 12:5?' ~
PAGf
•*• HOOELING OPTIONS USED: CONC RURAL ELE\T CRDRIS NOSTD
*** THE SUMMARY OF HIGHEST 1-HR RESULTS ***
** CONC OF FUGITIVE IN NICROGRANS/M**3 **
DATE NETWORK
GROUP ID AVERAGE CONC (YYNMDDHH) RECEPTOR (XR. YR. 2ELEV, ZFLAG) OF TYPE GRID-ID
ALL HIGH 1ST HIGH VALUE IS 218.07961 ON 93010303: AT ( 100.00, 0.00, 292.60, 0.00) DC
*** RECEPTOR TYPES: GC - GRIDCART
GP * GRIDPOLR
DC - DISCCART
DP = DISCPOLR
BD * BOUNDARY
Volume VH External Review Draft
Appendix VH-4 Do Not Cite or QuOte
-------
*** ISCOMDEP VERSION 94227 *** **• WTI Truck Accident Off-Site, Screen Modeling -- OFFSITE *** 09/U>
*** 1 Point source; 26 receptors up to 50 KM away; Vapor. *** 12:59:
_^ _. PAGE
*** MODELING OPTIONS USED: CONC RURAL ELEV ~~ GRDRIS NOSTD
*** Message Sunmary : ISCOMDEP Model Execution ***
Summary of Total Messages —
A Total of 0 Fatal Error Message(s)
A Total of 1 Warning Message(s)
A Total of 0 Informational Message(s)
FATAL ERROR MESSAGES
*** NONE ***
WARNING MESSAGES •*•*•••*
SO W320 17 PPARM : Source Parameter May Be Out-of-Range for Parameter OS
*** ISCOMDEP Finishes Successfully
««»««•««« ««««*»IH»*«« *»*«*«•«*««»•
V°lume External Review Draft
Appendix VH^ Do Not Cite or Quote
-------
ATTACHMENT 5
ISC-COMPDEP Outputs Using Real-Times Meteorology Data
Volume VII External Review Draft
Appendix VI1-4 Do Not Cite or Quote
-------
A. On-Site Fire Scenario
Volume VII External Review Draft
Appendix W-4 Do Not Cite or Quote
-------
CO STARTING
TITLEONE
TITLETWO
MOOELOPT
AVERTIME
POLLUTID
TERRHGTS
ELEVUNIT
RUNORMOT
•ERRORFIL
CO FINISHED
UTI Storage Tank Rupture, ISCOMDEP -- ONSITE ORGANIC TANK FARM
1 Point source; 936 receptors Tip to 50KH away; Vapor.
NOSTD GRORIS RURAL CONC
1 3 24 PERIOD
Chenical
ELEV
METERS
RUN
ONSITE.ERR
SO STARTING
LOCATION ONSITE POINT
** Point Source OS
** Parameters:
SO SRCPARAM ONSITE 1.0
186.385 105.445 212.1
HS TS VS DS
23.0 997. 0.225 15.14
** SO SRCPARAM ONSITE 1.0 23.0 997. 0.075 26.22
SO
so
so
so
so
so
so
so
so
so
so
so
BUILDHGT
BUILDHGT
BUILDHGT
BUILDHGT
BUILDHGT
BUILDHGT
BUILDWID
BUILDUID
BUILDWID
BUILDWID
BUILDWID
BUILDUID
ONSITE
ONSITE
ONSITE
ONSITE
ONSITE
ONSITE
ONSITE
ONSITE
ONSITE
ONSITE
ONSITE
ONSITE
17.37
17
17
.37
.37
17.37
17
17
50
18
51
50
18
51
.37
.37
.09
.23
.16
.09
.23
.16
17.37
17.37
17.37
17.37
17.37
17.37
47.00
26.39
51.86
47.00
26.39
51.86
17
17
17
17
17
17
42
33
50
42
33
50
.37
.37
.37
.37
.37
.37
.49
.74
.98
.49
.74
.98
17.37
17
17
17
17
17
36
40
50
36
40
50
.37
.37
.37
.37
.37
.68
.06
.09
.68
.06
.09
17.37
17.37
17.37
17.37
17.37
17.37
29.75
45.17
51.66
29.75
45.17
51.66
17.37
17.37
17.37
17.37
17.37
17.37
21.92
48.91
51.66
21.92
48.91
51.66
SO SRCGROUP ALL
SO FINISHED
RE STARTING
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
Volume Vn
Appendix VII-4
17.36482
34.72963
52.09445
69.45927
86.82409
104.18890
121.55372
138.91853
156.28336
173.64818
217.06021
260.47226
303.88431
347.29636
390.70837
434.12042
520.94452
694.59271
868.24084
1302.36133
1736.48169
2604.72266
3472.96338
5209.44531
6945.92676
98.48077
196.96155
295.44232
393.92310
492.40387
590.88464
689.36542
787.84619
886.32697
984.80774
1231.00964
1477.21167
1723.41357
1969.61548
2215.81738
2462.01929
2954.42334
3939.23096
4924.03857
7386.05811
9848.07715
14772.11620
19696.15430
29544.23240
39392.30860
213.4
225.6
225.6
225.6
225.6
225.6
243.8
256.0
280.4
286.5
353.6
353.6
310.9
347.5
353.6
359.7
347.5
341.4
341.4
365.8
360.0
340.0
340.0
360.0
350.0
External Review Draft
Do Not Cite or Quote
-------
RE DISCCART
RE OISCCART
RE DISCCART
RE OISCCART
RE DISCCART
RE DISCCART
RE1 DISCCART
RE DISCCART
RE OISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
HE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
Volume Vn
Appendix Vfl-4
8682.40820
34.20201
68.40403
102.60604
136.80806
171.01007
205.21208
239.41409
273.61612
307.81812
342.02014
427.52518
513.03021
598.53522
684.04028
769.54529
855.05035
1026.06042
1368.08057
1710.10071
2565.15112
3420.20142
5130.30225
6840.40283
10260.60450
13680.80570
17101.00590
50.00000
100.00000
150.00000
200.00000
250.00000
300.00000
350.00000
400.00000
450.00000
500.00000
625.00000
750.00000
875.00000
1000.00000
1125.00000
1250.00000
1500.00000
2000.00000
2500.00000
3750.00000
5000.00000
7500.00000
10000.00000
15000.00000
20000.00000
25000.00000
64.27876
128.55753
192.83627
257.11505
321.39380
385.67255
449.95132
514.23010
578.50885
642.78760
49240.38670
93.96926
187.93852
281.90778"
375.87704
469.84631
563.81555
657.78485
751.75409
845.72339
939.69263
1174.61572
1409.53894
1644.46204
1879.38525
2114.30835
2349.23145
2819.07788
3758.77051
4698.46289
7047.69482
9396.92578
14095.38960
18793.85160
28190.77930
37587.70310
46964.63280
86.60254
173.20506
259.80762
346.41016
433.01270
519.61523
606.21777
692.82031
779.42285
866.02539
1082.53174
1299.03809
1515.54443
1732.05078
1948.55713
2165.06348
2598.07617
3464.10156
4330.12695
6495.19043
8660.25391
12990.38090
17320.50780
25980.76170
34641.01560
43301.26950
76.60445
153.20889
229.81334
306.41779
383.02222
459.62668
536.23114
612.83557
689.44000
766.04443
360.0
213.4
225.6
" 225 .^
225.6
225.6
225.6
237.7
243.8
256.0
286.5
329.2
347.5
335.3
347.5
353.6
359.7
362.4
329.2
359.7
369.7
385.9
340.0
340.0
360.0
380.0
390.0
213.4
219.5
225.6
225.6
225.6
225.6
225.6
231.6
243.8
262.1
225.6
347.5
359.7
353.6
353.6
329.2
323.1
361.2
366.7
378.0
396.2
320.0
360.0
380.0
370.0
400.0
213.4
213.4
225.6
225.6
225.6
225.6
225.6
225.6
225.6
243.8
External Review Draft
Do Not Cite or Quote
-------
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
803.48450
964.18140
1124.87830
1285.57520
1446.27209
1606.96899
1928.36279
2571.15039
3213.93799
4820.90674
6427.87598
9641.81348
12855.75200
19283.62700
25711.50390
32139.37890
76.60445
153.20889
229.81334
306.41779
383.02222
459.62668
536.23114
612.83557
689.44000
766.04443
957.55554
1149.06665
1340.57776
1532.08887
1723.59996
1915.11108
2298.13330
3064.17773
3830.22217
5745.33350
7660.44434
11490.66700
15320.88870
22981.33400
30641.77730
38302.22270
86.60254
173.20508
259.80762
346.41016
433.01270
519.61523
606.21777
692.82031
779.42285
866.02539
1082.53174
1299.03809
1515.54443
1732.05078
1948.55725
2165.06348
2598.07617
3464.10156
4330.12695
6495.19043
8660.25391
957.55554
1149.06665
1340.57776
1532.08887"
1723.59996
1915.11108
2298.13330
3064.17773
3830.22217
5745.33350
7660.44434
11490.66700
15320.88870
22981.33400
30641.77730
38302.22270
64.27876
128.55753
192.83629
257.11505
321.39380
385.67258
449.95132
514.23010
578.50885
642.78760
803.48450
964.18140
1124.87830
1285.57520
1446.27209
1606.96899
1928.36279
2571.15039
3213.93799
4820.90723
6427.87598
9641.81445
12855.75200
19283.62890
25711.50390
32139.38090
50.00000
W» WWv
150.00000
199.99998
249.99996
300.00000
349.99997
399.99997
449.99997
499.99997
624.99994
749.99994
874.99994
VTTaT^TT*
1125.00000
1249.99988
1499.99988
lyyy»TTToe
2499.99976
3749.99976
4999.99951
280.4
353.6
361.5
"353.6
353.6
353.6
335.3
353.9
353.0
378.0
396.4
376.0
380.0
360.0
420.0
420.0
213.4
207.3
213.4
219.5
219.5
219.5
219.5
219.5
225.6
219.5
219.5
323.1
353.6
353.6
335.3
347.5
347.5
341.4
335.3
373.1
396.2
360.0
380.0
380.0
420.0
420.0
213.4
207.3
207.3
201.2
207.3
213.4
213.4
213.4
213.4
219.5
225.6
219.5
243.8
292.6
310.9
323.1
317.0
323.1
359.7
378.9
408.7
Volume VII
Appendix VTJ-4
External Review Draft
Do Not Cite or Quote
-------
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
Volume Vn
12990.38090
17320.50780
25980.76170
34641.01560
43301.26950
93.96926
187.93852
281.90778
375.87704
469.84631
563.81555
657.78485
751.75409
845.72333
939.69263
1174.61572
1409.53894
1644.46204
1879.38525
2114.30835
2349.23145
2819.07788
3758.77051
4698.46289
7047.69462
9396.92578
14095.38960
18793.85160
28190.77930
37587.70310
46984.63280
98.48077
196.96155
295.44232
393.92310
492.40387
590.88464
689.36542
787.84619
886.32697
984.80774
1231.00964
1477.21167
1723.41357
1969.61548
2215.81738
2462.01929
2954.42334
3939.23096
4924.03857
7386.05811
9848.07715
14772.11620
19696.15430
29544.23240
39392.30860
49240.38670
100.00000
200.00000
300.00000
400.00000
500.00000
600.00000
7499.99951
9999.99902
14999.99900
19999.99806"'
24999.99800
34.20201
68.40403
102.60604
136.80806
171.01007
205.21208
239.41411
273.61612
307.81815
342.02014
427.52518
513.03021
598.53528
684.04028
769.54535
855.05035
1026.06042
1368.08057
1710.10071
2565.15112
3420.20142
5130.30225
6840.40283
10260.60450
13680.80570
17101.00780
17.36482
34.72964
52.09447
69.45929
86.82411
104.18893
121.55375
138.91858
156.28340
173.64822
217.06027
260.47232
303.88437
347.29645
390.70850
434.12054
520.94464
694.59290
868.24109
1302.36157
1736.48218
2604.72314
3472.96436
5209.44629
6945.92871
8682.41113
0.00001
0.00002
0.00002
0.00003
0.00004
0.00005
380.0
360.0
380.0
~ysa.a~
420.0
207.3
201.2
202.7
202.7
207.3
207.3
207.3
213.4
213.4
213.4
213.4
213.4
213.4
213.4
213.4
231.6
231.6
310.9
384.0
384.0
370.3
360.0
380.0
400.0
360.0
400.0
207.3
202.7
202.7
202.7
202.7
202.7
202.7
202.7
202.7
202.7
202.7
202.7
213.4
207.3
207.3
231.6
304.8
346.6
365.8
384.0
371.9
320.0
360.0
380.0
380.0
400.0
207.3
202.7
202.7
202.7
202.7
202.7
Appendix VH.-4
External Review Draft
Do Not Cite or Quote
-------
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE' DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
Volume VII
700.00000
800.00000
900.00000
1000.00000
1250.00000
1500.00000
1750.00000
2000.00000
2250.00000
2500.00000
3000.00000
4000.00000
5000.00000
7500.00000
10000.00000
15000.00000
20000.00000
30000.00000
40000.00000
50000.00000
98.48077
196.96155
295.44232
393.92310
492.40387
590.88464
689.36542
787.84619
886.32697
984.80774
1231.00964
1477.21167
1723.41357
1969.61548
2215.81738
2462.01929
2954.42334
3939.23096
4924.03857
7386.05811
9848.07715
14772.11620
19696.15430
29544.23240
39392.30860
49240.38670
93.96926
187.93852
281.90778
375.87704
469.84631
563.81555
657.78485
751.75409
845.72339
939.69263
1174.61584
1409.53894
1644.46216
1879.38525
2114.30835
2349.23169
2819.07788
0.00005
0.00006
0.00007
0.00008"
0.00009
0.00011
0.00013
0.00015
0.00017
0.00019
0.00023
0.00030
0.00038
0.00057
0.00075
0.00113
0.00151
0.00226
0.00302
0.00377
-17.36482
-34.72964
-52.09446
•69.45927
-86.82410
-104.18891
•121.55373
-138.91855
-156.28337
-173.64819
-217.06023
-260.47229
-303.88434
-347.29639
-390.70840
-434.12045
-520.94458
-694.59277
-868.24091
-1302.36145
-1736.48181
-2604.72290
-3472.96362
-5209.44580
-6945.92725
-8682.40918
-34.20201
-68.40402
-102.60603
-136.80804
-171.01006
-205.21207
-239.41408
-273.61609
-307.81812
-342.02011
-427.52515
-513.03015
-598.53522
-684.04022
-769.54529
-855.05029
-1026.06030
202.7
202.7
202.7
'202.7
243.8
341.4
323.1
341.4
304.8
292.6
310.9
359.7
402.3
347.5
380.1
360.0
360.0
380.0
400.0
360.0
207.3
202.7
202.7
202.7
202.7
202.7
202.7
219.5
225.6
329.2
347.5
353.6
323.1
341.4
341.4
323.1
347.5
353.6
386.5
353.6
360.0
340.0
380.0
380.0
380.0
400.0
207.3
202.7
202.7
202.7
202.7
213.4
256.0
298.7
286.5
323.1
347.5
347.5
310,9
353.6
350.2
347.5
347.5
Appendix VII-4
External Review Draft
Do Not Cite or Quote
-------
RE OISCCART
RE OISCCART
RE DISCCART
RE OISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE OISCCART
RE DISCCART
RE OISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE OISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE OISCCART
RE DISCCART
RE OISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE OISCCART
RE DISCCART
Volume VH
3758.77051
4698.46338
7047.69482
9396.92676
14095.38960
18793.85350
28190.77930
37587.70700
46984.63280
86.60254
173.20508
259.80762
346.41016
433.01270
519.61523
606.21777
692.82031
779.42285
866.02539
1082.53174
1299.03809
1515.54443
1732.05078
1948.55713
2165.06348
2598.07617
3464.10156
4330.12695
6495.19043
8660.25391
12990.38090
17320.50780
25980.76170
34641.01560
43301.26950
76.60445
153.20889
229.81332
306.41779
383.02222
459.62665
536.23108
612.83557
689.44000
766.04443
957.55554
1149.06665
1340.57776
1532.08887
1723.59998
1915.11108
2298.13330
3064.17773
3830.22217
5745.33301
7660.44434
11490.66600
-1368.08044
-1710.10059
-2565.15088
-3420. 20flT
-5130.30176
-6840.40234
-10260.60350
-13680.80470
-17101.00590
•50.00000
-100.00001
-150.00002
-200.00002
-250.00003
-300.00003
-350.00003
-400.00003
-450.00003
-500.00006
-625.00006
-750.00006
-875.00006
-1000.00012
-1125.00012
-1250.00012
-1500.00012
-2000.00024
-2500.00024
-3750.00049
-5000.00049
-7500.00098
-10000.00100
-15000.00200
-20000.00200
-25000.00200
-64.27876
-128.55753
-192.83629
-257.11505
-321.39380
-385.67258
-449.95132
-514.23010
-578.50885
-642.78760
-803.48456
-964.18146
-1124.87830
-1285.57520
-1446.27222
-1606.96912
-1928.36292
-2571.15039
-3213.93823
-4820.90723
-6427.87646
-9641.81445
15320.88870 -12855.75290
22981.33200 -19283.62890
30641.77730 -25711.50590
38302.22270 -32139.38090
64.27876
128.55753
-76.60445
-153.20889
345.9
371.9
365.8
'408.?
380.0
360.0
360.0
360.0
360.0
207.3
202.7
202.7
202.7
213.4
268.2
317.0
347.5
353.6
347.5
310.9
359.7
335.3
359.7
359.7
347.5
365.8
359.7
353.6
402.3
396.2
380.0
380.0
360.0
360.0
360.0
207.3
202.7
202.7
202.7
243.8
298.7
323.1
353.6
353.6
353.6
353.6
359.7
341.4
353.6
353.6
341.4
359.7
359.7
359.7
408.4
408.4
380.0
360.0
360.0
360.0
360.0
207.3
202.7
Appendix VTJ-4
External Review Draft
Do Not Cite or Quote
-------
RE
RE
RE
RE
RE
RE
RE
RE
RE
RE
RE
RE
RE
RE
RE
RE
RE
RE
RE
RE
RE
RE
RE
RE
RE
RE
RE
RE
RE
RE
RE
RE
RE
RE
RE
RE
RE
RE
RE
RE
RE
RE
RE
RE
RE
RE
RE
RE
RE
RE
RE
RE
RE
RE
RE
RE
RE
RE
RE
RE
RE
RE
RE
DISCCART
DISCCART
DISCCART
DISCCART
DISCCART
DISCCART
DISCCART
DISCCART
DISCCART
DISCCART
DISCCART
DISCCART
DISCCART
DISCCART
DISCCART
DISCCART
DISCCART
DISCCART
DISCCART
DISCCART
DISCCART
DISCCART
DISCCART
DISCCART
DISCCART
DISCCART
DISCCART
DISCCART
DISCCART
DISCCART
DISCCART
DISCCART
DISCCART
DISCCART
DISCCART
DISCCART
DISCCART
DISCCART
DISCCART
DISCCART
DISCCART
DISCCART
DISCCART
DISCCART
DISCCART
DISCCART
DISCCART
DISCCART
DISCCART
DISCCART
DISCCART
DISCCART
DISCCART
DISCCART
DISCCART
DISCCART
DISCCART
DISCCART
DISCCART
DISCCART
DISCCART
DISCCART
DISCCART
Volume
192.
257.
321.
385.
449.
514.
578.
642.
803.
964.
1124.
1285.
1446.
1606.
1928.
2571.
3213.
4820.
6427.
9641.
12855.
19283.
25711.
32139.
50.
100.
150.
200.
250.
300.
350.
400.
450.
500.
625.
750.
875.
1000.
1125.
1250.
1500.
2000.
2500.
3750.
5000.
7500.
10000.
83629
11505
39380
67258
95132
23010
50885
78760
48450
18146
87830
57520
27209
96899
36292
15039
93799
90723
87598
81445
75200
62890
50390
38090
00000
00001
00002
00002
00002
00003
00003
00003
00003
00003
00006
00006
00006
00006
00012
00012
00012
00012
00024
00024
00049
00049
00100
15000.00100
20000.
25000.
34.
68.
102.
136.
171.
00200
00200
20202
40405
60606
80809
01012
205.21213
239.
273.
307.
342.
41415
61618
81821
02023
427.52527
513.
598.
VII
03033
53540
-229
-306
-383
.81332
.41779
.02222
202.7
202.7
268.2
-459.62661" 'Wr.tT
-536
.23108
•612.83557
•689
-766
-957
-1149
-1340
•1532
-1723
-1915
-2298
-3064
-3830
-5745
-7660
-11490
-15320
-22981
-30641
.44000
.04443
.55554
.06665
.57776
.08887
COOOfl
•7TYTO
.11108
.13330
.17773
.22217
.33350
.44434
.66700
.88870
.33400
.77730
-38302.22270
-86
.60254
-173.20508
-259
•346
-433
-519
-606
-692
-779
-866
-1082
-1299
-1515
-1732
-1948
-2165
-2598
-3464
-4330
-6495
-8660
-12990
-17320
-25980
-34641
.80762
.41016
.01270
.61523
.21777
.82031
.42285
.02539
.53174
.03809
.54443
.05078
.55713
.06348
.07617
.10156
.12695
.19043
.25391
.38090
.50780
.76170
.01560
-43301 .26950
-93
-187
-281
-375
-469
-563
.96926
.93852
.90778
.87704
.84628
.81555
-657.78479
-751
-845
-939
-1174
-1409
-1644
.75409
.72333
.69257
.61572
.53894
.46204
310.9
323.1
329.2
323.1
347.5
359.7
329.2
359.7
353.6
359.7
408.4
420.6
371.9
392.0
390.1
340.0
380.0
400.0
400.0
380.0
207.3
202.7
202.7
213.4
268.2
298.7
310.9
323.1
323.1
329.2
298.7
341.4
341.4
359.7
365.8
371.9
408.4
420.6
408.4
408.4
396.2
340.0
360.0
420.0
400.0
400.0
207.3
202.7
202.7
207.3
268.2
292.6
304.8
304.8
286.5
286.5
304.8
310.9
304.8
Appendix VII-4
External Review Draft
Do Not Cite or Quote
-------
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
Volume VH
684.04047
769.54547
855.05054
1026.06067
1368.08093
1710.10107
2565.15161
3420.20215
5130.30322
6840.40430
10260.60640
13680.80860
17101.01170
17.36483
34.72966
52.09449
69.45932
86.82414
104.18897
121.55380
138.91864
156.28346
173.64828
217.06036
260.47244
303.88452
347.29657
390.70865
434.12073
520.94489
694.59314
868.24146
1302.36218
1736.48291
2604.72437
3472.96582
5209.44873
6945.93164
8682.41504
0.00002
0.00003
0.00005
0.00006
0.00008
0.00009
0.00011
0.00012
0.00014
0.00015
0.00019
0.00023
0.00026
0.00030
0.00034
0.00038
0.00045
0.00060
0.00075
0.00113
0.00151
0.00226
0.00302
0.00453
-1879.38513
-2114.30835
-2349.23145
-2819.0778$
-3758.77026
-4698.46289
-7047.69434
-9396.92578
-14095.38870
-18793.85160
-28190.77730
-37587.70310
-46984.62890
-98.48077
-196.96155
-295.44232
-393.92310
-492.40387
-590.88464
-689.36542
-787.84619
-886.32697
-984.80774
-1231.00964
-1477.21155
-1723.41357
-1969.61548
-2215.81738
-2462.01929
-2954.42310
-3939.23096
-4924.03857
-7386.05811
-9848.07715
-14772.11620
-19696.15430
-29544.23240
-39392.30860
-49240.38670
-100.00000
-200.00000
-300.00000
-400.00000
-500.00000
-600.00000
-700.00000
-800.00000
-900.00000
-1000.00000
-1250.00000
-1500.00000
-1750.00000
-2000.00000
-2250.00000
-2500.00000
-3000.00000
-4000.00000
-5000.00000
-7500.00000
-10000.00000
-15000.00000
-20000.00000
-30000.00000
335.3
359.7
378.0
'396.7
402.3
411.5
402.3
408.1
360.0
360.0
420.0
400.0
420.0
207.3
202.7
202.7
202.7
249.9
286.5
280.4
274.3
286.5
286.5
298.7
304.8
304.8
298.7
298.7
365.8
402.3
390.1
414.5
408.4
398.1
380.0
360.0
400.0
400.0
400.0
207.3
202.7
202.7
202.7
219.5
274.3
280.4
274.3
243.8
298.7
304.8
304.8
304.8
292.6
298.7
365.8
406.3
402.3
396.2
390.1
396.2
380.0
360.0
380.0
Appendix VTJ-4
External Review Draft
Do Not Cite or Quote
-------
RE OISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
0.00604
0.00755
-17.36482
-34.72964
-52.09447
-69.45929
-86.82411
-104.18893
-121.55376
-138.91858
-156.28340
-173.64822
-217.06029
-260.47235
-303.88440
-347.29645
-390.70853
-434.12057
-520.94470
-694.59290
-868.24115
-1302.36169
-1736.48230
-2604.72339
-3472.96460
-5209.44678
-6945.92920
-8682.41113
-34.20201
-68.40403
-102.60605
-136.80806
-171.01009
-205.21210
-239.41411
-273.61612
-307.81815
-342.02017
-427.52521
-513.03021
-598.53528
-684.04034
-769.54535
-855.05042
-1026.06042
-1368.08069
-1710.10083
-2565.15112
-3420.20166
-5130.30225
-6840.40332
-10260.60450
-13680.80660
-17101.00780
-50.00000
-100.00000
-150.00000
-200.00000
-250.00000
-300.00000
-350.00000
-400.00000
-450.00000
-40000.00000
-50000.00000
-98.48077
- 196.96155"
-295.44232
-393.92310
-492.40387
-590.88464
-689.36542
-787.84619
-886.32697
-984.80774
-1231.00964
-1477.21167
-1723.41357
-1969.61548
-2215.81738
-2462.01929
-2954.42334
-3939.23096
-4924.03857
-7386.05811
-9848.07715
-14772.11620
-19696.15430
-29544.23240
-39392.30860
-49240.38670
-93.96926
-187.93852
-281 .90778
-375.87704
-469.84631
-563.81555
-657.78485
-751.75409
-845.72333
-939.69263
-1174.61572
-1409.53894
-1644.46204
-1879.38525
-2114.30835
-2349.23145
-2819.07788
-3758.77051
-4696.46289
-7047.69482
-9396.92578
-14095.38960
-18793.85160
-28190.77930
-37587.70310
-46984.62890
-86.60254
-173.20508
-259.80762
-346.41016
-433.01270
-519.61523
-606.21777
•692.82031
-779.42285
380.0
400.0
207.3
202.7
202.7
202.7
202.7
225.6
274.3
274.3
237.7
292.6
304.8
286.5
292.6
280.4
304.8
353.6
384.0
396.2
415.4
390.1
392.0
360.0
340.0
340.0
360.0
380.0
213.4
202.7
202.7
202.7
202.7
202.7
219.5
249.9
219.5
280.4
280.4
280.4
280.4
262.1
298.7
353.6
371.9
402.3
397.2
384.0
384.0
340.0
340.0
360.0
380.0
380.0
213.4
202.7
202.7
202.7
202.7
202.7
202.7
202.7
202.7
Volume VH
Appendix VTI-4
External Review Draft
Do Not Cite or Quote
-------
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE OISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE OISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE OISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
Volume Vn
-500.00000
-625.00000
-750.00000
-875.00000
-1000.00000
-1125.00000
-1250.00000
-1500.00000
-2000.00000
-2500.00000
-3750.00000
-5000.00000
-7500.00000
-10000.00000
-15000.00000
-20000.00000
-25000.00000
-64.27876
-128.55751
-192.83627
-257.11502
-321.39380
-385.67255
-449.95129
-514.23004
-578.50879
-642.78760
-803.48444
-964.18134
-1124.87830
-1285.57520
-1446.27197
-1606.96887
•1928.36267
-2571.15039
-3213.93774
-4820.90674
-6427.87549
-9641.81348
-12855.75100
-19283.62700
-25711.50200
-32139.37890
-76.60445
-153.20891
-229.81337
-306.41782
-383.02228
-459.62674
-536.23120
-612.83563
-689.44006
-766.04456
-957.55566
-1149.06677
-1340.57800
-1532.08911
-1723.60022
-1915.11133
-2298.13354
•3064.17822
-3830.22266
-5745.33398
-866.02539
-1082.53174
-1299.03809
-1515.54443"
-1732.05078
-1948.55713
-2165.06348
-2598.07617
-3464.10156
-4330.12695
-6495.19043
-8660.25391
-12990.38090
-17320.50780
-25980.76170
-34641.01560
-43301.26950
-76.60445
-153.20889
-229.81334
-306.41779
-383.02225
-459.62668
-536.23114
-612.83557
-689.44000
-766.04449
-957.55560
-1149.06677
-1340.57788
-1532.08899
-1723.60010
-1915.11121
-2298.13354
-3064.17798
-3830.22241
-5745.33350
-7660.44482
-11490.66700
-15320.88960
-22981.33400
-30641.77930
-38302.22270
-64.27875
-128.55750
-192.83624
-257.11499
-321.39374
-385.67249
-449.95123
-514.22998
-578.50873
-642.78748
-803.48438
-964.18121
-1124.87817
-1285.57495
-1446.27185
-1606.96875
-1928.36243
-2571.14990
-3213.93750
-4820.90625
219.5
219.5
_ 213.4
2T5.4~
231.6
231.6
292.6
359.7
396.2
414.5
396.2
392.6
360.0
380.0
360.0
360.0
380.0
213.4
202.7
202.7
202.7
202.7
202.7
202.7
202.7
202.7
202.7
202.7
213.4
213.4
213.4
213.4
213.4
371.9
378.0
396.2
396.2
378.0
349.0
360.0
360.0
380.0
360.0
213.4
201.2
207.3
207.3
202.7
202.7
202.7
202.7
207.3
207.3
207.3
207.3
207.3
213.4
213.4
256.0
323.1
359.7
384.0
378.0
Appendix VII-4
External Review Draft
Do Not Cite or Quote
-------
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
-7660.44531
-11490.66800
-15320.89060
-22981.33590
-30641.78130
-38302.22660
-86.60255
-173.20509
-259.80765
-346.41019
-433.01273
-519.61530
-606.21783
-692.82037
-779.42291
-866.02545
-1082.53186
-1299.03821
-1515.54456
-1732.05090
-1948.55725
-2165.06372
-2598.07642
-3464.10181
-4330.12744
-6495.19092
-8660.25488
-12990.38180
-17320.50980
-25980.76370
-34641.01950
-43301.27340
-93.96926
-187.93852
-281.90781
-375.87704
-469.84631
-563.81561
-657.78485
-751.75409
-845.72339
-939.69263
-1174.61584
-1409.53894
-1644.46216
-1879.38525
-2114.30835
-2349.23169
-2819.07788
-3758.77051
-4698.46338
-7047.69482
-9396.92676
-14095.38960
-18793.85350
-28190.77930
-37587.70700
-46984.63280
-98.48077
-196.96155
-295.44232
-393.92310
-492.40387
-6427.87500
-9641.81250
-12855.75000
-19283.62500"
-25711.50000
-32139.37500
-49.99999
-99.99998
-149.99997
" 199.99995
-249.99995
-299.99994
-349.99994
-399.99991
-449.99991
-499.99991
-624.99988
-749.99988
-674.99982
-999.99982
-1124.99976
-1249.99976
-1499.99976
-1999.99963
-2499.99951
-3749.99927
-4999.99902
-7499.99854
-9999.99805
-14999.99710
-19999.99610
-24999.99410
-34.20201
-68.40401
-102.60602
-136.80803
-171.01004
-205.21204
-239.41405
-273.61606
-307.81805
-342.02008
-427.52509
-513.03009
-598.53510
-684.04016
-769.54517
-855.05017
-1026.06018
-1368.08032
-1710.10034
-2565.15039
-3420.20068
-5130.30078
-6840.40137
-10260.60160
-13680.80270
-17101.00390
-17.36481
-34.72963
-52.09444
-69.45925
-86.82407
378.0
360.0
380.0
400.0
400.0
380.0
213.4
213.4
213.4
207.3
213.4
213.4
213.4
213.4
213.4
213.4
225.6
274.3
329.2
310.9
286.5
256.0
243.8
365.8
372.5
378.0
402.3
360.0
380.0
380.0
400.0
360.0
213.4
213.4
213.4
213.4
213.4
213.4
213.4
219.5
219.5
213.4
353.6
353.6
341.4
335.3
353.6
304.8
243.8
298.7
359.7
365.8
402.3
380.0
400.0
380.0
400.0
360.0
213.4
213.4
213.4
213.4
213.4
Volume VH
Appendix VTJ-4
External Review Draft
Do Not Cite or Quote
-------
V..
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
REOISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE OISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DlSCOUtr
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
-590.88464
-689.36542
-787.84619
-886.32697
-984.80774
-1231.00964
-1477.21167
-1723.41357
-1969.61548
-2215.81738
-2462.01929
-2954.42334
-3939.23096
-4924.03857
-7386.05811
-9848.07715
-14772.11620
-19696.15430
-29544.23240
-39392.30860
-49240.38670
-100.00000 .
-200.00000
-300.00000
-400.00000
-500.00000
-600.00000
-700.00000
-800.00000
-900.00000
-1000.00000
-1250.00000
-1500.00000
-1750.00000
-2000.00000
-2250.00000
-2500.00000
-3000.00000
-4000.00000
-5000.00000
-7500.00000
-10000.00000
-15000.00000
-20000.00000
-30000.00000
-40000.00000
-50000.00000
-98.48077
•196.96155
-295.44232
-393.92310
-492.40387
-590.88464
-689.36542
-787.84619
-886.32697'
-984.80774
-1231.00964
-1477.21167
-1723.41357
-1969.61548
-2215.81738
RE DISCCART -2462.01929
Volume Vn
-104.18888
-121.55370
-138.91850
-156.28333*
-173.64813
-217.06017
-260.47220
-303.88422
-347.29626
-390.70828
^434.12033
-520.94440
-694.59253
-868.24066
-1302.36096
-1736.48132
-2604.72192
-3472.96265
-5209.44385
-6945.92529
-8682.40625
0.00000
0.00000
0.00000
0.00000
0.00001
0.00001
0.00001
0.00001
0.00001
0.00001
0.00001
0.00002
0.00002
0.00002
0.00003
0.00003
0.00004
0.00005
0.00006
0.00009
0.00012
0.00018
0.00024
0.00036
0.00048
0.00060
17.36481
34.72963
52.09445
69.45926
86.82407
104.18890
121.55371
138.91852
156.28334
173.64815
217.06020
260.47223
303.88428
347.29630
390.70834
434.12039
213.4
213.4
219.5
22T.6
310.9
359.7
359.7
365.8
371.9
353.6
371.9
353.6
365.8
365.8
390.1
339.9
360.0
380.0
420.0
400.0
400.0
213.4
213.4
213.4
213.4
213.4
213.4
213.4
213.4
243.8
298.7
304.8
304.8
335.3
341.4
371.9
371.9
371.9
378.0
371.9
371.9
360.0
340.0
360.0
380.0
380.0
400.0
213.4
213.4
213.4
213.4
213.4
225.6
225.6
237.7
243.6
280.4
317.0
304.8
298.7
341.4
371.9
353.6
Appendix VTJ-4
External Review Draft
Do Not Cite or Quote
-------
RE D1SCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
-2954.42334
-3939.23096
-4924.03857
-7386.05811
-9848.07715
-14772.11620
-19696.15430
-29544.23240
-39392.30860
-49240.38670
-93.96926
-187.93852
-281.90781
-375.87704
-469.84631
-563.81561
-657.78485
-751.75409
-845.72339
-939.69263
-1174.61584
-1409.53894
-1644.46216
-1879.38525
-2114.30835
-2349.23169
-2819.07788
-3758.77051
-4698.46338
-7047.69482
-9396.92676
-14095.38960
-18793.85350
-28190.77930
-37587.70700
-46964.63280
-86.60255
-173.20509
-259.80765
-346.41019
-433.01273
-519.61530
-606.21783
-692.82037
-779.42291
-866.02545
-1082.53186
-1299.03821
•1515.54456
-1732.05090
-1948.55725
-2165.06372
-2598.07642
-3464.10181
-4330.12744
-6495.19092
-8660.25488
-12990.38180
-17320.50980
-25980.76370
-34641.01950
-43301.27340
-76.60445
520.94446
694.59259
868.24078
1302.36121"
1736.48157
2604.72241
3472.96313
5209.44482
6945.92627
8682.40820
34.20201
68.40401
102.60603
136.80803
171.01004
205.21205
239.41406
273.61606
307.81808
342.02008
427.52512
513.03015
598.53516
684.04016
769.54523
855.05023
1026.06030
1368.08032
1710.10046
2565.15063
3420.20093
5130.30127
6840.40186
10260.60250
13680.80370
17101.00390
49.99999
99.99998
149.99997
199.99997
249.99995
299.99994
349.99994
399.99994
449.99994
499.99991
624.99988
749.99988
874.99988
999.99982
1124.99988
1249.99976
1499.99976
1999.99963
2499.99951
3749.99951
4999.99902
7499.99902
9999.99805
14999.99800
19999.99610
24999.99610
64.27875
365.8
353.6
378.0
~385-.0-
389.2
400.0
420.0
380.0
380.0
400.0
213.4
213.4
213.4
219.5
225.6
225.6
243.8
274.3
286.5
298.7
317.0
298.7
298.7
359.7
384.0
378.0
378.0
378.0
378.0
371.9
424.9
420.0
360.0
400.0
380.0
400.0
213.4
213.4
219.5
231.6
225.6
231.6
268.2
304.8
310.9
304.8
292.6
323.1
359.7
371.9
371.9
378.0
378.0
378.0
384.0
384.0
426.7
400.0
400.0
420.0
400.0
350.0
213.4
Volume VH
Appendix VII-4
External Review Draft
Do Not Cite or Quote
-------
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE' DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
-153.20891
-229.81335
-306.41782
-383.02225
-459.62671
-536.23114
-612.83563
-689.44006
-766.04449
-957.55566
-1149.06677
-1340.57788
-1532.08899
-1723.60022
-1915.11133
-2298.13354
-3064.17796
-3830.22266
-5745.33398
-7660.44531
-11490.66800
-15320.89060
-22981.33590
-30641.78130
-38302.22660
-64.27877
-128.55754
-192.83632
-257.11508
-321.39386
-385.67264
-449.95142
-514.23016
-578.50897
-642.78772
-803.48468
-964.18158
-1124.87854
-1285.57544
-1446.27246
-1606.96936
-1928.36316
-2571.15088
-3213.93872
-4820.90820
-6427.87744
-9641.81641
-12855.75490
-19283.63280
-25711.50980
-32139.38670
-50.00002
-100.00003
-150.00005
-200.00006
-250.00009
-300.00009
-350.00012
-400.00012
-450.00015
-500.00018
-625.00024
-750.00024
128.55750
192.83626
257.11499
321.3937T
385.67252
449.95126
514.22998
578.50879
642.78754
803.48438
964.18127
1124.87817
1285.57507
1446.27185
1606.96875
1928.36255
2571.15015
3213.93750
4820.90625
6427.87500
9641.81250
12855.75000
19283.62500
25711.50000
32139.37500
76.60443
153.20886
229.81331
306.41772
383.02216
459.62662
536.23102
612.83545
689.43988
766.04431
957.55542
1149.06653
1340.57764
1532.08862
1723.59973
1915.11084
2298.13306
3064.17725
3830.22168
5745.33252
7660.44336
11490.66500
15320.88670
22981.33010
30641.77340
38302.21880
86.60253
173.20506
259.80759
346.41013
433.01266
519.61517
606.21771
692.82025
779.42279
866.02533
1082.53162
1299.03796
213.4
225.6
231.6
225.Y
231.6
268.2
304.8
316.4
317.0
304.8
341.4
353.6
365.8
371.9
378.0
384.0
359.7
384.0
378.0
379.2
360.0
400.0
400.0
400.0
370.0
213.4
225.6
231.6
231.6
225.6
231.6
274.3
304.8
310.9
310.9
317.0
347.5
353.6
353.6
359.7
365.8
384.0
384.0
378.0
378.0
378.0
380.0
400.0
400.0
360.0
360.0
213.4
225.6
231.6
231.6
225.
243.
249.
243.
304.
304.
286.5
329.2
Volume VH
Appendix VH.-4
External Review Draft
Do Not Cite or Quote
-------
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE-DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
•875.00051
-1000.00037
-1125.00037
-1250.00049
-1500.00049
-2000.00073
-2500.00098
-3750.00122
-5000.00195
-7500.00244
-10000.00390
-15000.00490
-20000.00780
-25000.00780
-34.20204
-68.40408
-102.60611
-136.80815
-171.01018
-205.21222
-239.41425
-273.61630
-307.81833
-342.02036
-427.52545
-513.03052
-598.53564
-684.04071
-769.54584
-855.05090
-1026.06104
-1368.08142
-1710.10181
-2565.15283
-3420.20361
-5130.30566
-6840.40723
-10260.61130
-13680.81450
-17101.01760
-17.36484
-34.72969
-52.09453
-69.45937
-86.82422
-104.18906
-121.55391
-138.91875
-156.28360
-173.64844
-217.06055
-260.47266
-303.88477
-347.29688
-390.70898
-434.12109
-520.94531
-694.59375
-868.24219
-1302.36328
-1736.48438
-2604.72656
-3472.96875
1515.54431
1732.05066
1948.55688
347.5
353.6
353.6
2165.06323 — 3W.tr
2598.07593
3464.10132
4330.12646
6495.18994
8660.25293
12990.37990
17320.50590
25980.75980
34641.01170
43301.26560
93.96925
187.93851
281.90778
375.87701
469.84628
563.81555
657.78479
751.75403
845.72327
939.69257
1174.61572
1409.53882
1644.46191
1879.38513
2114.30811
2349.23145
2819.07764
3758.77026
4698.46289
7047.69385
9396.92578
14095.38770
18793.85160
28190.77540
37587.70310
46984.62890
96.48077
196.96155
295.44232
393.92310
492.40384
590.88464
689.36542
787.84619
886.32697
984.80768
1231.00964
1477.21155
1723.41345
1969.61536
2215.81738
2462.01929
2954.42310
3939.23071
4924.03857
7386.05762
9848.07715
14772.11520
19696.15430
384.0
384.0
378.0
365.8
371.9
360.0
360.0
340.0
380.0
350.0
213.4
225.6
225.6
225.6
225.6
243.8
262.1
286.5
280.4
292.6
323.1
353.6
359.7
359.7
329.2
347.5
378.0
385.0
371.9
329.2
349.0
360.0
360.0
340.0
370.0
350.0
213.4
225.6
225.6
225.6
225.6
243.8
262.1
292.6
298.7
298.7
335.3
365.8
359.7
359.7
341.4
378.0
384.0
378.0
365.8
341.4
339.9
340.0
360.0
Volume VH
Appendix VH-4
External Review Draft
Do Not Cite or Quote
-------
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE FINISHED
ME STARTING
ME INPUTFIL
ME ANENHGHT
ME SURFDATA
ME UAIRDATA
ME PROFFILE
NE PROFFILE
** DAYRANGE
ME FINISHED
TG STARTING
INPUTFIL
LOCATION
TG FINISHED
-5209.45313
-6945.93750
-8682.42188
-0.00003
-0.00006
-0.00009
-0.00012
-0.00015
-0.00018
-0.00021
-0.00024
-0.00027
-0.00030
-0.00038
-0.00045
-0.00053
-0.00060
-0.00068
-0.00075
-0.00091
-0.00121
-0.00151
-0.00226
-0.00302
-0.00453
-0.00604
-0.00906
-0.01208
-0.01510
DEPBIN.NET
30.0 METERS
94823 1993
94823 1993
TEMPS ISC_TEMP
WINDS ISc'uiND
1/3
utilOOk.out
538.4 4497.8
29544.23050
39392.30860
49240.38670
100.00000"
200.00000
300.00000
400.00000
500.00000
600.00000
700.00000
800.00000
900.00000
1000.00000
1250.00000
1500.00000
1750.00000
2000.00000
2250.00000
2500.00000
3000.00000
4000*00000
5000.00000
7500.00000
10000.00000
15000.00000
20000.00000
30000.00000
40000.00000
50000.00000
.STIC
.STK
km
340.0
330.0
320.0
~ 213.4"
225.6
225.6
225.6
225.6
237.7
256.0
280.4
298.7
292.6
353.6
323.1
341.4
317.0
359.7
359.7
378.0
383.4
359.7
371.9
380.1
360.0
340.0
380.0
350.0
350.0
OU STARTING
RECTABLE ALLAVE FIRST-SECOND
** DAYTABLE ALLAVE ^
MAXTABLE ALLAVE 50
** MAXIFILE 3 ALL 30.0 NAXIALL.FIL 25
** MAXIFILE 24 ALL 10.0 NAXIALL.FIL 25
** POSTFILE 1 ALL INDIV POST2C.BIN 20
** POSTFILE PERIOD ALL PLOT PSTANALL.FIL 21
** Note that the following two input cards generate PLOTFILEs with the file
** unit dynamically allocated by the ISCST2 program. When porting the model
** to another coaputer system, the user may need to specify the file units
** as is done on the previous four input cards.
** PLOTFILE 3 ALL 2ND PLT03ALL.FIL
** PLOTFILE 24 ALL 2ND PLT24ALL.FIL
OU PLOTFILE 1 ALL 1ST ONSITE.1
OU PLOTFILE 3 ALL 1ST ONSITE.3
OU PLOTFILE 24 ALL 1ST ONSITE.24
Volume VII
Appendix VTJ-4
External Review Draft
Do Not Cite or Quote
-------
OU PLOTFILE PERIOD ALL ONSITE.ANN
** OU PLOTFILE 1 ALL 1ST ONSITE.PL2
OU FINISHED
SETUP Finishes Successfully
•*«»•«•«««
/"""->•
Volume VH External Review Draft
Appendix VH^ Do Not Cite or Quote
-------
* ISCST2 (94227): WTI Storage Tank Rijtture, ISCOMDEP -- ONSITE ORGANIC TANK FARM
* MODELING OPTIONS USED:
* CONC RURAL ELEV GRDRIS NOSTD
*
*
*
*
*
PLOT FILE OF HIGH 1ST HIGH 1-HR
FOR A
FORMAT
X
17.36482
34.72963
52.09445
69.45927
86.82409
104.18890
121.55373
138.91852
156.28337
173.64818
217.06021
260.47229
303.88428
347.29639
390.70837
434.12042
520.94452
694.59271
868.24084
1302.36133
1736.48169
2604.72241
3472.96313
5209.44531
6945.92627
8682.40820
34.20201
68.40403
102.60603
136.80806
171.01007
205.21207
239.41408
273.61615
307.81812
342.02011
427.52518
513.03021
598.53522
684.04022
769.54523
855.05035
1026.06042
1368.08057
1710.10071
2565.15112
3420.20142
5130.30176
6840.40283
10260.60450
13680.80570
17101.00590
50.00000
100.00000
VALUES FOR SOURCE GROUP
: ALL
TOTAL OF 936 RECEPTORS.
: (3(1X,F13.5)
Y
98.48077
196.96155
295.44235
393.92307
492.40384
590.88470
689.36542
787.84613
886.32697
984.80774
1231.00964
1477.21167
1723.41370
1969.61548
2215.81738
2462.01929
2954.42310
3939.23096
4924.03809
7386.05762
9848.07715
14772.11520
19696.15430
29544.23050
39392.30860
49240.38670
93.96926
187.93851
281.90778
375.87701
469.84631
563.81555
657.78491
751.75409
845.72339
939.69263
1174.61572
1409.53894
1644.46204
1879.38525
2114.30835
2349.23145
2819.07788
3758.77051
4698.46289
7047.69482
9396.92578
14095.38960
18793.85350
28190.77930
37587.70310
46984.63670
86.60254
173.20508
,1X,F8.2,3X,AS
CONC
16.79521
16.61840
5'.53868
5.30869
3.10193
3.69308
10.97034
13.74630
12.91760
16.09260
36.37793
29.38692
18.73467
19.57441
18.22014
16.84233
9.75648
6.88101
5.18808
3.01776
2.12708
1.25943
0.88135
0.57982
0.43556
0.34810
20.09486
62.92639
9.69793
9.42351
7.11029
5.43599
5.06535
4.94948
5.26656
15.08930
29.01570
23.78149
19.79313
16.52250
14.10990
12.23069
9.67375
6.04362
5.15676
3.00116
1.99441
1.73969
1.57623
0.73020
0.36371
0.26962
26.97623
59.04914
,2XfA8,2X
ZELEV
213.40
225.60
225.60
225.60
225.60
225.60
243.80
256.00
280.40
286.50
353.60
353.60
310.90
347.50
353.60
359.70
347.50
341.40
341.40
365.80
360.00
340.00
340.00
360.00
350.00
360.00
213.40
225.60
225.60
225.60
225.60
225.60
237.70
243.80
256.00
286.50
329.20
347.50
335.30
347.50
353.60
359.70
362.40
329.20
359.70
369.70
385.90
340.00
340.00
360.00
380.00
390.00
213.40
219.50
,A4)
AVE
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-»R
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
Volume VII
GRP
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL .
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL*
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
NIVAL
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST '
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
Appendix VII-4
External Review Draft
Do Not Cite or Quote
-------
150.00000
200.00000
250.00000
300.00000
350.00000
400.00000
450.00000
500.00000
625.00000
750.00000
875.00000
1000.00000
1125.00000
1250.00000
1500.00000
2000.00000
2500.00000
3750.00000
5000.00000
7500.00000
10000.00000
15000.00000
20000.00000
25000.00000
64.27876
128.55754
192.83627
257.11508
321.39377
385.67258
449.95132
514.23016
578.50885
642.78766
803.48456
964.18140
1124.87830
1285.57520
1446.27197
1606.96912
1928.36292
2571.15039
3213.93799
4820.90625
6427.87549
9641.81250
12855.75200
19283.62700
25711.50390
32139.37890
76.60445
153.20888
229.81335
306.41779
383.02225
459.62671
536.23120
612.83557
689.44000
766.04443
957.55554
1149.06665
1340.57764
Volume VH
Appendix VII-4
259.80762
346.41016
433.01273
519.61517
606.21777
692.82031
779.42291
866.02539
1082.53174
1299.03821
1515.54443
1732.05090
1948.55713
2165.06348
2598.07617
3464.10156
4330.12695
6495.19043
8660.25391
12990.38090
17320.50780
25980.76170
34641.01560
43301.26560
76.60445
153.20888
229.81335
306.41779
383.02225
459.62671
536.23120
612.83557
689.44000
766.04443
957.55554
1149.06665
1340.57764
1532.08899
1723.59998
1915.11108
2298.13330
3064.17798
3830.22192
5745.33301
7660.44434
11490.66600
15320.88870
22981.33400
30641.77730
38302.22270
64.27876
128.55754
192.83629
257.11508
321.39377
385.67261
449.95132
514.23016
578.50885
642.78766
803.48456
964.18140
1124.87830
27.20872
15.02902
14.53630
8.97993 ~"
6.45860
8.83360
14.90733
15.70679
7.27158
27.62148
21.64511
18.32998
15.58878
14.43524
11.43595
7.01111
5.10995
2.97486
1.97396
2.82748
0.96089
0.51697
0.37340
0.26257
33.78500
34.00709
100.29875
57.44691
33.55591
13.53698
7.75491
5.32684
5.06455
15.17323
22.78652
27.62006
21.84241
18.55730
15.75471
13.64595
11.16552
7.19737
5.33632
2.98305
1.96627
1.24070
0.86084
0.67867
0.32632
0.24829
20.86079
0.00000
55.07706
45.54440
21.33775
17.94308
13.29508
9.78028
9.54597
6.58953
4.85307
29.78035
22.22086
225.60
225.60
225.60
225.60
225.60
231.60
243.80
262.10
225.60
347.50
359.70
353.60
353.60
329.20
323.10
361.20
366.70
378.00
396.20
320.00
360.00
380.00
370.00
400.00
213.40
213.40
225.60
225.60
225.60
225.60
225.60
225.60
225.60
243.80
280.40
353.60
361.50
353.60
353.60
353.60
335.30
353.90
353.00
378.00
398.40
376.00
380.00
360.00
420.00
420.00
213.40
207.30
213.40
219.50
219.50
219.50
219.50
219.50
225.60
219.50
219.50
323.10
353.60
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
.ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL,
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
External Review Draft
Do Not Cite or Quote
-------
1532.08899
1723.59998
1915.11108
2298.13330
3064.17798
3830.22192
5745.33301
7660.44434
11490.66600
15320.88870
22981.33400
30641.77730
38302.22270
86.60254
173.20508
259.80762
346.41016
433.01273
519.61517
606.21777
692.82031
779.42291
866.02539
1082.53174
1299.03821
1515.54443
1732.05090
1948.55725
2165.06348
2598.07617
3464.10156
4330.12695
6495.19043
8660.25391
12990.38090
17320.50780
25980.76170
34641.01560
43301.26560
93.96926
187.93851
281 .90778
375.87701
469.84631
563.81555
657.78491
751.75409
845.72333
939.69263
1174.61572
1409.53894
1644.46204
1879.38525
2114.30835
2349.23145
2819.07788
3758.77051
4698.46289
7047.69482
9396.92578
14095.38960
18793.85350
28190.77930
Volume VII
Appendix VII-4
1285.57520
1446.27197
1606.96912
1928.36292
2571.15039
3213.93799
4820.90674
6427.87549
9641.81348
12655.75200
19283.62700
25711.50390
32139.38090
50.00000
TY •TTTTV
150.00000
199.99997
249.99997
300.00000
349.99994
399.99994
449.99994
499.99994
625.00000
750.00000
875.00000
1000.00000
1125.00000
1250.00000
1500.00000
2000.00000
2499.99976
3749.99976
4999.99902
7499.99902
9999.99902
14999.99900
19999.99800
24999.99800
34.20201
68.40403
102.60603
136.80806
171.01007
205.21207
239.41411
273.61615
307.81815
342.02011
427.52518
513.03021
598.53526
684.04022
769.54535
855.05035
1026.06042
1368.08057
1710.10071
2565.15112
3420.20142
5130.30176
6840.40283
10260.60450
18.47447
16.48253
13.82754
10177820
7.44035
5.59988
3.05963
1.99478
1.29926
0.86138
0.51739
0.32525
0.24724
27.17797
0.00000
18.20800
9.06094
16.68992
29.36513
25.16099
22.83578
20.88769
27.52405
28.21201
17.26831
25.65752
21.83312
21.23749
17.81623
14.05590
9.35248
6.25248
3.38971
2.09213
1.31895
1.12988
0.53638
0.37378
0.25133
12.33390
0.00000
7.39211
8.37012
10.97494
7.23640
4.84703
9.17665
9.66306
9.78090
9.29955
8.43639
7.42095
7.03921
6.56121
24.12316
20.86826
9.63144
5.81526
3.33586
2.35683
1.39824
0.90783
0.50488
353.60
335.30
347.50
- 357.50
341.40
335.30
373.10
396.20
360.00
380.00
380.00
420.00
420.00
213.40
207.30
207.30
201.20
207.30
213.40
213.40
213.40
213.40
219.50
225.60
219.50
243.80
292.60
310.90
323.10
317.00
323.10
359.70
378.90
408.70
380.00
360.00
380.00
380.00
420.00
207.30
201.20
202.70
202.70
207.30
207.30
207.30
213.40
213.40
213.40
213.40
213.40
213.40
213.40
213.40
231.60
231.60
310.90
384.00
384.00
370.30
360.00
360.00
400.00
1-HR ALL
1-HR ALL
1-HR ALL
1-HR ALL
1-HR ALL
1-HR ALL
1-HR ALL
1-HR ALL
1-HR ALL
1-HR ALL
1-HR ALL
1-HR ALL
1-HR ALL
1-HR ALL
1-HR ALL
1-HR ALL
1-HR ALL
1-HR ALL
1-HR ALL
1-HR ALL
1-HR ALL
1-HR ALL
1-HR ALL
1-HR ALL
1-HR ALL
1-HR ALL
1-HR ALL
1-HR ALL
1-HR ALL
1-HR ALL
1-HR ALL
1-HR ALL
1-HR ALL
1-HR ALL
1-HR ALL
1-HR ALL
1-HR ALL
1-HR ALL
1-HR ALL
1-HR ALL
1-HR ALL
1-HR ALL
1-HR ALL
1-HR ALL
1-HR ALL
1-HR ALL
1-HR ALL
1-HR ALL
1-HR ALL 4
1-HR ALL
1-HR ALL
1-HR ALL
1-HR ALL
1-HR ALL
1-HR ALL
1-HR ALL
1-HR ALL
1-HR ALL
1-HR ALL
1-HR ALL
1-HR ALL
1-HR ALL
1-HR ALL
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
External Review Draft
Do Not Cite or Quote
-------
37587.70310
46984.63670
98.48077
196.96155
295.44235
393.92307
492.40384
590.88470
689.36542
787.84613
886.32697
984.80774
1231.00964
1477.21167
1723.41370
1969.61548
2215.81738
2462.01929
2954.42310
3939.23096
4924.03809
7386.05762
9848.07715
14772.11520
19696.15430
29544.23050
39392.30860
49240.38670
100.00000
200.00000
300.00000
400.00000
500.00000
600.00000
700.00000
800.00000
900.00000
1000.00000
1250.00000
1500.00000
- 1750.00000
2000.00000
2250.00000
2500.00000
3000.00000
4000.00000
5000.00000
7500.00000
10000.00000
15000.00000
20000.00000
30000.00000
40000.00000
50000.00000
98.48077
196.96155
295.44235
393.92307
492.40384
590.88470
689.36542
787.84613
886.32697
Volume VH
Appendix VII-4
13680.80570
17101.00780
17.36482
34.72964
52.09447
69.45930
86.82410
104.18893
121.55376
138.91856
15i&.28340
173.64821
217.06027
260.47235
303.88434
347.29648
390.70850
434.12051
520.94470
694.59296
868.24103
1302.36169
1736.48218
2604.72290
3472.96411
5209.44580
6945.92822
8682.41113
0.00001
0.00002
0.00002
0.00003
0.00004
0.00005
0.00005
0.00006
0.00007
0.00008
0.00009
0.00011
0.00013
0.00015
0.00017
0.00019
0.00023
0.00030
0.00038
0.00057
0.00075
0.00113
0.00151
0.00226
0.00302
0.00377
-17.36482
-34.72964
-52.09446
-69.45927
-86.82410
-104.18891
-121.55373
-138.91853
-156.28339
0.62891
0.26623
2.59753
4.W783
8.48135
4.77423
5.68795
4.62604
3.23299
3.10778
2.97928
2.75755
2.63681
2.60276
3.90019
3.02954
3.33715
10.95022
17.00310
10.19148
7.07213
3.61724
2.53417
4.01392
1.03218
0.57193
0.39790
0.28149
1.92787
5.61738
5.52209
7.13858
4.49742
2.27909
1.83655
1.56700
1.53429
1.81226
15.36937
40.81028
34.50356
27.13080
25.28048
40.27191
16.60923
9.75752
6.26888
4.22683
2.58858
1.57603
1.20421
0.59988
0.39122
0.80650
5.56092
3.58844
1.14107
1.82645
3.62259
2.75895
2.71497
16.38509
29.87196
360.00
400.00
207.30
~202.7D
202.70
202.70
202.70
202.70
202.70
202.70
202.70
202.70
202.70
202.70
213.40
207.30
207.30
231.60
304.80
346.60
365.80
384.00
371.90
320.00
360.00
380.00
380.00
400.00
207.30
202.70
202.70
202.70
202.70
202.70
202.70
202.70
202.70
202.70
243.80
341.40
323.10
341.40
304.80
292.60
310.90
359.70
402.30
347.50
380.10
360.00
360.00
380.00
400.00
360.00
207.30
202.70
202.70
202.70
202.70
202.70
202.70
219.50
225.60
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL 4
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
External Review Draft
Do Not Cite or Quote
-------
984.80774
1231.00964
1477.21167
1723.41370
1969.61548
2215.81738
2462.01929
2954.42310
3939.23096
4924.03809
7386.05762
9848.07715
14772.11520
19696.15430
29544.23050
39392.30860
49240.38670
93.96926
187.93851
281.90778
375.87701
469.84631
563.81555
657.78491
751.75409
845.72339
939.69263
1174.61584
1409.53894
1644.46216
1879.36525
2114.30835
2349.23145
2819.07788
3758,77051
4698.46338
7047.69482
9396.92676
14095.38960
18793.85550
28190.77930
37587.70700
46984.63670
86.60254
173.20508
259.80762
346.41016
433.01273
519.61517
606.21777
692.82031
779.42291
866.02539
1082.53174
1299.03821
1515.54443
1732.05090
1948.55713
2165.06348
2598.07617
3464.10156
4330.12695
6495.19043
Volume Vn
Appendix VII-4
-173.64819
-217.06023
-260.47232
-303.88431
-347.29642
-390.70840
-434.12045
-520.94458
-694.59277
-868.24091
-1302.36145
-1736.48181
-2604.72290
-3472.96338
-5209.44580
-6945.92676
-8682.40918
-34.20201
-68.40402
-102.60603
-136.80804
-171.01006
-205.21207
-239.41406
-273.61612
-307.81812
-342.02008
-427.52515
-513.03021
-598.53522
-684.04016
-769.54523
-855.05023
-1026.06030
-1368.08032
-1710.10059
•2565.15088
-3420.20093
-5130.30127
-6840.40234
-10260.60350
-13680.80470
-17101.00590
-50.00000
-100.00001
-150.00002
-200.00002
-250.00003
-300.00003
-350.00003
-400.00003
-450.00003
-500.00006
-625.00006
-750.00006
-875.00006
-1000.00012
-1125.00012
-1250.00012
-1500.00012
-2000.00024
-2500.00024
-3750.00049
47.39488
35.12508
30.09088
23.TS125
18.63275
16.09868
14.47428
14.88407
9.85795
6.85141
4.23198
3.01603
1.66579
1.22616
0.73998
0.52144
0.37662
7.23791
2.85747
2.54463
1.01166
1.63203
6.18410
60.31136
64.43974
56.14117
45.98010
34.14631
27.58699
21.40200
20.86284
17.59651
15.12554
12.18979
8.55346
7.06592
4.30253
2.70832
1.74549
1.73035
1.45142
1.19983
1.01686
7.53693
3.91989
1.94186
0.60907
1.40083
17.92687
68.57710
53.22472
45.19359
40.00871
33.03910
25.07100
19.61588
17.31517
17.01828
13.59570
11.98690
7.98354
6.89194
3.92211
329.20
347.50
353.60
-323.10
341.40
341.40
323.10
347.50
353.60
386.50
353.60
360.00
340.00
380.00
380.00
380.00
400.00
207.30
202.70
202.70
202.70
202.70
213.40
256.00
298.70
286.50
323.10
347.50
347.50
310.90
353.60
350.20
347.50
347.50
345.90
371.90
365.80
408.40
380.00
360.00
360.00
360.00
360.00
207.30
202.70
202.70
202.70
213.40
268.20
317.00
347.50
353.60
347.50
310.90
359.70
335.30
359.70
359.70
347.50
365.80
359.70
353.60
402.30
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
t-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL 4
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
External Review Draft
Do Not Cite or Quote
-------
8660.25391
12990.38090
17320.50780
25980.76170
34641.01560
43301.26560
76.60445
153.20888
229.81332
306.41779
383.02225
459.62668
536.23108
612.83557
689.44000
766.04443
957.55554
1149.06665
1340.57764
1532.08899
1723.59998
1915.11108
2298.13330
3064.17798
3830.22192
5745.33252
7660.44434
11490.66500
15320.88870
22981 .33200
30641.77730
38302.22270
64.27876
128.55754
192.83629
257.11508
321.39377
385.67261
449.95132
514.23016
578.50885
642.78766
803.48456
964.18146
1124.87830
1285.57520
1446.27197
1606.96912
1928.36292
2571.15039
3213.93799
4820.90674
6427.87549
9641.81348
12855.75200
19283.62700
25711.50390
32139.38090
50.00000
100.00001
150.00002
200.00002
250.00002
Volume Vn
Appendix VU-4
-5000.00049
-7500.00098
-10000.00100
-15000.00200
-20000.00200
-25000.00200
-64.27876
-128.55754
-192.83629
-257.11508
-321.39377
-385.67261
-449.95132
-514.23016
-578.50885
-642.78766
-803.48462
-964.18146
-1124.87830
-1285.57520
-1446.27209
-1606.96924
-1928.36292
-2571.15039
-3213.93823
-4820.90674
-6427.87598
-9641.81348
-12855.75290
-19283.62700
-25711.50590
-32139.38090
-76.60445
-153.20888
-229.81332
-306.41779
-383.02225
-459.62668
-536.23108
-612.83557
-689.44000
-766.04443
-957.55554
-1149.06665
-1340.57764
-1532.08899
-1723.59998
-19T5. 11108
-2298.13330
-3064.17798
-3830.22192
-5745.33301
-7660.44434
-11490.66600
-15320.88870
-22981.33400
-30641.77730
-38302.22270
-86.60254
-173.20508
-259.80762
-346.41016
-433.01273
2.78922
1.74092
1.22185
1.14*704
1.02555
0.91796
5.97005
2.41463
2.96012
0.83440
10.33235
75.25845
51.98043
45.41471
39.49252
34.75198
28.23686
24.33154
18.75085
16.38378
14.12012
11.84992
10.00768
6.79648
5.07020
2.91289
2.25937
1.46347
1.02686
0.68462
0.51672
0.41124
4.38358
2.52213
1.93266
1.76028
47.94463
80.78226
70.10665
59.61766
51.50412
46.42023
33.62111
21.11974
17.29639
14.43187
12.16668
11.21856
8.61108
5.96116
5.16030
3.02526
2.13824
1.97471
0.93038
0.53573
0.37855
0.30412
2.77348
4.71098
1.42148
3.18960
89.94217
396.20
380.00
380.00
"350.00
360.00
360.00
207.30
202.70
202.70
202.70
243.80
298.70
323.10
353.60
353.60
353.60
353.60
359.70
341.40
353.60
353.60
341.40
359.70
359.70
359.70
408.40
408.40
380.00
360.00
360.00
360.00
360.00
207.30
202.70
202.70
202.70
268.20
304.80
310.90
323.10
329.20
323.10
347.50
359.70
329.20
359.70
353.60
359.70
408.40
420.60
371.90
392.00
390.10
340.00
380.00
400.00
400.00
380.00
207.30
202.70
202.70
213.40
268.20
-HR
-HR
-HR
-HR
-HR
-HR
-HR
-HR
-HR
-HR
•HR
-HR
-HR
-HR
-HR
-HR
-HR
-HR
-HR
-HR
-HR
-HR
-HR
-HR
-HR
-HR
-HR
-HR
-HR
-HR
-HR
-HR
-HR
-HR
-HR
-HR
-HR
-HR
-HR
-HR
-HR
-HR
-HR
-HR
-HR
-HR
-HR
-HR
-HR
-HR
-HR
1-HR
1-HR
1-HR
-HR
-HR
-HR
-HR
-HR
-HR
-HR
-HR
-HR
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL .
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL i
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
External Review Draft
Do Not Cite or Quote
-------
300.00003
350.00003
400.00003
450.00003
500.00003
625.00006
750.00006
875.00006
1000.00006
1125.00012
1250.00012
1500.00012
2000.00012
2500.00024
3750.00024
5000.00049
7500.00049
10000.00100
15000.00100
20000.00200
25000.00200
34.20202
68.40405
102.60606
136.80809
171.01012
205.21213
239.41414
273.61621
307.81821
342.02023
427.52527
513.03033
598.53546
684.04047
769.54547
855.05054
1026.06079
1368.08081
1710.10107
2565.15161
3420.20190
5130.30273
6840.40430
10260.60550
13680.80860
17101.01170
17.36483
34.72966
52.09449
69.45933
86.82413
104.18897
121.55380
138.91862
156.28346
173.64827
217.06036
260.47244
303.88449
347.29657
390.70868
434.12073
Volume VII
Appendix VII-4
-519.61517
-606.21777
-692.82031
-779.42291
-866.02539
-1082.53174
-1299.03821
-1515.54443
-1732.05090
-1948.55713
-2165.06348
-2598.07617
-3464.10156
-4330.12695
-6495.19043
-8660.25391
-12990.38090
-17320.50780
-25980.76170
-34641.01560
-43301.26560
-93.96926
-187.93851
-281.90778
-375.87701
-469.84631
-563.81555
-657.78479
-751.75409
-845.72333
-939.69257
-1174.61572
-1409.53894
-1644.46204
-1879.38513
-2114.30835
-2349.23145
-2819.07788
-3758.77026
-4698.46289
-7047.69434
-9396.92578
-14095.38870
-18793.85350
-28190.77730
-37587.70310
-46984.62890
-98.48077
-196.96155
-295.44235
-393.92307
-492.40384
-590.88470
-689.36542
-787.84613
-886.32697
-984.80774
-1231.00964
-1477.21 US
-1723.41370
-1969.61548
-2215.81738
-2462.01929
66.08169
66.22234
56.64050
49.*3258-
43.79440
31.07504
26.65701
22.13122
17.84415
15.17900
13.08045
9.27843
6.20439
4.84817
2.84755
2.09474
1.65744
0.92703
0.50641
0.37813
0.28847
1.37136
3.75761
1.62716
2.51654
43.81467
45.06506
48.77239
42.64601
29.65354
26.27966
33.52998
27.65158
22.71933
18.64600
16.64400
14.82052
11.49531
8.14357
6.11550
3.85132
2.67066
1.75650
1.23901
0.66618
0.49753
0.35912
1.14018
1.51251
2.86994
1.32097
77.43610
53.58073
46.07051
34.40146
30.28798
26.93969
23.40391
20.81326
17.37552
13.80888
12.04333
14.79132
298.70
310.90
323.10
323.10
329.20
298.70
341.40
341.40
359.70
365.80
371.90
408.40
420.60
408.40
408.40
396.20
340.00
360.00
420.00
400.00
400.00
207.30
202.70
202.70
207.30
268.20
292.60
304.80
304.80
286.50
286.50
304.80
310.90
304.80
335.30
359.70
378.00
396.20
402.30
411.50
402.30
408.10
360.00
360.00
420.00
400.00
420.00
207.30
202.70
202.70
202.70
249.90
286.50
280.40
274.30
286.50
286.50
298.70
304.80
304.80
298.70
298.70
365.80
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR.
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL4
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
External Review Draft
Do Not Cite or Quote
-------
520.9089
694.59320
868.24146
1302.36230
1736.48279
2604.72412
3472.96558
5209.44824
6945.93115
8682.41504
0.00002
0.00003
0.00005
0.00006
0.00008
0.00009
0.00011
0.00012
0.00014
0.00015
0.00019
0.00023
0.00026
0.00030
0.00034
0.00038
0.00045
0.00060
0.00075
0.00113
0.00151
0.00226
0.00302
0.00453
0.00604
0.00755
-17.36482
-34.72964
-52.09447
-69.45930
-86.82410
-104.18893
-121.55376
-138.91856
-156.28340
-173.64821
-217.06029
-260.47238
-303.88437
-347.29648
-390.70853
-434.12054
-520.94470
-694.59296
-868.24115
-1302.36182
-1736.48218
-2604.72314
-3472.96436
-5209.44629
-6945.92871
-8682.41113
-34.20201
Volume VII
Appendix VII-4
-2954.42285
-3939.23096
-4924.03809
•7386.05762
-9848.07715
-14772.11520
-19696.15430
-29544.23050
-39392.30860
-49240.38670
-100.00000
-200.00000
-300.00000
-400.00000
-500.00000
-600.00000
-700.00000
-800.00000
-900.00000
-1000.00000
-1250.00000
-1500.00000
-1750.00000
-2000.00000
-2250.00000
-2500.00000
-3000.00000
-4000.00000
-5000.00000
-7500.00000
-10000.00000
-15000.00000
-20000.00000
-30000.00000
-40000.00000
-50000.00000
-98.48077
-196.96155
-295.44235
-393.92307
-492.40384
-590.88470
-689.36542
-787.84613
-886.32697
-984.80774
-1231.00964
-1477.21167
-1723.41370
-1969.61548
-2215.81738
-2462.01929
-2954.42310
-3939.23096
-4924.03809
-7386.05762
-9848.07715
-14772.11520
-19696.15430
-29544.23050
-39392.30860
-49240.38670
-93.96926
11.16015
8.32588
6.01372
3^76614—
2.73186
1 •O^OOT
1.60476
0.70296
0.49698
0.37916
1.18899
1.55394
2.78737
2.62236
15.94195
70.80370
60.24691
69.79847
65.60147
29.83179
24.86773
20.31074
17.00008
13.31331
11.84105
11.75147
9.55354
7.02217
5.53371
3.49347
2.44021
1.53054
1.03666
0.66141
0.46885
0.34421
1.77386
0.65214
2.04140
1.63558
4.05286
31.95099
46.12041
51.06259
42.27361
38.83279
30.91996
45.35656
20.88086
33.96033
15.57271
12.01333
8.74889
5.88201
4.14445
2.61500
1.80513
1.29386
1.05388
0.77197
0.56158
0.24594
12.70181
402.30
390.10
414.50
TO8.40
398.10
380.00
360.00
400.00
400.00
400.00
207.30
202.70
202.70
202.70
219.50
274.30
280.40
274.30
243.80
298.70
304.80
304.80
304.80
292.60
298.70
365.80
406.30
402.30
396.20
390.10
396.20
380.00
360.00
380.00
380.00
400.00
207.30
202.70
202.70
202.70
202.70
225.60
274.30
274.30
237.70
292.60
304.80
286.50
292.60
280.40
304.80
353.60
384.00
396.20
415.40
390.10
392.00
360.00
340.00
340.00
360.00
380.00
213.40
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL,
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
External Review Draft
Do Not Cite or Quote
-------
-68.40403
-102.60605
-136.80806
-171.01009
-205.21210
-239.41411
' -273.61615
-307.81815
-342.02014
-427.52521
-513.03021
-598.53528
-684.04034
-769.54535
-855.05042
-1026.06042
-1368.08069
-1710.10083
-2565.15112
-3420.20142
-5130.30176
-6840.40332
-10260.60450
-13680.80660
-17101.00780
-50.00000
-100.00000
-150.00000
-200.00000
-250.00000
-300.00000
-350.00000
-400.00000
-450.00000
-500.00000
-625.00000
-750.00000
-875.00000
-1000.00000
-1125.00000
-1250.00000
-1500.00000
-2000.00000
-2500.00000
-3750.00000
-5000.00000
-7500.00000
-10000.00000
-15000.00000
-20000.00000
-25000.00000
-64.27876
-128.55753
-192.83627
-257.11505
-321.39377
-385.67258
-449.95129
-514.23010
-578.50873
-642.78766
-803.48456
-964.18134
Volume VII
Appendix VIM
-187.93851
-281 .90778
-375.87701
-469.84631
-563.81555
-657.78491
-751.75409
-845.72333
-939.69263
-1174.61572
-1409.53894.
-1644.46204
-1879.38525
-2114.30835
-2349.23145
-2819.07788
-3758.77051
-4698.46289
-7047.69482
-9396.92578
-14095.38960
-18793.85350
-28190.77930
-37587.70310
-46984.62890
-86.60254
-173.20508
-259.80762
-346.41016
-433.01273
-519.61517
-606.21777
-692.82031
-779.42291
-866.02539
-1082.53174
-1299.03821
-1515.54443
-1732.05090
-1948.55713
-2165.06348
•2598.07617
-3464.10156
-4330.12695
-6495.19043
-8660.25391
-12990.38090
-17320.50780
-25980.76170
-34641.01560
-43301.26560
-76.60445
-153.20888
-229.81335
-306.41779
-383.02228
-459.62671
-536.23120
-612.83557
-689.44000
-766.04449
-957.55560
-1149.06689
0.86153
0.93634
1.68689
2H«ri85
2.94671
18.42518
48.94185
8.92396
27.73095
22.20589
20.58523
23.44049
24.37258
24.78194
12.96266
12.41295
8.66000
6.82291
4.40018
3.12666
1.70519
1.51687
0.80036
0.58628
0.44819
5.39811
1.32882
1.44368
1.52961
2.20288
2.48093
2.45845
2.27271
2.44395
9.57495
11.06908
8.12199
8.05387
15.33556
13.64701
16.00921
11.35485
8.74818
6.48581
4.25152
3.05143
1.82504
1 J5214
1.17298
0.99391
0.44796
5.64776
2.28080
2.93358
3.35882
2.75452
2.62344
2.44089
2.18523
1.91879
1.72417
2.03672
4.56743
202.70
202.70
202.70
-202.70
202.70
219.50
249.90
219.50
280.40
280.40
280.40
280.40
262.10
298.70
353.60
371.90
402.30
397.20
384.00
384.00
340.00
340.00
360.00
380.00
380.00
213.40
202.70
202.70
202.70
202.70
202.70
202.70
202.70
202.70
219.50
219.50
213.40
213.40
231.60
231.60
292.60
359.70
396.20
414.50
396.20
392.60
360.00
380.00
360.00
360.00
380.00
213.40
202.70
202.70
202.70
202.70
202.70
202.70
202.70
202.70
202.70
202.70 1
213.40 1
1-HR
-MR
-MR
-HR
-MR
-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
-HR
-HR
-HR
-HR
-HR
-HR
-HR
-HR
-HR
-HR
-HR
-HR
-HR
-HR
-HR
-HR
-HR
-HR
-HR
-HR
-HR
-HR
-HR
-HR
-HR
-HR
-HR
-HR
1-HR
1-HR
1-HR
-HR
-HR
-HR
-HR
-HR
-HR
1-HR
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL,
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
External Review Draft
Do Not Cite or Quote
-------
-1124.87830
-1285.57520
-1446.27185
-1606.96912
-1928.36279
-2571.15039
-3213.93774
-4820.90625
-6427.87500
-9641.81250
-12855.75100
-19283.62700
-25711.50200
-32139.37890
-76.60445
-153.20891
-229.81339
-306.41782
-383.02231
-459.62674
-536.23120
-612.83563
-689.44006
-766.04456
-957.55566
-1149.06689
-1340.57800
-1532.08911
-1723.60022
-1915.11121
-2298.13354
-3064.17847
-3830.22241
-5745.33350
-7660.44531
-11490.66700
-15320.89060
-22981 .33590
-30641.78130
-38302.22660
. -86.60255
-173.20509
-259.80765
-346.41019
-433.01276
-519.61530
-606.21783
-692.82037
-779.42297
-866.02551
-1082.53186
-1299.03833
-1515.54456
-1732.05090
-1948.55725
-2165.06372
-2598.07666
-3464.10181
-4330.12744
-6495.19092
-8660.25488
-12990.38180
-17320.50980
Volume VH
Appendix VIM
-1340.57788
-1532.08899
-1723.60010
-1915.11121
-2298.13354
-3064.17822
-3830.22241
-5745.33301
-7660.44482
-11490.66600
-15320.88960
-22981.33400
-30641 .77930
-38302.22270
-64.27876
-128.55751
-192.83624
-257.11499
-321.39371
-385.67252
-449.95123
-514.22998
-578.50867
-642.78754
-803.48444
-964.18115
-1124.87830
-1285.57483
-1446.27173
-1606.96887
-1928.36243
-2571.15015
-3213.93750
-4820.90576
-6427.87451
-9641.81250
-12855.75000
-19283.62500
-25711.50000
-32139.37700
-49.99999
-99.99998
-149.99997
-199.99994
-249.99994
-299.99991
-349.99991
-399.99988
-449.99988
-499.99988
-624.99988
-749.99988
-874.99982
-999.99982
-1124.99976
-1249.99976
-1499.99976
-1999.99963
-2499.99951
-3749.99927
-4999.99854
-7499.99805
-9999.99805
4.31771
4.53335
4.62574
4j5324*3 —
10.26536
7.03551
5.04717
2.95479
2.09482
2.16312
1.62116
1.03687
0.35845
0.56918
18.36013
2.49516
3.85340
5.35805
4.28739
4.57951
4.56497
4.35188
4.20323
3.83155
2.98818
2.33672
1.85432
2.26492
2.44622
13.31734
12.64878
8.06207
5.66495
3.43284
2.42915
1.50944
1.03402
0.59627
0.42175
0.33931
10.86113
10.37302
10.07992
4.63257
9.71033
8.79802
o.oBoBo
8.52437
8.36413
8.20592
19.95044
33.91507
24.77423
22.17144
26.00478
25.29171
23.81646
7.91192
5.86184
3.43095
2.27681
1.62650
1.03379
213.40
213.40
213.40
213.40
371.90
378.00
396.20
396.20
378.00
349.00
360.00
360.00
380.00
360.00
213.40
201.20
207.30
207.30
202.70
202.70
202.70
202.70
207.30
207.30
207.30
207.30
207.30
213.40
213.40
256.00
323.10
359.70
384.00
378.00
378.00
360.00
380.00
400.00
400.00
380.00
213.40
213.40
213.40
207.30
213.40
213.40
213.40
213.40
213.40
213.40
225.60
274.30
329.20
310.90
286.50
256.00
243.80
365.80
372.50
378.00
402.30
360.00
380.00
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL 4
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
External Review Draft
Do Not Cite or Quote
-------
-25980.76370
-34641.01950
-43301 .27340
-93.96926
-187.93851
-281.90778
-375.87701
-469.84631
-563.81561
-657.78491
-751.75409
-845.72339
-939.69263
-1174.61584
-1409.53894
-1644.46216
-1879.38525
-2114.30835
-2349.23145
-2819.07788
-3758.77051
-4698.46338
-7047.69482
-9396.92676
-14095.38960
-18793.85550
-28190.77930
-37587.70700
-46984.63670
-98.48077
-196.96155
-295.44235
-393.92307
-492.40384
-590.88470
-689.36542
-787.84613
-886.32697
-984.80774
-1231.00964
-1477.21167
-1723.41370
-1969.61548
-2215.81738
-2462.01929
-2954.42310
-3939.23096
-4924.03809
-7386.05762
-9848.07715
-14772.11520
-19696.15430
-29544.23050
-39392.30860
-49240.38670
-100.00000
-200.00000
-300.00000
-400.00000
-500.00000
-600.00000
-700.00000
-800.00000
Volume VB
Appendix VII-4
-14999.99710
-19999.99610
-24999.99410
-34.20201
-68.40401
-102.60602
-136.80803
-171.01004
-205.21204
-239.41403
-273.61609
-307.81805
-342.02008
-427.52509
-513.03009
-598.53516
-684.04016
•769.54517
-855.05017
-1026.06030
-1368.08020
-1710.10022
-2565.15039
-3420.20044
-5130.30029
-6840.40137
-10260.60160
-13680.80270
-17101.00390
-17.36481
-34.72963
-52.09444
-69.45926
-86.82407
-104.18888
-121.55370
-138.91849
-156.28334
-173.64813
-217.06018
-260.47223
-303.88422
-347.29630
-390.70831
-434.12033
-520.94446
-694.59253
-868.24066
-1302.36096
-1736.48120
-2604.72192
-3472.96240
-5209.44385
-6945.92480
-8682.40625
0.00000
0.00000
0.00000
0.00000
0.00001
0.00001
0.00001
0.00001
0.62859
0.42170
0.96324
7.86850
18.80952
25.32590
27.80023
28.05257
27.25646
23.85008
41.54283
38.07674
19.90770
34.40738
27.84657
23.96006
20.74460
16.98963
17.09451
22.68429
12.31288
6.09084
3.54936
2.97932
1.91597
1.28700
0.82624
0.55549
0.45978
29.34946
10.83371
4.15836
6.76746
6.52867
7.37878
7.82478
8.32453
9.51651
50.06646
34.01350
27.77934
23.66722
20.31624
18.26186
16.04321
13.38622
9.71345
7.51949
4.36529
3.36789
2.61097
1.78871
0.74273
0.55564
0.42435
12.76491
3.06791
6.02702
9.60168
8.68618
9.13065
9.20840
8.77952
380.00
400.00
360.00
~2T3.40
213.40
213.40
213.40
213.40
213.40
213.40
219.50
219.50
213.40
353.60
353.60
341.40
335.30
353.60
304.80
243.80
298.70
359.70
365.80
402.30
380.00
400.00
380.00
400.00
360.00
213.40
213.40
213.40
213.40
213.40
213.40
213.40
219.50
225.60
310.90
359.70
359.70
365.80
371.90
353.60
371.90
353.60
365.80
365.80
390.10
339.90
360.00
380.00
420.00
400.00
400.00
213.40
213.40
213.40
213.40
213.40
213.40
213.40 1
213.40 1
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-Hft
-MR
-HR
-HR
-HR
-HR
-HR
-HR
-HR
-HR
-HR
-HR
-HR
-HR
-HR
-HR
-HR
-HR
-HR
-HR
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL t
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
External Review Draft
Do Not Cite or Quote
-------
-900.00000
-1000.00000
-1250.00000
-1500.00000
-1750.00000
-2000.00000
-2250.00000
-2500.00000
-3000.00000
-4000.00000
-5000.00000
-7500,00000
-10000.00000
-15000.00000
-20000.00000
-30000.00000
-40000.00000
-50000.00000
-98.48077
-196.96155
-295.44235
-393.92307
-492.40384
-590.88470
-689.36542
-787.84613
-886.32697
-984.80774
-1231.00964
-1477.21167
-1723.41370
-1969.61548
-2215.81738
-2462.01929
-2954.42310
-3939.23096
-4924.03809
-7386.05762
-9848.07715
-14772.11520
-19696.15430
-29544.23050
-39392.30860
-49240.38670
-93.96926
-187.93851
-281.90778
-375.87701
-469.84631
-563.81561
-657.78491
-751.75409
-845.72339
-939.69263
-1174.61584
-1409.53894
-1644.46216
-1879.38525
-2114.30835
-2349.23145
-2819.07788
-3758.77051
-4698.46338
Volume VH
Appendix VII-4
0.00001
0.00001
0.00001
0.00002
0.00002
0.00002
0.00003
0.00003
0.00004
.0.00005
0.00006
0.00009
0.00012
0.00018
0.00024
0.00036
0.00048
0.00060
17.36481
34.72963
52.09445
69.45927
86.82407
104.18890
121.55371
138.91850
156.28336
173.64815
217.06020
260.47226
303.88428
347.29633
390.70834
434.12039
520.94452
694.59259
868.24072
1302.36133
1736.48157
2604.72241
3472.96289
5209.44482
6945.92578
8682.40820
34.20201
68.40401
102.60603
136.80803
171.01004
205.21204
239.41405
273.61609
307.81808
342.02008
427.52512
513.03021
598.53522
684.04016
769.54517
855.05017
1026.06030
1368.08020
1710.10034
9.68365
37.71264
26.04151
21.13331"
19.57903
18.67771
18.07789
16.14324
13.22895
9.45539
7.43008
4.58871
3.30348
1.88862
1.40696
0.82705
0.58559
0.42451
4.10510
3.68074
5.41183
8.30245
6.39872
6.91676
5.92658
13.92644
15.20514
19.01018
27.81129
21.44968
16.65633
14.89861
13.11940
12.07690
9.71089
7.14024
5.25179
3.17776
2.20612
1.07114
0.70314
0.47572
0.33406
0.23940
6.75835
2.85728
3.10267
3.43951
3.34285
2.90392
4.51938
17.65741
25.69429
31.42371
28.42215
15.94647
12.67577
13.71146
11.06869
9.93518
8.04758
5.74839
4.39151
243.80
298.70
304.80
304.80
335.30
341.40
371.90
371.90
371.90
378.00
371.90
371.90
360.00
340.00
360.00
380.00
380.00
400.00
213.40
213.40
213.40
213.40
213.40
225.60
225.60
237.70
243.80
280.40
317.00
304.80
298.70
341.40
371.90
353.60
365.80
353.60
378.00
384.00
389.20
400.00
420.00
380.00
380.00
400.00
213.40
213.40
213.40
219.50
225.60
225.60
243.80
274.30
286.50
298.70
317.00
298.70
298.70
359.70
384.00
378.00
378.00
378.00
378.00
1-HR ALL
1-HR ALL
1-HR ALL
1-HR ALL
1-HR ALL
1-HR ALL
1-HR ALL
1-HR ALL
1-HR ALL
1-HR ALL
1-HR ALL
1-HR ALL
1-HR ALL
1-HR ALL
1-HR ALL
1-HR ALL
1-HR ALL
1-HR ALL
1-HR ALL
1-HR ALL
1-HR ALL
1-HR ALL
1-HR ALL
1-HR ALL
1-HR ALL
1-HR ALL
1-HR ALL
1-HR ALL
1-HR ALL
1-HR ALL
1-HR ALL
1-HR ALL
1-HR ALL
1-HR ALL
1-HR ALL
1-HR ALL
1-HR ALL
1-HR ALL
1-HR ALL
1-HR ALL
1-HR ALL
1-HR* ALL
1-HR ALL
1-HR ALL
1-HR ALL
1-HR ALL
1-HR ALL
1-HR ALL
1-HR ALL t
1-HR ALL
1-HR ALL
1-HR ALL
1-HR ALL
1-HR ALL
1-HR ALL
1-HR ALL
1-HR ALL
1-HR ALL
1-HR ALL
1-HR ALL
1-HR ALL
1-HR ALL
1-HR ALL
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
External Review Draft
Do Not Cite or Quote
-------
V
-7047.69482
-9396.92676
-14095.38960
-18793.85550
-28190.77930
-37587.70700
-46984.63670
•86.60255
-173.20509
-259.80765
-346.41019
-433.01276
-519.61530
-606.21783
-692.82037
-779.42297
-866.02551
-1082.53186
-1299.03833
-1515.54456
-1732.05090
-1948.55725
-2165.06372
-2598.07666
-3464.10181
-4330.12744
-6495.19092
-8660.25488
-12990.38180
-17320.50980
-25980.76370
-34641.01950
-43301 .27340
-76.60445
-153.20891
-229.81335
-306.41782
-383.02228
-459.62671
-536.23120
-612.83563
-689.44006
-766.04449
-957.55566
-1149.06689
-1340.57788
-1532.08899
-1723.60022
-1915.11121
-2298.13354
-3064.17822
-3830.22241
-5745.33350
-7660.44531
-11490.66700
-15320.89060
-22981.33590
-30641.78130
-38302.22660
-64.27877
-128.55756
•192.83632
-257.11511
Volume Vn
Appendix VIJ-4
2565.15063
3420.20093
5130.30078
6840.40186
10260.60250
13680.80370
17101.00390
49.99999
99.99998
149.99997
199.99997 .
249.99994
299.99991
349.99991
399.99991
449.99991
499.99988
624.99988
749.99988
874.99988
999.99982
1125.00000
1249.99976
1499.99976
1999.99963
2499.99951
3749.99951
4999.99854
7499.99854
9999.99805
14999.99800
19999.99610
24999.99610
64.27876
128.55751
192.83626
257.11499
321.39374
385.67255
449.95126
514.22998
578.50873
642.78760
803.48444
964.18121
1124.87830
1285.57507
1446.27173
1606.96887
1928.36255
2571.15015
3213.93750
4820.90576
6427.87451
9641.81250
12855.75000
19283.62500
25711.50000
32139.37700
76.60442
153.20885
229.61332
306.41772
2.87244
1.72744
1JJ4763
0.92909
0.46991
0.34988
0.25169
7.29729
2.66494
1.88088
3.08625
2.50315
3.92369
8.42885
31.76547
32.02022
28.58289
19.71223
21.17135
16.48961
13.68632
12.01355
10.49539
8.51523
6.10111
4.59829
2.79373
1.72431
1.11421
0.78104
0.44347
0.33119
0.50245
6.74444
2.43339
3.34839
2.39780
2.01682
2.16860
14.90388
38.32684
36.18783
32.62605
22.65782
21.43189
17.14719
14.15745
12.20940
10.65245
8.48230
6.46535
4.63533
2.85532
1.98738
1.24561
0.78267
0.47113
0.33153
0.45354
8.48427
8.40527
4.76649
2.18069
371.90
424.90
420.00
" 360.00
400.00
380.00
400.00
213.40
213.40
219.50
231.60
225.60
231.60
266.20
304.80
310.90
304.80
292.60
323.10
359.70
371.90
371.90
378.00
378.00
378.00
384.00
384.00
426.70
400.00
400.00
420.00
400.00
350.00
213.40
213.40
225.60
231.60
225.60
231.60
268.20
304.80
316.40
3t7.00
304.80
341.40
353.60
365.80
371.90
378.00
384.00
359.70
384.00
378.00
379.20
360.00
400.00
400.00
400.00
370.00
213.40
225.60
231.60
231.60
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR.
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL 4
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
External Review Draft
Do Not Cite or Quote
-------
-321.39383
-385.67267
-449.95142
-514.23022
-578.50897
-642.78772
-803.48474
-964.18152
-1124.87854
-1285.57532
-1446.27222
-1606.96936
-1928.36328
-2571.15088
-3213.93872
-4820.90771
-6427.87695
-9641.81543
-12855.75490
-19283.63090
-25711.50980
-32139.38670
-50.00002
-100.00003
-150.00005
-200.00006
-250.00009
-300.00009
-350.00012
-400.00012
-450.00015
-500.00018
-625.00024
-750.00024
-875.00031
-1000.00037
-1125.00037
-1250.00049
-1500.00049
-2000.00073
-2500.00098
-3750.00122
-5000.00195
-7500.00244
-10000.00390
-15000.00490
-20000.00780
-25000.00780
-34.20204
-68.40408
-102.60610
-136.80815
-171.01018
-205.21220
-239.41423
-273.61633
-307.81833
-342.02036
-427.52545
-513.03052
-598.53571
-684.04065
-769.54584
Volume VII
Appendix VII-4
383.02216
459.62665
536.23102
612.83551
689.43988
766.04431
957.55542
1149.06653
1340.57751
1532.08862
1723.59973
1915.11084
2298.13306
3064.17749
3830.22144
5745.33203
7660.44336
11490.66410
15320.88670
22981.33010
30641.77340
38302.21880
86.60253
173.20506
259.80756
346.41013
433.01270
519.61517
606.21771
692.82025
779.42279
866.02533
1082.53162
1299.03784
1515.54431
1732.05066
1948.55701
2165.06323
2598.07593
3464.10132
4330.12646
6495.18994
8660.25293
12990.37990
17320.50590
25980.75980
34641.01170
43301.26170
93.96925
187.93851
281.90778
375.87698
469.84631
563.81555
657.78479
751.75403
845.72327
939.69257
1174.61572
1409.53894
1644.46191
1879.38513
2114.30811
4.08251
12.21246
20.82514
40721757-
34.97815
30.83339
24.27721
23.19573
20.07016
17.05709
14.80667
12.93382
9.78141
6.69608
5.06957
2.92663
1.96190
1.14278
0.76577
0.46537
0.59070
0.51383
8.62542
6.76894
3.82833
8.45730
0.82822
2.55397
2.81276
2.89723
27.36086
24.50089
9.91413
19.44755
19.85781
17.44489
15.06950
12.57573
9.93906
6.77750
5.11994
3.03971
2.00307
1.32361
1.05032
0.72083
0.33429
0.43038
8.87911
10.94706
3.05174
1.86098
0.58779
1.20937
4.06183
14.22526
10.02501
12.97981
22.93865
25.57636
21.21321
16.50457
12.81844
225.60
231.60
274.30
304.80
310.90
310.90
317.00
347.50
353.60
353.60
359.70
365.80
384.00
384.00
378.00
378.00
378.00
380.00
400.00
400.00
360.00
360.00
213.40
225.60
231.60
231.60
225.60
243.80
249.90
243.80
304.80
304.80
286.50
329.20
347.50
353.60
353.60
384.00
384.00
384.00
378.00
365.80
371.90
360.00
360.00
340.00
380.00
350.00
213.40
225.60
225.60
225.60
225.60
243.80
262.10
286.50
280.40
292.60
323.10
353.60
359.70
359.70
329.20
-HR
-MR
-HR
-HR
-HR
-HR
-HR
1-HR
1-HR
1-HR
1-HR
1-HR
-HR
-HR
-HR
-HR
-HR
-HR
-HR
-HR
-HR
-HR
-HR
-HR
-HR
-HR
-HR
-HR
-HR
-HR
-HR
-HR
-HR
-HR
-HR
-HR
-HR
-HR
-HR
-HR
-HR
-HR
-HR
-HR
-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
.ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL 4
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
External Review Draft
Do Not Cite or Quote
-------
-855.05090
-1026.06104
-1368.08130
-1710.10181
-2565.15283
-3420.20337
-5130.30518
-6840.40674
-10260.61040
-13680.81450
-17101.01760
-17.36484
-34.72969
-52.09453
-69.45937
-86.82422
-104.18906
-121.55391
-138.91873
-156.28360
-173.64844
-217.06055
-260.47269
-303.88474
-347.29691
-390.70898
-434.12109
-520.94531
-694.59375
-868.24219
-1302.36353
-1736.48438
-2604.72656
-3472.96875
-5209.45264
-6945.93701
-8682.42188
-0.00003
-0.00006
-0.00009
-0.00012
-0.00015
-0.00018
-0.00021
-0.00024
-0.00027
-0.00030
-0.00038
-0.00045
-0.00053
-0.00060
-0.00068
-0.00075
-0.00091
-0.00121
-0.00151
-0.00226
-0.00302
-0.00453
-0.00604
-0.00906
-0.01208
-0.01510
Volume VII
Appendix VII-4
2349.23145
2819.07764
3758.77026
4698.46289
7047.69385
9396.92578
14095.38770
18793.85350
28190.77540
37587.70310
46984.62890
98.48077
196.96155
295.44235
393.92307
492.40381
590.88470
689.36542
787.84613
886.32697
984.80768
1231.00964
1477.21143
1723.41345
1969.61523
2215.81738
2462.01929
2954.42285
3939.23071
4924.03809
7386.05713
9848.07715
14772.11430
19696.15430
29544.22850
39392.30860
49240.38670
100.00000
200.00000
300.00000
400.00000
500.00000
600.00000
700.00000
800.00000
900.00000
1000.00000
1250.00000
1500.00000
1750.00000
2000.00000
2250.00000
2500.00000
3000.00000
4000.00000
5000.00000
7500.00000
10000.00000
15000.00000
20000.00000
30000.00000
40000.00000
50000.00000
11.72927
10.96301
7.72337
6.0?30i
2.96586
2.36762
1.53541
1.08532
0.60606
0.47564
0.34774
12.20264
12.15792
7.01011
1.00551
2.05384
3.54073
4.76516
14.10182
16.50330
14.94542
27.44732
24.43270
19.61405
21.11319
15.18397
16.30547
12.95497
9.37742
7.28307
3.88370
2.73447
1.68321
1.30668
0.73742
0.57570
0.49303
15.70024
11.35771
2.70458
3.69062
4.05660
4.32104
3.79221
13.82174
28.61089
20.37133
35.25359
24.48816
20.46308
16.81103
18.77208
16.58580
13.33968
9.34522
7.26469
4.45992
3.06368
1.86240
1.36128
0.78080
0.63847
0.54603
347.50
378.00
385.00
-371.90
329.20
349.00
360.00
360.00
340.00
370.00
350.00
213.40
225.60
225.60
225.60
225.60
243.80
262.10
292.60
298.70
298.70
335.30
365.80
359.70
359.70
341.40
378.00
384.00
378.00
365.80
341.40
339.90
340.00
360.00
340.00
330.00
320.00
213.40
225.60
225.60
225.60
225.60
237.70
256.00
280.40
298.70
292.60
353.60
323.10
341.40
317.00
359.70
359.70
378.00
383.40
359.70
371.90
380.10
360.00
340.00
380.00
350.00 1
350.00 1
-MR ALL
-HR ALL
-HR ALL
-HR ALL
-HR ALL
-HR ALL
-HR ALL
-HR ALL
-HR ALL
-HR ALL
-HR ALL
-HR ALL
-HR ALL
-HR ALL
-HR ALL
-HR ALL
-HR ALL
-HR ALL
-HR ALL
-HR ALL
-HR ALL
-HR ALL
-HR ALL
-HR ALL
-HR ALL
-HR ALL
-HR ALL
-HR ALL
-HR ALL
-HR ALL
-HR ALL
-HR ALL
-HR ALL
-HR ALL
-HR ALL
-HR ALL
-HR ALL
-HR ALL
-HR ALL
-HR ALL
-HR ALL
-HR ALL
-HR ALL
-HR ALL
-HR ALL
-HR ALL
-HR ALL
-HR ALL
-HR ALL *
-HR ALL
-HR ALL
-HR ALL
-HR ALL
-HR ALL
-HR ALL
-HR ALL
-HR ALL
-HR ALL
-HR ALL
-HR ALL
-HR ALL
-HR ALL
-HR ALL
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST.
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
External Review Draft
Do Not Cite or Quote
-------
* ISCST2 (94227): UTI Storage Tank Ripture,
* MODELING OPTIONS USED:
* COMC RURAL ELEV
ISCCMDEP " ONSITE ORGANIC TANK FARM
fiRDRIS NOSTD
* PLOT FILE OF PERIOD
* FOR A
* FORMAT
* X
*
17.36482
34.72963
52.09445
69.45927
86.82409
104.18890
121.55373
138.91852
156.28337
173.64818
217.06021
260.47229
303.88428
347.29639
390.70837
434.12042
520.94452
694.59271
868.24084
1302.36133
1736.48169
2604.72241
3472.96313
5209.44531
6945.92627
8682.40820
34.20201
68.40403
102.60603
136.80806
171.01007
205.21207
239.41408
273.61615
307.81812
342.02011
427.52518
513.03021
598.53522
684.04022
769.54523
855.05035
1026.06042
1368.08057
1710.10071
2565.15112
3420.20142
5130.30176
6840.40283
10260.60450
13680.80570
17101.00590
50.00000
100.00000
Volume VH
Appendix VIM
TOTAL OF 93
: (3(1X,F13.5
Y
98.48077
196.96155
295.44235
393.92307
492.40384
590.88470
689.36542
787.84613
886.32697
984.80774
1231.00964
1477.21167
1723.41370
1969.61548
2215.81738
2462.01929
2954.42310
3939.23096
4924.03809
7386.05762
9848.07715
14772.11520
19696.15430
29544.23050
39392.30860
49240.38670
93.96926
187.93851
281.90778
375.87701
469.84631
563.81555
657.78491
751.75409
845.72339
939.69263
1174.61572
1409.53894
1644.46204
1879.38525
2114.30835
2349.23145
2819.07788
3758.77051
4698.46289
7047.69482
9396.92578
14095.38960
18793.85350
28190.77930
37587.70310
46984.63670
86.60254
173.20508
936 RECEPTORS.
(,F8.2,2X,A
CONC
0.02545
0.01694
0.00306
0.00344
0.00391
0.00438
0.01219
0.01832
0.03929
0.04757
0.12532
0.10666
0.06029
0.07316
0.06579
0.05995
0.04539
0.03239
0.02653
0.01414
0.01078
0.00656
0.00456
0.00251
0.00186
0.00136
0.03513
0.03285
0.00772
0.01256
0.00896
0.00535
0.00951
0.01138
0.01675
0.04749
0.11497
0.10945
0.08917
0.07980
0.07215
0.06242
0.05135
0.03571
0.02814
0.01694
0.01174
0.00844
0.00600
0.00306
0.00204
0.00150
0.05057
0.02778
ZELEV
213.40
225.60
225.60
225.60
225.60
225.60
243.80
256.00
280.40
286.50
353.60
353.60
310.90
347.50
353.60
359.70
347.50
341.40
341.40
365.80
360.00
340.00
340.00
360.00
350.00
360.00
213.40
225.60
225.60
225.60
225.60
225.60
237.70
243.80
256.00
286.50
329.20
347.50
335.30
347.50
353.60
359.70
362.40
329.20
359.70
369.70
385.90
340.00
340.00
360.00
380.00
390.00
213.40
219.50
AVE
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
GRP
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
NUN HRS
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
External Review Draft
Do Not Cite or Quote
-------
150.00000
200.00000
250.00000
300.00000
350.00000
400.00000
450.00000
500.00000
625.00000
750.00000
875.00000
1000.00000
1125.00000
1250.00000
1500.00000
2000.00000
2500.00000
3750.00000
5000.00000
7500.00000
10000.00000
15000.00000
20000.00000
25000.00000
64.27876
128.55754
192.83627
257.11508
321.39377
385.67258
449.95132
514.23016
578.50885
642.78766
803.48456
964.18140
1124.87830
1285.57520
1446.27197
1606.96912
1928.36292
2571.15039
3213.93799
4820.90625
6427.87549
9641 .81250
12855.75200
19283.62700
25711.50390
32139.37890
76.60445
153.20888
229.81335
306.41779
383.02225
459.62671
536.23120
612.83557
689.44000
766.04443
957.55554
1149.06665
1340.57764
Volume VII
Appendix VII-4
259.80762
346.41016
433.01273
519.61517
606.21777
692.82031
779.42291
866.02539
1082.53174
1299.03821
1515.54443
1732.05090
1948.55713
2165.06348
2598.07617
3464.10156
4330.12695
6495.19043
8660.25391
12990.38090
17320.50780
25980.76170
34641.01560
43301.26560
76.60445
153.20888
229.81335
306.41779
383.02225
459.62671
536.23120
612.83557
689.44000
766.04443
957.55554
1149.06665
1340.57764
1532.08899
1723.59998
1915.11108
2298.13330
3064.17798
3830.22192
5745.33301
7660.44434
11490.66600
15320.88870
22981.33400
30641.77730
38302.22270
64.27876
128.55754
192.83629
257.11508
321.39377
385.67261
449.95132
514.23016
578.50885
642.78766
803.48456
964.18140
1124.87830
0.04241
0.02802
0.02022
O.TJft67
0.01002
0.01377
0.02142
0.03306
0.01570
0.13254
0.11912
0.09986
0.09015
0.07452
0.06321
0.04596
0.03511
0.02129
0.01400
0.01018
0.00598
0.00343
0.00241
0.00171
0.05370
0.01995
0.19797
0.17097
0.05783
0.03036
0.01963
0.01457
0.01843
0.03922
0.08612
0.17944
0.16109
0.13633
0.12412
0.10984
0.08659
0.06507
0.05013
0.02861
0.01879
0.01150
0.00831
0.00521
0.00310
0.00234
0.03277
0.00000
0.20144
0.22828
0.08641
0.04802
0.03157
0.02336
0.03823
0.02691
0.03639
0.32847
0.30432
225.60
225.60
225.60
-225.60
225.60
231.60
243.80
262.10
225.60
347.50
359.70
353.60
353.60
329.20
323.10
361.20
366.70
378.00
396.20
320.00
360.00
380.00
370.00
400.00
213.40
213.40
225.60
225.60
225.60
225.60
225.60
225.60
225.60
243.80
280.40
353.60
361.50
353.60
353.60
353.60
335.30
353.90
353.00
378.00
398.40
376.00
380.00
360.00
420.00
420.00
213.40
207.30
213.40
219.50
219.50
219.50
219.50
219.50
225.60
219.50
219.50
323.10
353.60
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL ;
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL .
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
External Review Draft
Do Not Cite or Quote
-------
1532.08899
1723.59998
1915.11108
2298.13330
3064.17798
3830.22192
5745.33301
7660.44434
11490.66600
15320.88870
22981.33400
30641 .77730
38302.22270
86.60254
173.20508
259.80762
346.41016
433.01273
519.61517
606.21777
692.82031
779.42291
866.02539
1082.53174
1299.03821
1515.54443
1732.05090
1948.55725
2165.06348
2598.07617
3464.10156
4330.12695
6495.19043
8660.25391
12990.38090
17320.50780
25980.76170
34641.01560
43301.26560
93.96926
- 187.93851
281.90778
375.87701
469.84631
563.81555
657.78491
751.75409
845.72333
939.69263
1174.61572
1409.53894
1644.46204
1879.38525
2114.30835
2349.23145
2819.07788
3758.77051
4698.46289
7047.69482
9396.92578
14095.38960
18793.85350
28190.77930
Volume VH
Appendix VII-4
1285.57520
1446.27197
1606.96912
1928.36292
2571.15039
3213.93799
4820.90674
6427.87549
9641.81348
12855. 75200
19283.62700
25711.50390
32139.38090
50.00000
^V.Tyryy
150.00000
199.99997
249.99997
300.00000
349.99994
399.99994
449.99994
499.99994
625.00000
750.00000
875.00000
1000.00000
1125.00000
1250.00000
1500.00000
2000.00000
2499.99976
3749.99976
4999.99902
7499.99902
9999.99902
14999.99900
19999.99800
24999.99800
34.20201
68.40403
102.60603
136.80806
171.01007
205.21207
239.41411
273.61615
307.81815
342.02011
427.52518
513.03021
596.53528
684.04022
769.54535
855.05035
1026.06042
1368.08057
1710.10071
2565.15112
3420.20142
5130.30176
6840.40283
10260.60450
0.26639
0.22985
0.20481
0.7&37
0.11599
0.08966
0.04832
0.03265
0.02060
0.01307
0.00770
0.00492
0.00370
0.02886
0.00000
0.40564
0.11439
0.11840
0.12144
0.07655
0.05486
0.05410
0.07719
0.11710
0.08957
0.19280
0.32995
0.33746
0.31120
0.24750
0.17578
0.12641
0.07047
0.04496
0.02709
0.01922
0.01059
0.00726
0.00499
0.00580
0.00000
0.03026
0.05300
0.06818
0.05043
0.03915
0.05184
0.05533
0.05587
0.07287
0.08321
0.08773
0.08926
0.08794
0.14988
0.13186
0.18034
0.12153
0.07017
0.04957
0.02924
0.01897
0.01054
353.60
335.30
347.50
-357.50
341.40
335.30
373.10
396.20
360.00
380.00
380.00
420.00
420.00
213.40
207.30
207.30
201.20
207.30
213.40
213.40
213.40
213.40
219.50
225.60
219.50
243.80
292.60
310.90
323.10
317.00
323.10
359.70
378.90
408.70
380.00
360.00
380.00
380.00
420.00
207.30
201.20
202.70
202.70
207.30
207.30
207.30
213.40
213.40
213.40
213.40
213.40
213.40
213.40
213.40
231.60
231.60
310.90
384.00
384.00
370.30
360.00
380.00
400.00
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL 4.
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
External Review Draft
Do Not Cite or Quote
-------
37587.70310
46984.63670
98.48077
196.96155
295.44235
393.92307
492.40384
590.88470
689.36542
787.84613
, 886.32697
984.80774
1231.00964
1477.21167
1723.41370
1969.61548
2215.81738
2462.01929
2954.42310
3939.23096
4924.03809
7386.05762
9848.07715
14772.11520
19696.15430
29544.23050
39392.30860
49240.38670
100.00000
200.00000
300.00000
400.00000
500.00000
600.00000
700.00000
800.00000
900.00000
1000.00000
1250.00000
1500.00000
1750.00000
2000.00000
2250.00000
2500.00000
3000.00000
4000.00000
5000.00000
7500.00000
10000.00000
15000.00000
20000.00000
30000.00000
40000.00000
50000.00000
98.48077
196.96155
295.44235
393.92307
492.40384
590.88470
689.36542
787.84613
886.32697
Volume VH
Appendix VII-4
13680.80570
17101.00780
17.36482
34.72964
52.09447
69.45930
86.82410
104.18893
121.55376
138.91856
156.28340
173.64821
217.06027
260.47235
303.88434
347.29648
390.70850
434.12051
520.94470
694.59296
868.24103
1302.36169
1736.48218
2604.72290
3472.96411
5209.44580
6945.92822
8682.41113
0.00001
0.00002
0.00002
0.00003
0.00004
0.00005
0.00005
0.00006
0.00007
0.00008
0.00009
0.00011
0.00013
0.00015
0.00017
0.00019
0.00023
0.00030
0.00038
0.00057
0.00075
0.00113
0.00151
0.00226
0.00302
0.00377
-17.36482
-34.72964
-52.09446
-69.45927
-86.82410
-104.18891
-121.55373
-138.91853
-156.28339
0.00804
0.00541
0.00193
0.00743"
0.02575
0.01364
0.00662
0.00554
0.00482
0.00449
0.00604
0.00687
0.01209
0.01715
0.03400
0.02922
0.03127
0.07780
0.20499
0.16610
0.12215
0.06699
0.04665
0.03223
0.01940
0.01084
0.00747
0.00536
0.00169
0.00582
0.00530
0.01446
0.00697
0.00373
0.00276
0.00284
0.00357
0.00524
0.07934
0.46378
0.36300
0.34013
0.23964
0.18899
0.19649
0.15428
0.10985
0.07560
0.04574
0.02821
0.01931
0.01072
0.00692
0.00603
0.00243
0.00382
0.00167
0.00373
0.00591
0.00500
0.00446
0.01769
0.02819
360.00
400.00
207.30
•202.70
202.70
202.70
202.70
202.70
202.70
202.70
202.70
202.70
202.70
202.70
213.40
207.30
207.30
231.60
304.80
346.60
365.80
384.00
371.90
320.00
360.00
380.00
380.00
400.00
207.30
202.70
202.70
202.70
202.70
202.70
202.70
202.70
202.70
202.70
243.80
341.40
323.10
341.40
304.80
292.60
310.90
359.70
402.30
347.50
380.10
360.00
360.00
380.00
400.00
360.00
207.30
202.70
202.70
202.70
202.70
202.70
202.70
219.50
225.60
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD.
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PER IX
PERIX
PERIOD
PERIX
PERIX
PERIX
PERIX
PERIX
PERIX
PERIX
PERIX
PERIX
PERIX
PERIX
PERIX
PERIX
PERIX
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL 4
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
External Review Draft
Do Not Cite or Quote
-------
984.80774
1231.00964
1477.21167
1723.41370
1969.61548
2215.81738
2462.01929
2954.42310
3939.23096
4924.03809
7386.05762
9848.07715
14772.11520
19696.15430
29544.23050
39392.30860
49240.38670
93.96926
187.93851
281 .90778
375.87701
469.84631
563.81555
657.78491
751.75409
845.72339
939.69263
1174.61584
1409.53894
1644.46216
1879.38525
2114.30835
2349.23145
2819.07788
3758.77051
4698.46338
7047.69482
9396.92676
14095.38960
18793.85550
28190.77930
37587.70700
46984.63670
86.60254
173.20508
259.80762
346.41016
433.01273
519.61517
606.21777
692.82031
779.42291
866.02539
1082.53174
1299.03821
1515.54443
1732.05090
1948.55713
2165.06348
2598.07617
3464.10156
4330.12695
6495.19043
Volume VH
-173.64819
-217.06023
-260.47232
-303.88431
-347.29642
-390.70840
-434.12045
-520.94458
-694.59277
-868.24091
-1302.36145
-1736.48181
-2604.72290
-3472.96338
-5209.44580
-6945.92676
-8682.40918
-34.20201
-68.40402
-102.60603
-136.80804
-171.01006
-205.21207
-239.41406
-273.61612
-307.81812
-342.02008
-427.52515
-513.03021
-598.53522
-684.04016
-769.54523
-855.05023
-1026.06030
-1368.08032
-1710.10059
-2565.15088
-3420.20093
-5130.30127
-6840.40334
-10260.60350
-13680.80470
-17101.00590
-50.00000
-100.00001
-150.00002
-200.00002
-250.00003
-300.00003
-350.00003
-400.00003
-450.00003
-500.00006
•625.00006
-750.00006
-875.00006
-1000.00012
-1125.00012
-1250.00012
-1500.00012
-2000.00024
-2500.00024
-3750.00049
0.50831
0.47633
0.42052
0.307~15~
0.30709
0.27303
0.22877
0.21500
0.15596
0.11311
0.07546
0.05095
0.03242
0.01888
0.01095
0.00776
0.00552
0.00314
0.00304
0.00199
0.00096
0.00161
0.00595
0.06812
0.22038
0.16963
0.34941
0.35778
0.31240
0.21257
0.25030
0.21184
0.19760
0.16270
0.12625
0.09872
0.05979
0.03998
0.02457
0.01808
0.01076
0.00770
0.00579
0.00376
0.00257
0.00284
0.00067
0.00180
0.04448
0.25351
0.37065
0.34719
0.28853
0.16991
0.21772
0.17343
0.16451
0.15628
0.13258
0.11563
0.08652
0.07382
0.04321
329.20
347.50
353.60
323.10
341.40
341.40
323.10
347.50
353.60
386.50
353.60
360.00
340.00
380.00
380.00
380.00
400.00
207.30
202.70
202.70
202.70
202.70
213.40
256.00
298.70
286.50
323.10
347.50
347.50
310.90
353.60
350.20
347.50
347.50
345.90
371.90
365.80
408.40
380.00
360.00
360.00
360.00
360.00
207.30
202.70
202.70
202.70
213.40
268.20
317.00
347.50
353.60
347.50
310.90
359.70
335.30
359.70
359.70
347.50
365.80
359.70
353.60
402.30
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL t
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
876P
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
Appendix VII-4
External Review Draft
Do Not Cite or Quote
-------
8660.25391 -5000.00049
12990.38090 -7500.00098
17320.50780 -10000.00100
25980.76170 -15000.00200
34641.01560 -20000.00200
43301 .26560 -25000 .00200
76.60445 -64.27876
153.20888 -128.55754
229.81332 -192.83629
306.41779 -257.11508
383.02225 -321.39377
459.62668 -385.67261
536.23108 -449.95132
612.83557 -514.23016
689.44000 -578.50885
766.04443 -642.78766
957.55554 -803.48462
1149.06665 -964.18146
1340.57764 -1124.87830
1532.08899 -1285.57520
1723.59998 -1446.27209
1915.11108 -1606.96924
2298.13330 -1928.36292
3064.17798 -2571.15039
3830.22192 -3213.93823
5745.33252 -4820.90674
7660.44434 -6427.87598
11490.66500 -9641.81348
15320.88870 -12855.75290
22981.33200 -19283.62700
30641.77730 -25711.50590
38302.22270 -32139.38090
64.27876 -76.60445
128.55754 -153.20888
192.83629 -229.81332
257.11508 -306.41779
321.39377 -383.02225
385.67261 -459.62668
449.95132 -536.23108
514.23016 -612.83557
578.50885 -689.44000
642.78766 -766.04443
803.48456 -957.55554
964.18146 -1149.06665
1124.87830 -1340.57764
1285.57520 -1532.08899
1446.27197 -1723.59996
1606.96912 -1915.11108
1928.36292 -2298.13330
2571.15039 -3064.17798
3213.93799 -3830.22192
4820.90674 -5745.33301
6427.87549 -7660.44434
9641.81348 -11490.66600
12855.75200 -15320.88870
19283.62700 -22981.33400
25711.50390 -30641.77730
32139.38090 -38302.22270
50.00000 -86.60254
100.00001 -173.20508
150.00002 -259.80762
200.00002 -346.41016
250.00002 -433.01273
Volume VII
Appendix V1I-4
0.03182 396.20 PERIOD ALL
0.01965 380.00 PERIOD ALL
0.01359 380.00 PERIOD ALL
0.0l>854~ 360.00 PERIOD ALL
0.00593 360.00 PERIOD ALL
0.00458 360.00 PERIOD ALL
0.00298 207.30 PERIOD ALL
0.00244 202.70 PERIOD ALL
0.00236 202.70 PERIOD ALL
0.00132 202.70 PERIOD ALL
0.01719 243.80 PERIOD ALL
0.15052 298.70 PERIOD ALL
0.22776 323.10 PERIOD ALL
0.25667 353.60 PERIOD ALL
0.25865 353.60 PERIOD ALL
0.24048 353.60 PERIOD ALL
0.18747 353.60 PERIOD ALL
0.17190 359.70 PERIOD ALL
0.14936 341.40 PERIOD ALL
0.14194 353.60 PERIOD ALL
0.12229 353.60 PERIOD ALL
0.10734 341.40 PERIOD ALL
0.09631 359.70 PERIOD ALL
0.07056 359.70 PERIOD ALL
0.05354 359.70 PERIOD ALL
0.03138 408.40 PERIOD ALL
0.02315 408.40 PERIOD ALL
0.01464 380.00 PERIOD ALL
0.01039 360.00 PERIOD ALL
0.00621 360.00 PERIOD ALL
0.00434 360.00 PERIOD ALL
0.00338 360.00 PERIOD ALL
0.00213 207.30 PERIOD ALL
0.00317 202.70 PERIOD ALL
0.00141 202.70 PERIOD ALL
0.00202 202.70 PERIOD ALL
0.05483 268.20 PERIOD ALL
0.16639 304.80 PERIOD ALL
0.16340 310.90 PERIOD ALL
0.17782 323.10 PERIOD ALL
0.18673 329.20 PERIOD ALL
0.14656 323.10 PERIOD ALL
0.17364 347.50 PERIOD ALL
0.14824 359.70 PERIOD ALL
0.10904 329.20 PERIOD ALL
0.10885 359.70 PERIOD ALL
0.09206 353.60 PERIOD ALL
0.09084 359.70 PERIOD ALL
0.07773 408.40 PERIOD ALL *
0.05626 420.60 PERIOD ALL
0.04241 371.90 PERIOD ALL
0.02668 392.00 PERIOD ALL
0.01965 390.10 PERIOD ALL
0.01385 340.00 PERIOD ALL
0.00843 380.00 PERIOD ALL
0.00466 400.00 PERIOD ALL
0.00322 400.00 PERIOD ALL
0.00273 380.00 PERIOD ALL
0.00146 207.30 PERIOD ALL
0.00415 202.70 PERIOD ALL
0.00138 202.70 PERIOD ALL
0.00336 213.40 PERIOD ALL
0.06463 268.20 PERIOD ALL
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
External Review Draft
Do Not Cite or Quote
-------
300.00003
350.00003
400.00003
450.00003
500.00003
625.00006
750.00006
875.00006
1000.00006
1125.00012
1250.00012
1500.00012
2000.00012
2500.00024
3750.00024
5000.00049
7500.00049
10000.00100
15000.00100
20000.00200
25000.00200
34.20202
68.40405
102.60606
136.80809
171.01012
205.21213
239.41414
273.61621
307.81821
342.02023
427.52527
513.03033
598.53546
684.04047
769.54547
855.05054
1026.06079
1368.08081
1710.10107
2565.15161
3420.20190
5130.30273
6840.40430
10260.60550
13680.80860
17101.01170
17.36483
34.72966
52.09449
69.45933
86.82413
104.18897
121.55380
138.91862
156.28346
173.64827
217.06036
260.47244
303.88449
347.29657
390.70868
434.12073
Volume VB
Appendix VII-4
-519.61517
-606.21777
-692.82031
-779.42291
-866.02539
-1082.53174
-1299.03821
-1515.54443
-1732.05090
-1948.55713
-2165.06348
-2598.07617
-3464.10156
-4330.12695
-6495.19043
-8660.25391
-12990.38090
-17320.50780
-25980.76170
-34641.01560
-43301.26560
-93.96926
-187.93851
-281.90778
-375.87701
-469.84631
-563.81555
-657.78479
-751.75409
-845.72333
-939.69257
-1174.61572
-1409.53894
-1644.46204
-1879.38513
-2114.30835
-2349.23145
-2819.07788
-3758.77026
-4698.46289
-7047.69434
-9396.92578
-14095.38870
-18793.85350
-28190.77730
-37587.70310
-46984.62890
-98.48077
-196.96155
-295.44235
-393.92307
-492.40384
-590.88470
•689.36542
-787.84613
-886.32697
-984.80774
-1231.00964
-1477.21143
-1723.41370
-1969.61548
-2215.81738
-2462.01929
0.16885
0.18694
0.19630
07!6994~
0.17670
0.08516
0.12500
0.10542
0.09865
0.08375
0.07867
0.06686
0.04844
0.03532
0.02278
0.01717
0.01213
0.00807
0.00401
0.00295
0.00232
0.00103
0.00361
0.00197
0.00218
0.06860
0.15540
0.18843
0.17923
0.08465
0.08048
0.11051
0.10331
0.07953
0.09491
0.08882
0.08416
0.06637
0.04711
0.03580
0.02268
0.01634
0.01084
0.00729
0.00368
0.00270
0.00200
0.00083
0.00177
0.00313
0.00203
0.04530
0.17778
0.10333
0.08049
0.10732
0.09488
0.10856
0.10526
0.09116
0.07445
0.07088
0.09381
298.70
310.90
323.10
323.10
329.20
298.70
341.40
341.40
359.70
365.80
371.90
408.40
420.60
408.40
408.40
396.20
340.00
360.00
420.00
400.00
400.00
207.30
202.70
202.70
207.30
268.20
292.60
304.80
304.80
286.50
286.50
304.80
310.90
304.80
335.30
359.70
378.00
396.20
402.30
411.50
402.30
408.10
360.00
360.00
420.00
400.00
420.00
207.30
202.70
202.70
202.70
249.90
286.50
280.40
274.30
286.50
286.50
298.70
304.80
304.80
298.70
298.70
365.80
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL 4
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
External Review Draft
Do Not Cite or Quote
-------
520.94489
694.S9320
868.24146
1302.36230
1736.48279
2604.72412
3472.96558
5209.44824
6945.93115
8682.41504
0.00002
0.00003
0.00005
0.00006
0.00008
0.00009
0.00011
0.00012
0.00014
0.00015
0.00019
0.00023
0.00026
0.00030
0.00034
0.00038
0.00045
0.00060
0.00075
0.00113
0.00151
0.00226
0.00302
0.00453
0.00604
0.00755
-17.36482
-34.72964
-52.09447
-69.45930
-86.82410
-104.18893
-121.55376
-138.91856
-156.28340
-173.64821
-217.06029
-260.47238
-303.88437
-347.29648
-390.70853
-434.12054
-520.94470
-694.59296
-868.24115
-1302.36182
-1736.48218
-2604.72314
-3472.96436
-5209.44629
-6945.92871
-8682.41113
-34.20201
Volume VII
Appendix VII-4
-2954.42285
-3939.23096
-4924.03809
-7386.05762
-9848.07715
-14772.11520
-19696.15430
-29544.23050
-39392.30860
-49240.38670
-100.00000 .
-200.00000
-300.00000
-400.00000
-500.00000
-600.00000
-700.00000
-800.00000
-900.00000
-1000.00000
-1250.00000
-1500.00000
-1750.00000
-2000.00000
-2250.00000
-2500.00000
-3000.00000
-4000.00000
-5000.00000
-7500.00000
-10000.00000
-15000.00000
-20000.00000
-30000.00000
-40000.00000
-50000.00000
-98.48077
-196.96155
-295.44235
-393.92307
-492.40384
-590.88470
-689.36542
-787.84613
-886.32697
-984.80774
-1231.00964
-1477.21167
-1723.41370
-1969.61548
-2215.81738
-2462.01929
-2954.42310
-3939.23096
-4924.03809
-7386.05762
-9848.07715
-14772.11520
-19696.15430
-29544.23050
-39392.30860
-49240.38670
-93.96926
0.07467
0.05239
0.03825
0.02312"
0.01769
0.01124
0.00804
0.00419
0.00297
0.00231
0.00087
0.00104
0.00198
0.00281
0.01558
0.17205
0.18625
0.11796
0.04582
0.18976
0.17140
0.13440
0.11465
0.07858
0.07567
0.09419
0.07330
0.05339
0.04182
0.02512
0.01794
0.01092
0.00809
0.00457
0.00320
0.00235
0.00118
0.00059
0.00114
0.00154
0.00246
0.02774
0.17269
0.15942
0.06227
0.19837
0.19489
0.13243
0.12700
0.09338
0.11507
0.11750
0.09531
0.06324
0.04728
0.02927
0.01987
0.01281
0.00967
0.00600
0.00382
0.00271
0.00405
402.30
390.10
414.50
408.40
398.10
380.00
360.00
400.00
400.00
400.00
207.30
202.70
202.70
202.70
219.50
274.30
280.40
274.30
243.80
298.70
304.80
304.80
304.80
292.60
298.70
365.80
406.30
402.30
396.20
390.10
396.20
380.00
360.00
380.00
380.00
400.00
207.30
202.70
202.70
202.70
202.70
225.60
274.30
274.30
237.70
292.60
304.80
286.50
292.60
280.40
304.80
353.60
384.00
396.20
415.40
390.10
392.00
360.00
340.00
340.00
360.00
380.00
213.40
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL.*
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
External Review Draft
Do Not Cite or Quote
-------
-68.40403
-102.60605
-136.80806
-171.01009
-205.21210
-239.41411
-273.61615
-307.81815
-342.02014
-427.52521
-513.03021
-598.53528
-684.04034
-769.54535
-855.05042
-1026.06042
-1368.08069
-1710.10083
-2565.15112
-3420.20142
-5130.30176
-6840.40332
-10260.60450
-13680.80660
-17101.00780
-50.00000
-100.00000
-150.00000
-200.00000
-250.00000
-300.00000
-350.00000
-400.00000
-450.00000
-500.00000
-625.00000
-750.00000
-875.00000
-1000.00000
-1125.00000
- -1250.00000
-1500.00000
-2000.00000
-2500.00000
-3750.00000
-5000.00000
-7500.00000
-10000.00000
•15000.00000
-20000.00000
-25000.00000
-64.27876
-128.55753
-192.83627
-257.11505
-321.39377
-385.67258
-449.95129
-514.23010
-578.50873
-642.78766
-803.48456
-964.18134
Volume Vn
Appendix VII-4
-187.93851
-281 .90778
-375.87701
-469.84631
-563.81555
-657.78491
-751.75409
-845.72333
-939.69263
-1174.61572
-1409.53894
-1644.46204
-1879.38525
-2114.30835
-2349.23145
-2819.07788
-3758.77051
-4698.46289
-7047.69482
-9396.92578
-14095.38960
-18793.85350
-28190.77930
-37587.70310
-46984.62890
-86.60254
-173.20508
-259.80762
-346.41016
-433.01273
-519.61517
-606.21777
-692.82031
-779.42291
-866.02539
-1082.53174
-1299.03821
-1515.54443
-1732.05090
-1948.55713
-2165.06348
•2598.07617
-3464.10156
-4330.12695
-6495.19043
-8660.25391
-12990.38090
-17320.50780
-25980.76170
-34641.01560
-43301.26560
-76.60445
•153.20888
•229.81335
-306.41779
•383.02228
-459.62671
-536.23120
-612.83557
-689.44000
-766.04449
-957.55560
-1149.06689
0.00053
0.00068
0.00107
O.WTCf
0.00240
0.01358
0.06265
0.01412
0.15044
0.12900
0.11789
0.10788
0.06898
0.11563
0.12673
0.09653
0.06549
0.04989
0.03163
0.02203
0.01495
0.01061
0.00595
0.00402
0.00304
0.00332
0.00077
0.00075
0.00098
0.00137
0.00190
0.00250
0.00312
0.00371
0.01135
0.01294
0.01012
0.01064
0.02554
0.02533
0.08815
0.09415
0.05987
0.04525
0.02896
0.01972
0.01264
0.00840
0.00571
0.00408
0.00289
0.00360
0.00091
0.00124
0.00148
0.00166
0.00198
0.00246
0.00300
0.00355
0.00410
0.00533
0.01016
202.70
202.70
202.70
-282.70
202.70
219.50
249.90
219.50
280.40
280.40
280.40
280.40
262.10
298.70
353.60
371.90
402.30
397.20
384.00
384.00
340.00
340.00
360.00
380.00
380.00
213.40
202.70
202.70
202.70
202.70
202.70
202.70
202.70
202.70
219.50
219.50
213.40
213.40
231.60
231.60
292.60
359.70
396.20
414.50
396.20
392.60
360.00
380.00
360.00
360.00
380.00
213.40
202.70
202.70
202.70
202.70
202.70
202.70
202.70
202.70
202.70
202.70
213.40
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
.ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
External Review Draft
Do Not Cite or Quote
-------
-1124.87830
-1285.57520
-106.27185
-1606.96912
-192B.36279
-2571.15039
-3213.93774
-4820.90625
•6427.87500
-9641.81250
02855.75100
-19283.62700
-25711.50200
-32139.37890
-76.60445
-153.20891
-229.81339
-306.41782
-383.02231
-459.62674
-536.23120
-612.83563
-689.44006
-766.04456
-957.55566
-1149.06689
-1340.57800
-1532.08911
-1723.60022
-1915.11121
-2298.13354
-3064.17847
-3830.22241
-5745.33350
-7660.44531
-11490.66700
-15320.89060
-22981.33590
-30641.78130
-38302.22660
-86.60255
-173.20509
-259.80765
-346.41019
-433.01276
-519.61530
-606.21783
-692.82037
-779.42297
-866.02551
-1082.53186
-1299.03833
-1515.54456
-1732.05090
-1948.55725
-2165.06372
-2598.07666
-3464.10181
-4330.12744
-6495.19092
-8660.25488
-12990.38180
-17320.50980
Volume Vn
Appendix Vn-4
-1340.57788
-1532.08899
-1723.60010
-1915.11121
-2298.13354
-3064.17822
-3830.22241
-5745.33301
-7660.44482
-11490.66600
-15320.88960
-22981.33400
-30641.77930
-38302.22270
-64.27876
-128.55751
-192.83624
-257.11499
-321.39371
-385.67252
-449.95123
-514.22998
-578.50867
-642.78754
-803.48444
-964.18115
-1124.87830
-1285.57483
-1446.27173
-1606.96887
-1928.36243
-2571.15015
-3213.93750
-4820.90576
-6427.87451
-9641.81250
-12855.75000
-19283.62500
-25711.50000
-32139.37700
-49.99999
™VV« i^T^^S
-149.99997
-199.99994
-249.99994
-299.99991
-349.99991
.TOO nnoftft
JTT«TTTOO
-449.99988
-499.99988
-624.99988
-749.99988
•874.99982
-999.99982
•1124.99976
-1249.99976
-1499.99976
•1999.99963
•2499.99951
-3749.99927
-4999.99854
-7499.99805
-9999.99805
0.01068
0.01124
0.01160
070T184
0.09079
0.06630
0.04908
0.02961
0.02185
0.01394
0.01000
0.00612
0.00415
0.00337
0.00669
0.00114
0.00170
0.00193
0.00170
0.00233
0.00302
0.00375
0.00528
0.00610
0.00791
0.00913
0.00991
0.01270
0.01312
0.05205
0.11794
0.08564
0.06276
0.03914
0.02796
0.01811
0.01210
0.00714
0.00509
0.00409
0.00580
0.00485
0.00487
0.00327
0.00598
0.00698
0.00811
0.00935
0.01057
0.01174
0.02671
0.10938
0.22403
0.17668
0.11064
0.06566
0.05516
0.09257
0.07103
0.04369
0.02961
0.01982
0.01346
213.40
213.40
213.40
= 213.40
371.90
378.00
396.20
396.20
378.00
349.00
360.00
360.00
380.00
360.00
213.40
201.20
207.50
207.30
202.70
202.70
202.70
202.70
207.30
207.30
207.30
207.30
207.30
213.40
213.40
256.00
323.10
359.70
384.00
378.00
378.00
360.00
380.00
400.00
400.00
380.00
213.40
213.40
213.40
207.30
213.40
213.40
213.40
213.40
213.40
213.40
225.60
274.30
329.20
310.90
286.50
256.00
243.80
365.80
372.50
378.00
402.30
360.00
380.00
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL ,
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
External Review Draft
Do Not Cite or Quote
-------
-25980.76370
-34641.01950
-43301.27340
-93.96926
-187.93851
-281.90778
1 -375.87701
-469.84631
-563.81561
-657.78491
. -751.75409
-845.72339
-939.69263
-1174.61584
-1409.53894
-1644.46216
-1879.38525
-2114.30835
-2349.23145
-2819.07788
-3758.77051
-4698.46338
-7047.69482
-9396.92676
-14095.38960
-18793.85550
-28190.77930
-37587.70700
-46984.63670
-98.48077
-196.96155
-295.44235
-393.92307
-492.40384
-590.88470
-689.36542
-787.84613
-886.32697
-984.80774
-1231.00964
-1477.21167
-1723.41370
-1969.61548
-2215.81738
-2462.01929
-2954.42310
-3939.23096
-4924.03809
-7386.05762
-9848.07715
-14772.11520
-19696.15430
-29544.23050
-39392.30860
-49240.38670
-100.00000
-200.00000
-300.00000
-400.00000
-500.00000
-600.00000
-700.00000
-800.00000
Volume VH
Appendix VII-4
-14999.99710
-19999.99610
-24999.99410
-34.20201
-68.40401
-102.60602
-136.80803
-171.01004
-205.21204
•239.41403
-273.61609
-307.81805
-342.02008
-427.52509
-513.03009
-598.53516
-684.04016
-769.54517
-855.05017
-1026.06030
-1368.08020
-1710.10022
-2565.15039
-3420.20044
-5130.30029
-6840.40137
-10260.60160
-13680.80270
-17101.00390
-17.36481
-34.72963
-52.09444
-69.45926
-86.82407
-104.18888
-121.55370
-138.91849
-156.28334
-173.64813
-217.06018
-260.47223
-303.88422
-347.29630
-390.70831
-434.12033
-520.94446
-694.59253
-868.24066
-1302.36096
-1736.48120
-2604.72192
-3472.96240
-5209.44385
-6945.92480
-8682.40625
0.00000
0.00000
0.00000
0.00000
0.00001
0.00001
0.00001
0.00001
0.00825
0.00559
0.00485
0:0003^
0.00487
0.00588
0.00674
0.00736
0.00828
0.00887
0.01496
0.01582
0.01163
0.32258
0.27203
0.22919
0.19988
0.17693 .
0.13400
0.04582
0.08150
0.07170
0.04415
0.03755
0.02407
0.01633
0.01048
0.00711
0.00591
0.00733
0.00372
0.00279
0.00337
0.00418
0.00527
0.00651
0.01012
0.01528
0.30117
0.34705
0.28299
0.24353
0.21066
0.18152
0.16176
0.13480
0.09856
0.07708
0.04648
0.03583
0.02213
0.01545
0.00866
0.00660
0.00516
0.00535
0.00322
0.00345
0.00397
0.00457
0.00514
0.00620
0.00725
380.00
400.00
360.00
213.40
213.40
213.40
213.40
213.40
213.40
213.40
219.50
219.50
213.40
353.60
353.60
341.40
335.30
353.60
304.80
243.80
298.70
359.70
365.80
402.30
380.00
400.00
380.00
400.00
360.00
213.40
213.40
213.40
213.40
213.40
213.40
213.40
219.50
225.60
310.90
359.70
359.70
365.80
371.90
353.60
371.90
353.60
365.80
365.80
390.10
339.90
360.00
380.00
420.00
400.00
400.00
213.40
213.40
213.40
213.40
213.40
213.40
213.40
213.40
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL,
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
External Review Draft
Do Not Cite or Quote
-------
-900.00000
•1000.00000
-1250.00000
-1500.00000
-1750.00000
-2000.00000
-2250.00000
-2500.00000
-3000.00000
-4000.00000
-5000.00000
-7500.00000
-10000.00000
-15000.00000
-20000.00000
-30000.00000
-40000.00000
-50000.00000
-98.48077
-196.96155
-295.44235
-393.92307
-492.40384
-590.88470
-689.36542
-787.84613
-886.32697
-984.80774
-1231.00964
-1477.21167
-1723.41370
-1969.61548
-2215.81738
-2462.01929
-2954.42310
-3939.23096
-4924.03809
-7386.05762
-9848.07715
-14772.11520
-19696.15430
-29544.23050
-39392.30860
-49240.38670
-93.96926
-187.93851
-281 .90778
-375.87701
-469.84631
-563.81561
-657.78491
-751.75409
-845.72339
-939.69263
-1174.61584
-1409.53894
-1644.46216
•1879.38525
-2114.30835
-2349.23145
-2819.07788
-3758.77051
-4698.46338
Volume Vn
Appendix VII-4
0.00001
0.00001
0.00001
0.00002
0.00002
0.00002
0.00003
0.00003
0.00004
0.00005
0.00006
0.00009
0.00012
0.00016
0.00024
0.00036
0.00048
0.00060
17.36481
34.72963
52.09445
69.45927
86.82407
104.18890
121.55371
138.91850
156.28336
173.64815
217.06020
260.47226
303.88428
347.29633
390.70834
434.12039
520.94452
694.59259
868.24072
1302.36133
1736.48157
2604.72241
3472.96289
5209.44482
6945.92578
8662.40820
34.20201
68.40401
102.60603
136.80803
171.01004
205.21204
239.41405
273.61609
307.81808
342.02008
427.52512
513.03021
598.53522
684.04016
769.54517
855.05017
1026.06030
1368.08020
1710.10034
0.03138
0.18154
0.16779
OflttSD
0.19326
0.17292
0.15736
0.14296
0.11785
0.08221
0.06486
0.04058
0.02916
0.01863
0.01288
0.00776
0.00551
0.00407
0.00503
0.00411
0.00324
0.00328
0.00320
0.00612
0.00704
0.01990
0.02121
0.05904
0.12692
0.08826
0.07458
0.09758
0.09362
0.08325
0.06789
0.05231
0.03879
0.02591
0.01857
0.01065
0.00728
0.00488
0.00357
0.00259
0.00707
0.00379
0.00220
0.00243
0.00335
0.00319
0.01324
0.04530
0.06577
0.08734
0.10862
0.06421
0.05717
0.08890
0.08513
0.07500
0.06389
0.04667
0.03903
243.80
298.70
304.80
* 384.80
335.30
341.40
371.90
371.90
371.90
378.00
371.90
371.90
360.00
340.00
360.00
380.00
380.00
400.00
213.40
213.40
213.40
213.40
213.40
225.60
225.60
237.70
243.80
280.40
317.00
304.80
298.70
341.40
371.90
353.60
365.80
353.60
378.00
384.00
389.20
400.00
420.00
380.00
380.00
400.00
213.40
213.40
213.40
219.50
225.60
225.60
243.80
274.30
286.50
298.70
317.00
298.70
298.70
359.70
384.00
378.00
378.00
378.00
378.00
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL,
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760*
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
External Review Draft
Do Not Cite or Quote
-------
-7047.69482
-9396.92676
-14095.38960
-18793.85550
-28190.77930
-37587.70700
-46984.63670
-86.60255
-173.20509
-259.80765
-346.41019
-433.01276
-519.61530
-606.21783
-692.82037
-779.42297
-866.02551
-1082.53186
-1299.03833
-1515.54456
-1732.05090
-1948.55725
-2165.06372
-2598.07666
-3464.10181
-4330.12744
-6495.19092
-8660.25488
-12990.38180
-17320.50980
-25980.76370
-34641.01950
-43301.27340
-76.60445
-153.20891
-229.81335
-306.41782
-383.02228
-459.62671
-536.23120
-612.83563
-689.44006
-766.04449
-957.55566
-1149.06689
-1340.57788
-1532.08899
-1723.60022
-1915.11121
-2298.13354
-3064.17822
-3830.22241
-5745.33350
-7660.44531
-11490.66700
-15320.89060
-22981.33590
-30641.78130
-38302.22660
-64.27877
-128.55756
-192.83632
-257.11511
Volume VII
Appendix VTI-4
2565.15063
3420.20093
5130.30078
6840.40186
10260.60250
13680.80370
17101.00390
49.99999
^VB^VTTO
149.99997
199.99997
249.99994
299.99991
349.99991
399.99991
449.99991
499.99988
624.99988
749.99988
874.99988
999.99982
1125.00000
1249.99976
1499.99976
1999.99963
2499.99951
3749.99951
4999.99854
7499.99854
9999.99805
14999.99800
19999.99610
24999.99610
64.27876
128.55751
192.83626
257.11499
321.39374
385.67255
449.95126
514.22998
578.50873
642.78760
803.48444
964.18121
1124.87830
1285.57507
1446.27173
1606.96887
1928.36255
2571.15015
3213.93750
4820.90576
6427.87451
9641.81250
12855.75000
19283.62500
25711.50000
32139.37700
76.60442
153.20885
229.81332
306.41772
0.02651
0.01750
0.01054
07*866=
0.00468
0.00366
0.00261
0.00909
0.00298
0.00224
0.00289
0.00185
0.00363
0.02855
0.11251
0.12740
0.10439
0.06826
0.12045
0.12632
0.11477
0.09956
0.09223
0.07538
0.05595
0.04624
0.02873
0.01943
0.01221
0.00850
0.00485
0.00361
0.00355
0.01046
0.00248
0.00261
0.00281
0.00154
0.00297
0.03484
0.14881
0.17976
0.16868
0.10859
0.15540
0.14294
0.12338
0.11137
0.09725
0.07671
0.05916
0.04344
0.02626
0.01903
0.01217
0.00736
0.00443
0.00316
0.00271
0.01127
0.00804
0.00507
0.00172
371.90
424.90
420.00
360.00
400.00
380.00
400.00
213.40
213.40
219.50
231.60
225.60
231.60
268.20
304.80
310.90
304.80
292.60
323.10
359.70
371.90
371.90
378.00
378.00
378.00
384.00
384.00
426.70
400.00
400.00
420.00
400.00
350.00
213.40
213.40
225.60
231.60
225.60
231.60
268.20
304.80
316.40
317.00
304.80
341.40
353.60
365.80
371.90
378.00
384.00
359.70
384.00
378.00
379.20
360.00
400.00
400.00
400.00
370.00
213.40
225.60
231.60
231.60
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL%
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
External Review Draft
Do Not Cite or Quote
-------
-321.39383
-385.67267
-449.95142
-514.23022
-578.50897
-642.78772
-803.48474
-964.18152
•1124.87854
-1285.57532
-1446.27222
-1606.96936
-1928.36328
-2571.15088
-3213.93872
-4820.90771
-6427.87695
-9641.81543
-12855.75490
-19283.63090
-25711.50980
-32139.38670
-50.00002
-100.00003
-150.00005
-200.00006
-250.00009
-300.00009
-350.00012
-400.00012
-450.00015
-500.00018
-625.00024
-750.00024
-875.00031
-1000.00037
-1125.00037
-1250.00049
-1500.00049
-2000.00073
-2500.00098
-3750.00122
-5000.00195
-7500.00244
-10000.00390
-15000.00490
-20000.00780
-25000.00780
-34.20204
-68.40408
-102.60610
-136.80815
-171.01018
-205.21220
-239.41423
-273.61633
-307.81833
-342.02036
-427.52545
-513.03052
-598.53571
-684.04065
-769.54584
Volume VH
Appendix VII-4
383.02216
459.62665
536.23102
612.83551
689.43988
766.04431
957.55542
1149.06653
1340.57751
1532.08862
1723.59973
1915.11084
2298.13306
3064.17749
3830.22144
5745.33203
7660.44336
11490.66410
15320.88670
22981.33010
30641.77340
38302.21880
86.60253
173.20506
259.80756
346.41013
433.01270
519.61517
606.21771
692.82025
779.42279
866.02533
1082.53162
1299.03784
1515.54431
1732.05066
1948.55701
2165.06323
2598.07593
3464.10132
4330.12646
6495.18994
8660.25293
12990.37990
17320.50590
25980.75980
34641.01170
43301.26170
93.96925
187.93851
281.90778
375.87698
469.84631
563.81555
657.78479
751.75403
845.72327
939.69257
1174.61572
1409.53894
1644.46191
1879.38513
2114.30811
0.00120
0.00337
0.04874
Orfttso
0.16194
0.14121
0.13229
0.14348
0.11287
0.10092
0.08770
0.07507
0.06108
0.04295
0.03208
0.01919
0.01385
0.00845
0.00540
0.00332
0.00273
0.00214
0.01205
0.00821
0.00338
0.00212
0.00064
0.00928
0.01154
0.00983
0.09395
0.08651
0.03698
0.08146
0.07954
0.06947
0.05363
0.04944
0.04007
0.02813
0.02042
0.01240
0.00900
0.00582
0.00388
0.00258
0.00160
0.00142
0.01349
0.01019
0.00144
0.00074
0.00054
0.00642
0.01477
0.03610
0.02741
0.03747
0.05964
0.07052
0.05843
0.04815
0.03696
225.60
231.60
274.30
-304.80
310.90
310.90
317.00
347.50
353.60
353.60
359.70
365.80
384.00
384.00
378.00
378.00
378.00
380.00
"400.00
400.00
360.00
360.00
213.40
225.60
231.60
231.60
225.60
243.80
249.90
243.80
304.80
304.80
286.50
329.20
347.50
353.60
353.60
384.00
384.00
384.00
378.00
365.80
371.90
360.00
360.00
340.00
380.00
350.00
213.40
225.60
225.60
225.60
225.60
243.80
262.10
286.50
280.40
292.60
323.10
353.60
359.70
359.70
329.20
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL,
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
External Review Draft
Do Not Cite or Quote
-------
-855.05090
-1026.06104
-1368.08130
-1710.10181
-2565.15283
-3420.20337
-5130.30518
-6840.40674
-10260.61040
-13680.81450
-17101.01760
-17.36484
-34.72969
-52.09453
-69.45937
-86.82422
-104.18906
-121.55391
-138.91873
-156.28360
-173.64844
-217.06055
-260.47269
-303.88474
-347.29691
-390.70898
-434.12109
-520.94531
-694.59375
-868.24219
-1302.36353
-1736.48438
-2604.72656
-3472.96875
-5209.45264
-6945.93701
-8682.42188
-0.00003
-0.00006
-0.00009
-0.00012
-0.00015
-0.00018
-0.00021
-0.00024
-0.00027
-0.00030
-0.00038
-0.00045
-0.00053
-0.00060
-0.00068
-0.00075
-0.00091
-0.00121
-0.00151
-0.00226
-0.00302
-0.00453
-0.00604
-0.00906
-0.01208
-0.01510
Volume VII
Appendix VII-4
2349.23145
2819.07764
3758.77026
4698.46289
7047.69385
9396.92578
14095.38770
18793.85350
28190.77540
37587.70310
46984.62890
98.48077
196.96155
295.44235
393.92307
492.40381
590.88470
689.36542
787.84613
886.32697
984.80768
1231.00964
1477.21143
1723.41345
1969.61523
2215.81738
2462.01929
2954.42285
3939.23071
4924.03809
7386.05713
9848.07715
14772.11430
19696.15430
29544.22850
39392.30860
49240.38670
100.00000
200.00000
300.00000
400.00000
500.00000
600.00000
700.00000
800.00000
900.00000
1000.00000
1250.00000
1500.00000
1750.00000
2000.00000
2250.00000
2500.00000
3000.00000
4000.00000
5000.00000
7500.00000
10000.00000
15000.00000
20000.00000
30000.00000
40000.00000
50000.00000
0.03845
0.03339
0.02373
010T773—
0.01035
0.00815
0.00503
0.00356
0.00230
0.00154
0.00129
0.01627
0.01058
0.00207
0.00071
0.00094
0.00594
0.01178
0.03511 -
0.04108
0.03979
0.07424
0.08236
0.06907
0.06204
0.05155
0.04931
0.04094
0.03026
0.02326
0.01429
0.01032
0.00644
0.00421
0.00284
0.00202
0.00162
0.02140
0.01037
0.00185
0.00148
0.00194
0.00569
0.01115
0.03124
0.06229
0.04796
0.12129
0.07946
0.08049
0.05599
0.06285
0.05486
0.04487
0.03086
0.02441
0.01426
0.00997
0.00619
0.00480
0.00235
0.00196
0.00153
347.50
378.00
385.00
3T1.90
329.20
349.00
360.00
360.00
340.00
370.00
350.00
213.40
225.60
225.60
225.60
225.60
243.80
262.10
292.60
298.70
298.70
335.30
365.80
359.70
359.70
341.40
378.00
384.00
378.00
365.80
341.40
339.90
340.00
360.00
340.00
330.00
320.00
213.40
225.60
225.60
225.60
225.60
237.70
256.00
280.40
298.70
292.60
353.60
323.10
341.40
317.00
359.70
359.70
378.00
383.40
359.70
371.90
380.10
360.00
340.00
380.00
350.00
350.00
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD .
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
External Review Draft
Do Not Cite or Quote
-------
B. Off-Site Fire Scenario
Volume VH External Review Draft
Appendix VII-4 Do Not Cite or Quote
-------
CO STARTING
TITLEONE
TITLETyO
NOOELOPT
AVERTINE
POLLUTID
TERRHGTS
ELEVUNIT
RUNORNOT
ERRORFIL
CO FINISHED
WTI Truck Accident Off-Site, ISCOMDEP -- OFFSITE
1 Point source; 26 receptfrr up to 50KM away; Vapor.
GRORIS NOSTO RURAL CONC
1 3 24 PERIOD
ChMical
ELEV
METERS
RUN
OFFSITE.ERR
SO STARTING
LOCATION OFFSITE POINT -908. 79. 212.1
** Point Source OS MS TS VS DS
** Parameters:
SO SRCPARAM OFFSITE 1.0 38.0 997. 0.225, 30.59
**SO SRCPARAM OFFSITE 1.0 38.0 997. 0.075 52.98
SO SRCGROUP ALL
SO FINISHED
RE STARTING
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
Volume Vn
17.36482
34.72963
52.09445
69.45927
86.82409
104.18890
121.55372
138.91853
156.28336
173.64818
217.06021
260.47226
303.88431
347.29636
390.70837
434.12042
520.94452
694.59271
868.24084
1302.36133
1736.48169
2604.72266
3472.96338
5209.44531
6945.92676
8682.40820
34.20201
68.40403
102.60604
136.80806
171.01007
205.21208
239.41409
273.61612
307.81812
342.02014
427.52518
513.03021
596.53522
98.48077
196.96155
295.44232
393.92310
492.40387
590.88464
689.36542
787.84619
886.32697
964.80774
1231.00964
1477.21167
1723.41357
1969.61548
2215.81738
2462.01929
2954.42334
3939.23096
4924.03857
7386.05811
9648.07715
14772.11620
19696.15430
29544.23240
39392.30860
49240.38670
93.96926
187.93852
281.90778
375.87704
469.84631
563.81555
657.78485
751.75409
845.72339
939.69263
1174.61572
1409.53894
1644.46204
213.4
225.6
225.6
225.6
225.6
225.6
243.8
256.0
280.4
286.5
353.6
353.6
310.9
347.5
353.6
359.7
347.5
341.4
341.4
365.8
360.0
340.0
340.0
360.0
350.0
360.0
213.4
225.6
225.6
225.6
225.6
225.6
237.7
243.8
256.0
286.5
329.2
347.5
335.3
Appendix VIJ-4
External Review Draft
Do Not Cite or Quote
-------
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE'DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE OISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE OISCCART
RE DISCCART
RE DISCCART
684.04028
769.54529
855.05035
1026.06042
1368.08057
1710.10071
2565.15112
3420.20142
5130.30225
6840.40283
10260.60450
13680.80570
17101.00590
50.00000
100.00000
150.00000
200.00000
250.00000
300.00000
350.00000
400.00000
450.00000
500.00000
625.00000
750.00000
875.00000
1000.00000
1125.00000
1250.00000
1500.00000
2000.00000
2500.00000
3750.00000
5000.00000
7500.00000
10000.00000
15000.00000
20000.00000
25000.00000
64.27876
128.55753
192.83627
257.11505
321.39380
385.67255
449.95132
514.23010
578.50885
642.78760
803.48450
964.18140
1124.87830
1285.57520
1446.27209
1606.96899
1928.36279
2571.15039
3213.93799
4820.90674
6427.87598
9641.81348
12855.75200
19283.62700
1879.38525
2114.30835
2349.23145
2819.07788*
3758.77051
4698.46289
7047.69482
9396.92578
14095.38960
18793.85160
28190.77930
37587.70310
46984.63280
86.60254
173.20508
259.80762
346.41016
433.01270
519.61523
606.21777
692.82031
779.42285
866.02539
1082.53174
1299.03809
1515.54443
1732.05078
1948.55713
2165.06348
2596.07617
3464.10156
4330.12695
6495.19043
8660,25391
12990.38090
17320.50780
25980.76170
34641.01560
43301.26950
76.60445
153.20889
229.81334
306.41779
383.02222
459.62668
536.23114
612.83557
689.44000
766.04443
957.55554
1149.06665
1340.57776
1532.08887
1723.59998
1915.11108
2298.13330
3064.17773
3830.22217
5745.33350
7660.44434
11490.66700
15320.88870
22981.33400
347.5
353.6
359.7
329.2
359.7
369.7
385.9
340.0
340.0
360.0
380.0
390.0
213.4
219.5
225.6
225.6
225.6
225.6
225.6
231.6
243.8
262.1
225.6
347.5
359.7
353.6
353.6
329.2
323.1
361.2
366.7
378.0
396.2
320.0
360.0
380.0
370.0
400.0
213.4
213.4
225.6
225.6
225.6
225.6
225.6
225.6
225.6
243.8
280.4
353.6
361.5
353.6
353.6
353.6
335.3
353.9
353.0
378.0
396.4
376.0
380.0
360.0
Volume VII
Appendix VU-4
External Review Draft
Do Not Cite or Quote
-------
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
25711.50390
32139.37890
76.604*5
153.20889
229.81334
306.41779
383.0????
459.62668
536.23114
612.83557
689.44000
766.04443
957.55554
1149.06665
1340.57776
1532.08887
1723.59998
1915.11108
2298.13330
3064.17773
3830.22217
5745.33350
7660.44434
11490.66700
15320.88870
22981.33400
30641.77730
38302.22270
86.60254
173.20508
259.80762
346.41016
433.01270
519.61523
606.21777
692.82031
779.42285
866.02539
1082.53174
1299.03809
1515.54443
1732.05078
1948.55725
2165.06348
2598.07617
3464.10156
4330.12695
6495.19043
8660.25391
12990.38090
17320.50780
25980.76170
34641.01560
43301.26950
93.96926
187.93852
281.90778
375.87704
469.84631
563.81555
657.78485
751.75409
845.72333
30641.77730
38302.22270
64.27876
128.557B*
192.83629
257.11505
321.39380
385.67258
449.95132
514.23010
578.50885
642.78760
803.48450
964.18140
1124.87830
1285.57520
1446.27209
1606.96899
1928.36279
2571.15039
3213.93799
4820.90723
6427.87598
9641.81445
12855.75200
19283.62890
25711.50390
32139.38090
50.00000
^r.in^^o'
150.00000
iWaWfl^O
249.99998
300.00000
349.99997
399.99997
449.99997
499.99997
624.99994
749.99994
874.99994
999.99994
1125.00000
1249.99988
1499.99988
1999.99988
2499.99976
3749.99976
4999.99951
7499.99951
9999.99902
14999.99900
19999.99800
24999.99800
34.20201
68.40403
102.60604
136.80806
171.01007
205.21208
239.41411
273.61612
307.81815
420.0
420.0
213.4
-20T.3--
213.4
219.5
219.5
219.5
219.5
219.5
225.6
219.5
219.5
323.1
353.6
353.6
335.3
347.5
347.5
341.4
335.3
373.1
396.2
360.0
380.0
380.0
420.0
420.0
213.4
207.3
207.3
201.2
207.3
213.4
213.4
213.4
213.4
219.5
225.6
219.S
243.8
292.6
310.9
323.1
317.0
323.1
359.7
378.9
408.7
380.0
360.0
380.0
380.0
420.0
207.3
201.2
202.7
202.7
207.3
207.3
207.3
213.4
213.4
Volume VH
Appendix VIJ-4
External Review Draft
Do Not Cite or Quote
-------
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
939.69263
1174.61572
1409.53894
1644.46204
1879.38525
2114.30835
2349.23145
2819.07788
3758.77051
4698.46289
7047.69482
9396.92578
14095.38960
18793.85160
28190.77930
37587.70310
46984.63280
98.48077
196.96155
295.44232
393.92310
492.40387
590.88464
689.36542
787.84619
886.32697
984.80774
1231.00964
1477.21167
1723.41357
1969.61548
2215.81738
2462.01929
2954.42334
3939.23096
4924.03857
7386.05811
9848.07715
14772.11620
19696.15430
29544.23240
39392.30860
49240.38670
100.00000
200.00000
300.00000
400.00000
500.00000
600.00000
700.00000
800.00000
900.00000
1000.00000
1250.00000
1500.00000
1750.00000
2000.00000
2250.00000
2500.00000
3000.00000
4000.00000
5000.00000
7500.00000
342.02014
427.52518
513.03021
598.53528*
684.04028
769.54535
855.05035
1026.06042
1368.08057
1710.10071
2565.15112
3420.20142
5130.30225
6840.40283
10260.60450
13680.80570
17101.00780
17.36482
34.72964
52.09447
69.45929
86.82411
104.18893
121.55375
138.91858
156.28340
173.64822
217.06027
260.47232
303.88437
347.29645
390.70850
434.12054
520.94464
694.59290
868.24109
1302.36157
1736.48218
2604.72314
3472.96436
5209.44629
6945.92871
8682.41113
0.00001
0.00002
0.00002
0.00003
0.00004
0.00005
0.00005
0.00006
0.00007
0.00008
0.00009
0.00011
0.00013
0.00015
0.00017
0.00019
0.00023
0.00030
0.00038
0.00057
213.4
213.4
213.4
-*B.4=
213.4
213.4
231.6
231.6
310.9
384.0
384.0
370.3
360.0
380.0
400.0
360.0
400.0
207.3
202.7
202.7
202.7
202.7
202.7
202.7
202.7
202.7
202.7
202.7
202.7
213.4
207.3
207.3
231.6
304.8
346.6
365.8
384.0
371.9
320.0
360.0
380.0
380.0
400.0
207.3
202.7
202.7
202.7
202.7
202.7
202.7
202.7
202.7
202.7
243.8
341.4
323.1
341.4
304.8
292.6
310.9
359.7
402.3
347.5
Volume VII
Appendix VIJ-4
External Review Draft
Do Not Cite or Quote
-------
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE- DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
10000.00000
15000.00000
20000.00000
30000.00000
40000.00000
50000.00000
98.48077
196.96155
295.44232
393.92310
492.40387
590.88464
689.36542
787.84619
886.32697
984.80774
1231.00964
1477.21167
1723.41357
1969.61548
2215.81738
2462.01929
2954.42334
3939.23096
4924.03857
7386.05811
9848.07715
14772.11620
19696.15430
29544.23240
39392.30860
49240.38670
93.96926
187.93852
281.90778
375.87704
469.84631
563.81555
657.78485
751.75409
845.72339
939.69263
1174.61584
1409.53894
1644.46216
1879.38525
2114.30835
2349.23169
2819.07788
3758.77051
4698.46338
7047.69482
9396.92676
14095.38960
18793.85350
28190.77930
37587.70700
46984.63280
86.60254
173.20508
259.80762
346.41016
433.01270
0.00075
0.00113
0.00151
0.002ZT"
0.00302
0.00377
-17.36482
-34.72964
-52.09446
-69.45927
-86.82410
-104.18891
-121.55373
-138.91855
-156.28337
-173.64819
-217.06023
-260.47229
-303.88434
-347.29639
-390.70840
-434.12045
-520.94458
-694.59277
-868.24091
-1302.36145
-1736.48181
-2604.72290
-3472.96362
-5209.44580
-6945.92725
-8682.40918
-34.20201
-68.40402
-102.60603
-136.80804
-171.01006
-205.21207
-239.41408
-273.61609
-307.81812
-342.02011
-427.52515
-513.03015
-598.53522
-684.04022
-769.54529
-855.05029
-1026.06030
-1368.08044
-1710.10059
-2565.15088
-3420.20117
-5130.30176
-6840.40234
-10260.60350
-13680.80470
-17101.00590
-50.00000
-100.00001
-150.00002
-200.00002
-250.00003
380.1
360.0
360.0
=i».o=
400.0
360.0
207.3
202.7
202.7
202.7
202.7
202.7
202.7
219.5
225.6
329.2
347.5
353.6
323.1
341.4
341.4
323.1
347.5
353.6
386.5
353.6
360.0
340.0
380.0
380.0
380.0
400.0
207.3
202.7
202.7
202.7
202.7
213.4
256.0
298.7
286.5
323.1
347.5
347.5
310.9
353.6
350.2
347.5
347.5
345.9
371.9
365.8
408.4
380.0
360.0
360.0
360.0
360.0
207.3
202.7
202.7
202.7
213.4
Volume vn
Appendix VU-4
External Review Draft
Do Not Cite or Quote
-------
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
Volume VH
519.61523
606.21777
692.82031
779.42285
866.02539
1082.53174
1299.03809
1515.54443
1732.05078
1948.55713
2165.06348
2598.07617
3464.10156
4330.12695
6495.19043
8660.25391
12990.38090
17320.50780
25980.76170
34641.01560
43301.26950
76.60445
153.20889
229.81332
306.41779
383.02222
459.62665
536.23108
612.83557
689.44000
766.04443
957.55554
1149.06665
1340.57776
1532.08887
1723.59998
1915.11108
2298.13330
3064.17773
3830.22217
5745.33301
7660.44434
11490.66600
15320.88870
22981.33200
30641.77730
38302.22270
64.27876
128.55753
192.83629
257.11505
321.39380
385.67258
449.95132
514.23010
578.50885
642.78760
803.48450
964.18146
1124.87830
1285.57520
1446.27209
1606.96899
-300.00003
-350.00003
-400.00003
-450.0000?
-500.00006
-625.00006
-750.00006
-875.00006
-1000.00012
-1125.00012
-1250.00012
-1500.00012
-2000.00024
-2500.00024
-3750.00049
-5000.00049
-7500.00098
-10000.00100
-15000.00200
-20000.00200
-25000.00200
-64.27876
-128.55753
-192.83629
-257.11505
-321.39380
-385.67258
-449.95132
-514.23010
-578.50885
-642.78760
-803.48456
-964.18146
-1124.87830
-1285.57520
-1446.27222
-1606.96912
-1928.36292
-2571.15039
-3213.93823
-4820.90723
-6427.87646
-9641.81445
-12855.75290
-19283.62890
-25711.50590
-32139.38090
-76.60445
-153.20889
-229.81332
-306.41779
-383.02222
-459.62665
-536.23108
-612.83557
-689.44000
-766.04443
-957.55554
-1149.06665
-1340.57776
-1532.08887
-1723.59998
-1915.11108
268.2
317.0
347.5
"3533
347.5
310.9
359.7
335.3
359.7
359.7
347.5
365.8
359.7
353.6
402.3
396.2
380.0
380.0
360.0
360.0
360.0
207.3
202.7
202.7
202.7
243.8
298.7
323.1
353.6
353.6
353.6
353.6
359.7
341.4
353.6
353.6
341.4
359.7
359.7
359.7
408.4
408.4
.380.0
360.0
360.0
360.0
360.0
207.3
202.7
202.7
202.7
268.2
304.8
310.9
323.1
329.2
323.1
347.5
359.7
329.2
359.7
353.6
359.7
Appendix VII-4
External Review Draft
Do Not Cite or Quote
-------
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE' DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE. DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
1928.36292
2571.15039
3213.93799
4820.90723
6427.87598
9641.81445
12855.75200
19283.62890
25711.50390
32139.38090
50.00000
100.00001
150.00002
200.00002
250.00002
300.00003
350.00003
400.00003
450.00003
500.00003
625.00006
750.00006
875.00006
1000.00006
1125.00012
1250.00012
1500.00012
2000.00012
2500.00024
3750.00024
5000.00049
7500.00049
10000.00100
15000.00100
20000.00200
25000.00200
34.20202
68.40405
102.60606
136.80809
171.01012
205.21213
239.41415
273.61618
307.81821
342.02023
427.52527
513.03033
598.53540
684.04047
769.54547
855.05054
1026.06067
1368.08093
1710.10107
2565.15161
3420.20215
5130.30322
6840.40430
10260.60640
13680.80860
17101.01170
17.36483
-2298.13330
-3064.17773
-3830.22217
-5745.33350*
-7660.44434
-11490.66700
-15320.88870
-22981.33400
-30641.77730
-38302.22270
-86.60254
-173.20508
-259.80762
-346.41016
-433.01270
-519.61523
-606.21777
-692.82031
-779.42285
-866.02539
-1082.53174
-1299.03809
-1515.54443
-1732.05078
-1948.55713
-2165.06348
-2598.07617
-3464.10156
-4330.12695
-6495.19043
-8660.25391
-12990.38090
-17320.50780
-25980.76170
-34641.01560
-43301.26950
-93.96926
-187.93852
-281.90778
-375.87704
-469.84628
-563.81555
-657.78479
-751.75409
-845.72333
-939.69257
-1174.61572
-1409.53894
-1644.46204
-1879.38513
-2114.30835
-2349.23145
-2819.07788
-3758.77026
-4698.46289
-7047.69434
-9396.92578
-14095.38870
-18793.85160
-28190.77730
-37587.70310
-46984.62890
-96.48077
408.4
420.6
371.9
"392 X
390.1
340.0
380.0
400.0
400.0
380.0
207.3
202.7
202.7
213.4
268.2
298.7
310.9
321.1
323.1
329.2
298.7
341.4
341.4
359.7
365.8
371.9
408.4
420.6
408.4
408.4
396.2
340.0
360.0
420.0
400.0
400.0
207.3
202.7
202.7
207.3
268.2
292.6
304.8
304.8
286.5
286.5
304.8
310.9
304.8
335.3
359.7
378.0
396.2
402.3
411.5
402.3
408.1
360.0
360,0
420.0
400.0
420.0
207.3
Volume Vn
Appendix VII-4
External Review Draft
Do Not Cite or Quote
-------
RE OISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE OISCCART
RE DISCCART
RE .DISCCART
RE OISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE OISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
Volume VII
Appendix VU-4
34.72966 -196.96155
52.09449 -295.44232
69.45932 -393.92310
202.7
202.7
202.7
86.82414 -492.40387*^249^
104.18897 -590.88464
121.55380 -689.36542
138.91864 -787.84619
156.28346 -886.32697
173.64828 -984.80774
217.06036 -1231.00964
260.47244 -1477.21155
303.88452 -1723.41357
347.29657 -1969.61548
390.70865 -2215.81738
434.12073 -2462.01929
520.94489 -2954.42310
694.59314 -3939.23096
868.24146 -4924.03857
1302.36218 -7386.05811
1736.48291 -9848.07715
2604.72437 -14772.11620
3472.96582 -19696.15430
5209.44873-29544.23240
6945.93164 -39392.30860
8682.41504 -49240.38670
0.00002 -100.00000
0.00003 -200.00000
0.00005 -300.00000
0.00006 -400.00000
0,00008 -500.00000
0.00009 -600.00000
0.00011 -700.00000
0.00012 -800.00000
0.00014 -900.00000
0.00015 -1000.00000
0.00019 -1250.00000
0.00023 -1500.00000
0.00026 -1750.00000
0.00030 -2000.00000
0.00034 -2250.00000
0.00038 -2500.00000
0.00045 -3000.00000
0.00060 -4000.00000
0.00075 -5000.00000
0.00113 -7500.00000
0.00151 -10000.00000
0.00226 -15000.00000
0.00302 -20000.00000
0.00453 -30000.00000
0.00604 -40000.00000
0.00755 -50000.00000
-17.36482 -98.48077
-34.72964 -196.96155
-52.09447 -295.44232
•69.45929 -393.92310
-86.82411 -492.40387
-104.18893 -590.88464
-121.55376 -689.36542
-138.91858 -787.84619
-156.28340 -886.32697
-173.64822 -964.80774
-217.06029 -1231.00964
-260.47235 -1477.21167
286.5
280.4
274.3
286.5
286.5
298.7
304.8
304.8
298.7
298.7
365.8
402.3
390.1
414.5
408.4
398.1
380.0
360.0
400.0
400.0
400.0
207.3
202.7
202.7
202.7
219.5
274.3
280.4
274.3
243.8
298.7
304.8
304.8
304.8
292.6
298.7
365.8
406.3
402.3
396.2
390.1
396.2
380.0
360.0
380.0
380.0
400.0
207.3
202.7
202.7
202.7
202.7
225.6
274.3
274.3
237.7
292.6
304.8
286.5
External Review Draft
Do Not Cite or Quote
-------
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
-303.88440
-347.29645
-390.70853
-434.12057
-520.94470
-694.59290
-868.24115
-1302.36169
-1736.48230
-2604.72339
-3472.96460
-5209.44678
-6945.92920
-8682.41113
-34.20201
-68.40403
-102.60605
-136.80806
-171.01009
-205.21210
-239.41411
-273.61612
-307.81815
-342.02017
-427.52521
-513.03021
-596.53528
-684.04034
-769.54535
-855.05042
-1026.06042
-1368.08069
-1710.10083
-2565.15112
-3420.20166
-5130.30225
-6840.40332
-10260.60450
-13680.80660
-17101.00780
-50.00000
-100.00000
-150.00000
-200.00000
-250.00000
-300.00000
-350.00000
-400.00000
-450.00000
-500.00000
-625.00000
-750.00000
-875.00000
-1000.00000
-1125.00000
-1250.00000
-1500.00000
-2000.00000
-2500.00000
-3750.00000
-5000.00000
-7500.00000
-10000.00000
-1723.41357
-1969.61548
-2215.81738
-2462.01929*"
-2954.42334
-3939.23096
-4924.03857
-7386.05811
-9848.07715
-14772.11620
-19696.15430
-29544.23240
-39392.30860
-49240.38670
-93.96926
-187.93852
-281.90778
-375.87704
-469.84631
-563.81555
-657.78485
-751.75409
-845.72333
-939.69263
-1174.61572
-1409.53894
-1644.46204
-1879.38525
-2114.30835
-2349.23145
-2819.07788
-3758.77051
-4698.46289
-7047.69482
-9396.92578
-14095.38960
-18793.85160
-28190.77930
-37587.70310
-46984.62890
-86.60254
-173.20508
-259.80762
-346.41016
-433.01270
-519.61523
-606.21777
-692.82031
-779.42285
-866.02539
-1082.53174
-1299.03809
-1515.54443
-1732.05078
-1948.55713
-2165.06348
-2598.07617
-3464.10156
-4330.12695
-6495.19043
-8660.25391
-12990.38090
-17320.50780
292.6
280.4
304.8
353.61
384.0
396.2
415.4
390.1
392.0
360.0
340.0
340.0
360.0
380.0
213.4
202.7
202.7
202.7
202.7
202.7
219.5
249.9
219.5
280.4
280.4
280.4
280.4
262.1
296.7
353.6
371.9
402.3
397.2
384.0
384.0
340.0
340.0
360.0
380.0
380.0
213.4
202.7
202.7
202.7
202.7
202.7
202.7
202.7
202.7
219.5
219.5
213.4
213.4
231.6
231.6
292.6
359.7
396.2
414.5
396.2
392.6
360.0
380.0
Volume VH
Appendix VIM
External Review Draft
Do Not Cite or Quote
-------
RE OISCCART
RE DISCCART
RE DISCCART
RE OISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE OISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
-15000.00000
-20000.00000
-25000.00000
-64.27876
-128.55751
-192.83627
-257.11502
-321.39380
-385.67255
-449.95129
-514.23004
-578.50879
-642.78760
-803.48444
-964.18134
-1124.87830
-1285.57520
-1446.27197
-1606.96887
-1928.36267
-2571.15039
-3213.93774
-4820.90674
-6427.87549
-9641.81348
-12855.75100
-19283.62700
-25711.50200
-32139.37890
-76.60445
-153.20891
-229.81337
-306.41782
-383.02228
-459.62674
-536.23120
-612.83563
-689.44006
-766.04456
-957.55566
-1149.06677
-1340.57800
-1532.08911
-17Z3. 60022
-1915.11133
-2298.13354
-3064.17822
-3830.22266
-5745.33398
-7660.44531
-11490.66800
-15320.89060
-22981.33590
-30641.78130
-38302.22660
-86.60255
-173.20509
-259.80765
-346.41019
-433.01273
-519.61530
-606.21783
-692.82037
-25980.76170
-34641.01560
-43301.26950
-76.6Q&?
-153.20889
-229.81334
-306.41779
•383.02225
-459.62668
-536.23114
-612.83557
-689.44000
-766.04449
-957.55560
-1149.06677
-1340.57788
-1532.08899
-1723.60010
-1915.11121
-2298.13354
-3064.17798
-3830,22241
-5745.33350
-7660.44482
-11490.66700
-15320.88960
-22981.33400
-30641.77930
-38302.22270
-64.27875
-128.55750
-192.83624
-257.11499
-321.39374
-385.67249
-449.95123
-514.22996
-578.50873
-642.78748
-803.48438
-964.18121
-1124.87817
-1285.57495
-1446.27185
-1606.96875
-1928.36243
-2571.14990
-3213.93750
•4820.90625
-6427.87500
-9641.81250
-12855.75000
-19283.62500
-25711.50000
-32139.37500
-49.99999
*W • l^^^^^S
-149.99997
-199.99995
-249.99995
"Z^9«T^9r4
™^^y» i^^^ff
"3TT»yyTr1
360.0
360.0
380.0
^'2«.€
202.7
202.7
202.7
202.7
202.7
202.7
202.7
202.7
202.7
202.7
213.4
213.4
213.4
213.4
213~.4
371.9
378.0
396.2
396.2
378.0
349.0
360.0
360.0
380.0
360.0
213.4
201.2
207.3
207.3
202.7
202.7
202.7
202.7
207.3
207.3
207.3
207.3
207.3
213.4
213.4
256.0
323.1
359.7
384.0
378.0
378.0
360.0
380.0
400.0
400.0
380.0
213.4
213.4
213.4
207.3
213.4
213.4
213.4
213.4
Volume VH
Appendix VU-4
External Review Draft
Do Not Cite or Quote
-------
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
Volume VIJ
-779.42291
-866.02545
-1082.53186
-1299.03821
-1515.54456
-1732.05090
-1948.55725
-2165.06372
-2598.07642
-3464.10181
-4330.12744
-6495.19092
-8660.25488
-12990.38180
-17320.50980
-25980.76370
-34641.01950
-43301 .27340
-93.96926
-187.93852
-281.90781
•375.87704
-469.84631
-563.81561
-657.78485
-751.75409
-845.72339
-939.69263
-1174.61584
-1409.53894
-1644.46216
-1879.38525
-2114.30835
-2349.23169
-2819.07788
-3758.77051
-4698.46338
-7047.69482
-9396.92676
-14095.38960
-18793.85350
-28190.77930
-37587.70700
-46964.63280
•96.48077
-196.96155
-295.44232
-393.92310
-492.40387
-590.88464
-689.36542
-787.84619
-886.32697
-984.80774
-1231.00964
-1477.21167
-1723.41357
-1969.61548
-2215.81738
-2462.01929
-2954.42334
-3939.23096
-4924.03857
-449.99991
-499.99991
-624.99988
-749.999BT*
-874.99982
-999.99982
-1124.99976
-1249.99976
-1499.99976
-1999.99963
-2499.99951
-3749.99927
-4999.99902
-7499.99854
-9999.99805
-14999.99710
-19999.99610
-24999.99410
-34.20201
-68.40401
-102.60602
-136.80803
-171.01004
-205.21204
-239.41405
-273.61606
-307.81805
-342.02008
-427.52509
-513.03009
-598.53510
-684.04016
-769.54517
-855.05017
-1026.06018
-1368.08032
-1710.10034
-2565.15039
-3420.20068
-5130.30078
-6840.40137
-10260.60160
-13680.80270
-17101.00390
-17.36481
-34.72963
-52.09444
-69.45925
-86.82407
-104.18888
-121.55370
-138.91850
-156.28333
-173.64813
-217.06017
-260.47220
-303.88422
-347.29626
-390.70828
-434.12033
-520.94440
-694.59253
-868.24066
213.4
213.4
225.6
'ZTf.r
329.2
310.9
286.5
256.0
243.8
365.8
372.5
378.0
402.3
360.0
380.0
380.0
400.0
360.0
213.4
213.4
213.4
213.4
213.4
213.4
213.4
219.5
219.5
213.4
353.6
353.6
341.4
335.3
353.6
304.8
243.8
298.7
359.7
365.8
402.3
380.0
400.0
380.0
400.0
360.0
213.4
213.4
213.4
213.4
213.4
213.4
213.4
219.5
225.6
310.9
359.7
359.7
365.8
371.9
353.6
371.9
353.6
365.8
365.8
Appendix VIJ-4
External Review Draft
Do Not Cite or Quote
-------
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
-7386.05811
-9848.07715
-H772.11620
-19696.15430
-29544.23240
-39392.30860
-49240.38670
-100.00000
-200.00000
-300.00000
-400.00000
-500.00000
-600.00000
-700.00000
-800.00000
-900.00000
-1000.00000
-1250.00000
-1500.00000
-1750.00000
-2000.00000
-2250.00000
-2500.00000
-3000.00000
-4000.00000
-5000.00000
-7500.00000
-10000.00000
-15000.00000
-20000.00000
-30000.00000
-40000.00000
-50000.00000
-98.48077
-196.96155
-295.44232
-393.92310
-492.40387
-590.88464
-689.36542
-787.84619
-886.32697
-984.80774
-1231.00964
-1477.21167
-1723.41357
-1969.61548
-2215.81738
-2462.01929
-2954.42334
-3939.23096
-4924.03857
-7386.05811
-9848.07715
-14772.11620
-19696.15430
-29544.23240
-39392.30860
-49240.38670
-93.96926
-187.93852
-281.90781
-375.87704
-1302.36096
-1736.48132
-2604.72192
-3472.96255"
-5209.44385
-6945.92529
-8682.40625
0.00000
0.00000
0.00000
0.00000
0.00001
0.00001
0.00001
0.00001
0.00001
0.00001
0.00001
0.00002
0.00002
0.00002
0.00003
0.00003
0.00004
0.00005
0.00006
0.00009
0.00012
0.00018
0.00024
0.00036
0.00048
0.00060
17.36481
34.72963
52.09445
69.45926
86.82407
104.18890
121.55371
138.91852
156.28334
173.64815
217.06020
260.47223
303.88428
347.29630
390.70834
434.12039
520.94446
694.59259
868.24078
1302.36121
1736.48157
2604.72241
3472.96313
5209.44482
6945.92627
8682.40820
34.20201
68.40401
102.60603
136.80803
390.1
339.9
360.0
^TSO.ff
420.0
400.0
400.0
213.4
213.4
213.4
213.4
213.4
213.4
213.4
213.4
243.8
298.7
304.8
304.8
335.3
341.4
371.9
371.9
371.9
378.0
371.9
371.9
360.0
340.0
360.0
380.0
380.0
400.0
213.4
213.4
213.4
213.4
213.4
225.6
225.6
237.7
243.8
280.4
317.0
304.8
298.7
341.4
371.9
353.6
365.8
353.6
378.0
384.0
389.2
400.0
420.0
380.0
380.0
400.0
213.4
213.4
213.4
219.5
Volume VH
Appendix VIJ-4
External Review Draft
Do Not Cite or Quote
-------
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE. DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
-469.84631
-563.81561
-657.78485
-751.75409
-845.72339
-939.69263
-1174.61584
-1409.53894
-1644.46216
-1879.38525
-2114.30835
-2349.23169
-2819.07788
-3758.77051
-4698.46338
-7047.69482
-9396.92676
-14095.38960
-18793.85350
-28190.77930
-37587.70700
-46984.63280
-86.60255
-173.20509
-259.80765
-346.41019
-433.01273
-519.61530
-606.21783
-692.82037
-779.42291
-866.02545
-1082.53186
-1299.03821
-1515.54456
-1732.05090
-1948.55725
-2165.06372
-2598.07642
-3464.10181
-4330.12744
-6495.19092
-8660.25488
-12990.38180
-17320.50980
-25980.76370
-34641.01950
-43301.27340
-76.60445
-153.20891
-229.81335
-306.41782
-383.02225
-459.62671
-536.23114
-612.83563
-689.44006
-766.04449
-957.55566
-1149.06677
-1340.57788
-1532.08899
-1723.60022
171.01004
205.21205
239.41406
273.6160^"
307.81808
342.02008
427.52512
513.03015
598.53516
684.04016
769.54523
855.05023
1026.06030
1368.08032
1710.10046
2565.15063
3420.20093
5130.30127
6840.40186
10260.60250
13680.80370
17101.00390
49.99999
^TF •^TM^^S
149.99997
199.99997
249.99995
9Ofi (MOO/,
CTT • 9 9 9 r*t
349.99994
jW«^T^^W>
449.99994
499.99991
624.99988
749.99988
874.99988
999.99982
1124.99988
1249.99976
1499.99976
1999.99963
2499.99951
3749.99951
4999.99902
7499.99902
9999.99805
14999.99800
19999.99610
24999.99610
64.27875
128.55750
192.83626
257.11499
321.39377
385.67252
449.95126
514.22998
578.50879
642.78754
803.48438
964.18127
1124.87817
1285.57507
1446.27185
225.6
225.6
243.8
-2W.5
286.5
298.7
317.0
296.7
298.7
359.7
384.0
378.0
378.0
378.0
378.0
371.9
424.9
420.0
360.0
400.0
380.0
400.0
213.4
213.4
219.5
231.6
225.6
231.6
268.2
304.8
310.9
304.8
292.6
323.1
359.7
371.9
371.9
378.0
378.0
378.0
384.0
384.0
426.7
400.0
400.0
420.0
400.0
350.0
213.4
213.4
225.6
231.6
225.6
231.6
268.2
304.8
316.4
317.0
304.8
341.4
353.6
365.8
371.9
Volume VH
Appendix VJJ-4
External Review Draft
Do Not Cite or Quote
-------
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE1 DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
-1915.11133
-2298.13354
-3064.17798
-3830.22266
-5745.33398
-7660.44531
-11490.66800
-15320.89060
-22981.33590
-30641.78130
-38302.22660
-64.27877
-128.55754
-192.83632
-257.11508
-321.39386
-385.67264
-449.95142
-514.23016
-578.50897
-642.78772
-803.48468
-964.18158
-1124.87854
-1285.57544
-1446.27246
-1606.96936
-1928.36316
-2571.15088
-3213.93872
-4820.90820
-6427.87744
-9641.81641
-12855.75490
-19283.63280
-25711.50980
-32139.38670
-50.00002
-100.00003
-150.00005
-200.00006
-250.00009
-300.00009
-350.00012
-400.00012
-450.00015
-500.00018
-625.00024
-750.00024
-875.00031
-1000.00037
-1125.00037
-1250.00049
-1500.00049
-2000.00073
-2500.00098
-3750.00122
-5000.00195
-7500.00244
-10000.00390
-15000.00490
-20000.00780
-25000.00780
1606.96875
1928.36255
257V.1"5015
3213.93750*
4820.90625
6427.87500
9641.81250
12855.75000
19283.62500
25711.50000
32139.37500
76.60443
153.20886
229.81331
306.41772
383.02216
459.62662
536.23102
612.83545
689.43988
766.04431
957.55542
1149.06653
1340.57764
1532.08862
1723.59973
1915.11084
2298.13306
3064.17725
3830.22168
5745.33252
7660.44336
11490.66500
15320.88670
22981.33010
30641.77340
38302.21880
86.60253
173.20506
259.80759
346.41013
433.01266
519.61517
606.21771
692.82025
779.42279
866.02533
1082.53162
1299.03796
1515.54431
1732.05066
1948.55688
2165.06323
2598.07593
3464.10132
4330.12646
6495.18994
8660.25293
12990.37990
17320.50590
25980.75980
34641.01170
43301.26560
378.0
384.0
359.7
~TSK.1F
378.0
379.2
360.0
400.0
400.0
400.0
370.0
213.4
225.6
231.6
231.6
225.6
231.6
274.3
304.8
310.9
310.9
317.0
347.5
353.6
353.6
359.7
365.8
384.0
384.0
378.0
378.0
378.0
380.0
400.0
400.0
360.0
360.0
213.4
225.6
231.6
231.6
225.6
243.8
249.9
243.8
304.8
304.8
286.5
329.2
347.5
353.6
353.6
384.0
384.0
384.0
378.0
365.8
371.9
360.0
360.0
340.0
380.0
350.0
Volume VH
Appendix VIM
External Review Draft
Do Not Cite or Quote
-------
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
-34.20204
-68.40408
-102.60611
-136.80815
-171.01018
-205.21222
-239.41425
-273.61630
-307.81833
-342.02036
-427.52545
-513.03052
-598.53564
-684.04071
-769.54584
-855.05090
-1026.06104
-1368.08142
-1710.10181
-2565.15283
-3420.20361
-5130.30566
-6840.40723
-10260.61130
-13680.81450
-17101.01760
-17.36484
-34.72969
-52.09453
-69.45937
-86.82422
-104.18906
-121.55391
-138.91875
-156.28360
-173.64844
-217.06055
-260.47266
-303.88477
-347.29688
-390.70898
-434.12109
-520.94531
-694.59375
-868.24219
-1302.36328
-1736.48438
-2604.72656
-3472.96875
-5209.45313
-6945.93750
-8682.42188
-0.00003
-0.00006
-0.00009
-0.00012
-0.00015
-0.00018
-0.00021
-0.00024
-0.00027
-0.00030
-0.00038
93.96925
187.93851
281.90778
375.8770T "
469.84628
563.81555
657.78479
751.75403
845.72327
939.69257
1174.61572
1409.53882
1644.46191
1879.38513
2114.30811
2349.23145
2819.07764
3758.77026
4698.46289
7047.69385
9396.92578
14095.38770
18793.85160
28190.77540
37587.70310
46984.62890
98.48077
196.96155
295.44232
393.92310
492.40384
590.88464
689.36542
787.84619
886.32697
984.80768
1231.00964
1477.21155
1723.41345
1969.61536
2215.81738
2462.01929
2954.42310
3939.23071
4924.03857
7386.05762
9848.07715
14772.11520
19696.15430
29544.23050
39392.30860
49240.38670
100.00000
200.00000
300.00000
400.00000
500.00000
600.00000
700.00000
800.00000
900.00000
1000.00000
1250.00000
213.4
225.6
225.6
225.5
225.6
243.8
262.1
286.5
280.4
292.6
323.1
353.6
359.7
359.7
329.2
347.5
378.0
385.0
371.9
329.2
349.0
360.0
360.0
340.0
370.0
350.0
213.4
225.6
225.6
225.6
225.6
243.8
262.1
292.6
298.7
298.7
335.3
365.8
359.7
359.7
341.4
378.0
384.0
378.0
365.8
341.4
339.9
340.0
360.0
340.0
330.0
320.0
213.4
225.6
225.6
225.6
225.6
237.7
256.0
280.4
298.7
292.6
353.6
Volume VII
Appendix VII-4
External Review Draft
Do Not Cite or Quote
-------
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE .DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE DISCCART
RE FINISHED
•0.00045
•0.00053
•0.00060
•0.00068
•0.00075
•0.00091
•0.00121
•0.00151
•0.00226
•0.00302
•0.00453
•0.00604
•0.00906
•0.01208
•0.01510
1500
1750
2000
2250
2500
3000
4000
5000
7500
10000
15000
20000
30000
40000
50000
.00000
.00000
.00000
.00000"
.00000
.00000
.00000
.00000
.00000
.00000
.00000
.00000
.00000
.00000
.00000
323.1
341.4
317.0
'iisr.T
359.7
378.0
383.4
359.7
371.9
380.1
360.0
340.0
380.0
350.0
350.0
ME STARTING
HE INPUTFfl
NE ANENHGHT
NE SURFDATA
NE UAIRDATA
DEPBIN.net
30.0 METERS
94823 1993
94823 1993
ME PROFFILE TEMPS ISC_TEMP.STK
ME PROFFILE WINDS ISC_WINO.STK
** DAYRANGE 1/3
ME FINISHED
TG STARTING
INPUTFIL UtilOOk.OUt
LOCATION 538.4 4497.8 Ion
TG FINISHED
OU STARTING
RECTABLE ALLAVE FIRST-SECOND
** DAYTABLE ALLAVE
MAXTABLE ALLAVE 50
** NAXIFILE 3 ALL 30.0 NAXIALL.FIL 25
** MAXIFILE 24 ALL 10.0 MAXIALL.FIL 25
** POSTFILE 1 ALL INDIV POST2C.BIN 20
** POSTFILE PERIOD ALL PLOT PSTANALL.FIL 21
** Note that the following two input cards generate PLOTFILEs with the file
** unit dynamically allocated by the ISCST2 program. Uhen porting the model
** to another computer system, the user may need to specify the file units
** as is done on the previous four input cards.
** PLOTFILE 3 ALL 2ND PLT03ALL.FIL
** PLOTFILE 24 ALL 2ND PLT24ALL.FIL
**OU PLOTFILE 1 ALL FIRST OFFSITE.PL1
OU PLOTFILE 1 ALL FIRST OFFSITE.1
OU PLOTFILE 3 ALL FIRST OFFSITE.3 ,
OU PLOTFILE 24 ALL FIRST OFFSITE.24
OU PLOTFILE PERIOD ALL OFFSITE.ANN
OU FINISHED
*** Message Summary For ISC2 Model Setup ***
Summary of Total Messages
A Total of
A Total of
A Total of
0 Fatal Error Message(s)
1 Warning Message(s)
0 Informational Message(s)
Volume VII
Appendix VIM
External Review Draft
Do Not Cite or Quote
-------
FATAL ERROR MESSAGES
*** NONE ***
***••*•* WARNING MESSAGES
SO U320 17 PPARM : Source Parameter May Be Out-of-Range for Parameter OS
SETUP Finishes Successfully
External Review Draft
Appendix VII-4 Do Not Cite or Quote
-------
* ISCST2 (94227): WTI Truck Accident Off-Site, ISCOHDEP -• OFFSITE
* MODELING OPTIONS USED:
* CONC RURAL ELEV GRDRIS NOSTD
PLOT FILE OF HIGH 1ST HIGH 1-HR
936 RECEPTORS.
(,F8.2,3X,J
CONC
0.26880
0.33598
0.36608
0.33730
0.34637
0.34860
0.57377
0.74484
1.46575
2.05302
12.61975
10.95565
3.79691
8.00698
7.59468
4.95435
4.70006
3.21313
2.67063
2.82567
1.94967
0.96299
0.74547
0.60941
0.40966
0.34829
0.26873
0.33691
0.37006
0.28694
0.28421
0.36934
0.51489
0.57323
0.72210
1.96807
7.70763
9.52555
6.95155
7.50002
7.13345
6.57642
5.47722
2.96731
2.47798
2.91211
2.52572
0.97345
0.76762
0.60601
0.50508
0.40785
0.28014
0.28716
VALUES FOR SOURCE GROUP: ALL
* FOR A
* FORMAT
* X
*
17.36482
34.72963
52.09445
69.45927
86.82409
104.18890
121.55373
138.91852
156.28337
173.64818
217.06021
260.47229
303.88428
347.29639
390.70837
434.12042
520.94452
694.59271
868.24084
1302.36133
1736.48169
2604.72241
3472.96313
5209.44531
6945.92627
8682.40820
34.20201
68.40403
102.60603
136.80806
171.01007
205.21207
239.41408
273.61615
307.81812
342.02011
427.52518
513.03021
598.53522
684.04022
769.54523
855.05035
1026.06042
1368.08057
1710.10071
2565.15112
3420.20142
5130.30176
6840.40283
10260.60450
13680.80570
17101.00590
50.00000
100.00000
Volume VII
Appendix VII-4
TOTAL OF 9J
: <3(1X,F13.!
Y
98.48077
196.96155
295.44235
393.92307
492.40384
590.88470
689.36542
787.84613
886.32697
984.80774
1231.00964
1477.21167
1723.41370
1969.61548
2215.81738
2462.01929
2954.42310
3939.23096
4924.03809
7386.05762
9848.07715
14772.11520
19696.15430
29544.23050
39392.30860
49240.38670
93.96926
187.93851
281.90778
375.87701
469.84631
563.81555
657.78491
751.75409
845.72339
939.69263
1174.61572
1409.53894
1644.46204
1879.38525
2114.30835
2349.23145
2819.07788
3758.77051
4698.46289
7047.69482
9396.92578
14095.38960
18793.85350
28190.77930
37587.70310
46984.63670
86.60254
173.20508
>,2X,A8,2X,A4)
ZELEV AVE
GRP
HIVAL
213.40
225.60
225.60
225.60
225.60
225.60
243.80
256.00
280.40
286.50
353.60
353.60
310.90
347.50
353.60
359.70
347.50
341.40
341.40
365.80
360.00
340.00
340.00
360.00
350.00
360.00
213.40
225.60
225.60
225.60
225.60
225.60
237.70
243.80
256.00
286.50
329.20
347.50
335.30
347.50
353.60
359.70
362.40
329.20
359.70
369.70
385.90
340.00
340.00
360.00
380.00
390.00
213.40
219.50
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL ,
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
External Review Draft
Do Not Cite or Quote
-------
150.00000
200.00000
250.00000
300.00000
350.00000
400.00000
' 450.00000
500.00000
625.00000
750.00000
875.00000
1000.00000
1125.00000
1250.00000
1500.00000
2000.00000
2500.00000
3750.00000
5000.00000
7500.00000
10000.00000
15000.00000
20000.00000
25000.00000
64.27876
128.55754
192.83627
257.11508
321.39377
385.67258
449.95132
514.23016
578.50885
642.78766
803.48456
964.18140
1124.87830
1285.57520
1446.27197
1606.96912
1928.36292
2571.15039
3213.93799
4820.90625
6427.87549
9641.81250
12855.75200
19283.62700
25711.50390
32139.37890
76.60445
153.20888
229.81335
306.41779
383.02225
459.62671
536.23120
612.83557
689.44000
766.04443
957.55554
1149.06665
1340.57764
Volume VE
Appendix VTJ-4
259.80762
346.41016
433.01273
519.61517
606.21777
692.82031
779.42291
866.02539
1082.53174
1299.03821
1515.54443
1732.05090
1948.55713
2165.06348
2598.07617
3464.10156
4330.12695
6495.19043
8660.25391
12990.38090
17320.50780
25980.76170
34641.01560
43301.26560
76.60445
153.20888
229.81335
306.41779
383.02225
459.62671
536.23120
612.83557
689.44000
766.04443
957.55554
1149.06665
1340.57764
1532.08899
1723.59998
1915.11108
2298.13330
3064.17798
3830.22192
5745.33301
7660.44434
11490.66600
15320.88870
22981.33400
30641.77730
38302.22270
64.27876
128.55754
192.83629
257.11508
321.39377
385.67261
449.95132
514.23016
578.50885
642.78766
803.48456
964.18140
1124.87830
0.35662
0.32557
0.29595
0^250 ~"
0.40863
0.52095
0.61621
0.69656
0.52869
7.05143
8.60613
7.51029
6.75558
4.36960
3.28977
3.88733
3.04323
2.02383
1.50030
0.63818
0.57857
0.39186
0.26915
0.22724
0.29348
0.25689
0.31493
0.34678
0.31477
0.29315
0.34602
0.36397
0.45102
0.66126
1.25427
8.61035
8.66311
6.78554
6.10540
4.98055
4.01522
3.70575
2.90410
1.98154
1.47763
0.85381
0.62720
0.69921
0.32790
0.25307
0.30847
0.22848
0.24067
0.30236
0.34634
0.34414
0.32472
0.28523
0.43696
0.35947
0.39340
5.49557
7.44629
225.60
225.60
225.60
225.60
225.60
231.60
243.80
262.10
225.60
347.50
359.70
353.60
353.60
329.20
323.10
361.20
366.70
378.00
396.20
320.00
360.00
380.00
370.00
400.00
213.40
213.40
225.60
225.60
225.60
225.60
225.60
225.60
225.60
243.80
280.40
353.60
361.50
353.60
353.60
353.60
335.30
353.90
353.00
378.00
398.40
376.00
380.00
360.00
420.00
420.00
213.40
207.30
213.40
219.50
219.50
219.50
219.50
219.50
225.60
219.50
219.50
323.10
353.60
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL ,
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
External Review Draft
Do Not Cite or Quote
-------
1532.08899
1723.59998
1915.11108
2298.13330
3064.17798
3830.22192
5745.33301
7660.44434
11490.66600
15320.88870
22981.33400
30641.77730
38302.22270
86.60254
173.20508
259.80762
346.41016
433.01273
519.61517
606.21777
692.82031
779.42291
866.02539
1082.53174
1299.03821
1515.54443
1732.05090
1948.55725
2165.06348
2598.07617
3464.10156
4330.12695
6495.19043
8660.25391
12990.38090
17320.50780
25980.76170
34641.01560
43301.26560
93.96926
187.93851
281.90778
375.87701
469.84631
563.81555
657.78491
751.75409
845.72333
939.69263
1174.61572
1409.53894
1644.46204
1879.38525
2114.30835
2349.23145
2819.07788
3758.77051
4698.46289
7047.69482
9396.92578
14095.38960
18793.85350
28190.77930
Volume Vn
Appendix VTJ-4
1285.57520
1446.27197
1606.96912
1928.36292
2571.15039
3213.93799
4820.90674
6427.87549
9641.81348
12855.75200
19283.62700
25711.50390
32139.38090
50.00000
99.99999
150.00000
199.99997
249.99997
300.00000
349.99994
399.99994
449.99994
499.99994
625.00000
750.00000
875.00000
1000.00000
1125.00000
1250.00000
1500.00000
2000.00000
2499.99976
3749.99976
4999.99902
7499.99902
9999.99902
14999.99900
19999.99800
24999.99800
34.20201
68.40403
102.60603
136.80806
171.01007
205.21207
239.41411
273.61615
307.81815
342.02011
427.52518
513.03021
598.53528
684.04022
769.54535
855.05035
1026.06042
1368.08057
1710.10071
2565.15112
3420.20142
5130.30176
6840.40283
10260.60450
6.75017
5.10144
5.28185
474X971
3.21061
2.39247
1.90956
1.52773
0.80456
0.64297
0.42405
0.39759
0.30839
0.32474
0.25609
0.24736
0.21004
0.24833
0.33927
0.37314
0.38559
0.38621
0.41852
0.45109
0.50349
1.20829
1.68499
2*95695
3.68385
2.79491
2.46894
3.16175
2.47585
1.82327
1.13814
0.73721
0.50751
0.40480
0.32852
0.33624
0.28222
0.22933
0.26756
0.32014
0.32257
0.32209
0.38282
0.39198
0.41010
0.44700
0.44691
0.43843
0.41389
0.40746
0.59610
0.53807
1.90567
3.83804
2.51031
1.70149
1.00714
0.81427
0.61590
353.60
335.30
347.50
" 347.50
341.40
335.30
373.10
396.20
360.00
380.00
380.00
420.00
420.00
213.40
207.30
207.30
201.20
207.30
213.40
213.40
213.40
213.40
219.50
225.60
219.50
243.80
292.60
310.90
323.10
317.00
323.10
359.70
378.90
408.70
380.00
360.00
380.00
380.00
420.00
207.30
201.20
202.70
202.70
207.30
207.30
207.30
213.40
213.40
213.40
213.40
213.40
213.40
213.40
213.40
231.60
231.60
310.90
384.00
384.00
370.30
360.00
380.00
400.00
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
.ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL ,
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
External Review Draft
Do Not Cite or Quote
-------
37587.70310
46984.63670
98.48077
196.96155
295.44235
393.92307
492.40384
590.88470
689.36542
787.84613
886.32697
984.80774
1231.00964
1477.21167
1723.41370
1969.61548
2215.81738
2462.01929
2954.42310
3939.23096
4924.03809
7386.05762
9848.07715
14772.11520
19696.15430
29544.23050
39392.30860
49240.38670
100.00000
200.00000
300.00000
400.00000
500.00000
600.00000
700.00000
800.00000
900.00000
1000.00000
1250.00000
1500.00000
1750.00000
2000.00000
2250.00000
2500.00000
3000.00000
4000.00000
5000.00000
7500.00000
10000.00000
15000.00000
20000.00000
30000.00000
40000.00000
50000.00000
98.48077
196.96155
295.44235
393.92307
492.40384
590.88470
689.36542
787.84613
886.32697
Volume VII
Appendix VII-4
13680.80570
17101.00780
17.36482
34.72964
52.09447
69.45930
86.82410
104.18893
121.55376
138.91856
156.28340
173.64821
217.06027
260.47235
303.88434
347.29648
390.70850
434.12051
520.94470
694.59296
868.24103
1302.36169
1736.48218
2604.72290
3472.96411
5209.44580
6945.92822
8682.41113
0.00001
0.00002
0.00002
0.00003
0.00004
0.00005
0.00005
0.00006
0.00007
0.00008
0.00009
0.00011
0.00013
0.00015
0.00017
0.00019
0.00023
0.00030
0.00038
0.00057
0.00075
0.00113
0.00151
0.00226
0.00302
0.00377
-17.36482
-34.72964
-52.09446
-69.45927
-86.82410
-104.18891
-121.55373
-138.91853
-156.28339
0.51459
0.43678
0.35359
031369-
0.26612
0.25329
0.29654
0.33247
0.36039
0.38045
0.39332
0.39995
0.39583
0.38275
0.42299
0.39281
0.37818
0.67194
1.50775
3.14562
3.31588
2.59716
1.71830
0.62321
0.73195
0.50496
0.36129
0.29837
0.37070
0.34405
0.30541
0.26293
0.22294
0.23606
0.25777
0.27584
0.29033
0.30148
0.62002
4.91194
2.94301
4.05619
1.53264
0.95428
1.49695
3.21661
4.47226
t. 55106
1.87059
1.00112
0.75303
0.58147
0.46521
0.28991
0.38699
0.37283
0.34232
0.30411
0.26565
0.23660
0.26201
0.37834
0.43138
360.00
400.00
207.30
202.70
202.70
202.70
202.70
202.70
202.70
202.70
202.70
202.70
202.70
202.70
213.40
207.30
207.30
231.60
304.80
346.60
365.80
384.00
371.90
320.00
360.00
380.00
380.00
400.00
207.30
202.70
202.70
202.70
202.70
202.70
202.70
202.70
202.70
202.70
243.80
341.40
323.10
341.40
304.80
292.60
310.90
359.70
402.30
347.50
380.10
360.00
360.00
380.00
400.00
360.00
207.30
202.70
202.70
202.70
202.70
202.70
202.70
219.50
225.60
1-HR ALL
1-HR ALL
1-HR ALL
1-HR ALL
1-HR ALL
1-HR ALL
1-HR ALL
1-HR ALL
1-HR ALL
1-HR ALL
1-HR ALL
1-HR ALL
1-HR ALL
1-HR ALL
1-HR ALL
1-HR ALL
1-HR ALL
1-HR ALL
1-HR ALL
1-HR ALL
1-HR ALL
1-HR ALL
1-HR ALL
1-HR ALL
1-HR ALL
1-HR ALL
1-HR ALL
1-HR ALL
1-HR ALL
1-HR ALL
1-HR ALL
1-HR ALL
1-HR ALL
1-HR ALL
1-HR ALL
1-HR ALL
1-HR ALL
1-HR ALL
1-HR ALL
1-HR ALL
1-HR ALL
1-HR ALL
1-HR ALL
1-HR ALL
1-HR ALL
1-HR ALL
1-HR ALL
1-HR ALL
1-HR ALL ,
1-HR ALL
1-HR ALL
1-HR ALL
1-HR ALL
1-HR ALL
1-HR ALL
1-HR ALL
1-HR ALL
1-HR ALL
1-HR ALL
1-HR ALL
1-HR ALL
1-HR ALL
1-HR ALL
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
External Review Draft
Do Not Cite or Quote
-------
984.80774
1231.00964
1477.21167
1723.41370
1969.61548
2215.81738
2462.01929
2954.42310
3939.23096
4924.03809
7386.05762
9848.07715
14772.11520
19696.15430
29544.23050
39392.30860
49240.38670
93.96926
187.93851
281.90778
375.87701
469.84631
563.81555
657.78491
751.75409
845.72339
939.69263
1174.61584
1409.53894
1644.46216
1879.38525
2114.30835
2349.23145
2819.07788
3758.77051
4698.46338
7047.69482
9396.92676
14095.38960
18793.85550
28190.77930
37587.70700
46984.63670
86.60254
173.20508
259.80762
346.41016
433.01273
519.61517
606.21777
692.82031
779.42291
866.02539
1082.53174
1299.03821
1515.54443
1732.05090
1948.55713
2165.06348
2598.07617
3464.10156
4330.12695
6495.19043
Volume VII
Appendix VII-4
-173.64819
-217.06023
-260.47232
-303.88431
-347.29642
-390.70840
-434.12045
-520.94458
-694.59277
-868.24091
-1302.36145
-1736.48181
-2604.72290
-3472.96338
-5209.44580
-6945.92676
-8682.40918
-34.20201
-68.40402
-102.60603
-136.80804
-171.01006
-205.21207
-239.41406
-273.61612
-307.81812
-342.02008
-427.52515
-513.03021
-598.53522
-684.04016
-769.54523
-855.05023
-1026.06030
-1368.08032
-1710.10059
-2565.15088
-3420.20093
-5130.30127
-6840.40234
-10260.60350
-13680.80470
-17101.00590
-50.00000
-100.00001
-150.00002
-200.00002
-250.00003
-300.00003
-350.00003
-400.00003
-450.00003
-500.00006
-625.00006
-750.00006
-875.00006
-1000.00012
-1125.00012
-1250.00012
-1500.00012
-2000.00024
-2500.00024
-3750.00049
4.76881
6.27329
6.16611
2194307-
4.09769
3.76287
2.30627
3.32791
2.86217
3.90679
1.72526
1.47350
0.76150
0.90514
0.58147
0.42380
0.35992
0.40190
0.39868
0.37433
0.33824
0.29924
0.32718
0.56942
1.97247
1.05365
4.18020
6.32271
5.63219
2.16176
5.05036
4.39445
3.88288
3.34770
2.54836
2.59361
1.64010
1.56278
0.89712
0.60835
0.49872
0.41280
0.35222
0.41493
0.42042
0.39936
0.36209
0.34550
0.52975
3.67296
8.20457
8.61100
7.31127
2.32594
6.84067
4.02515
5.52586
5.03001
3.93320
4.15538
3.02563
2.29373
1.99081
329.20
347.50
353.60
323.10
341.40
341.40
323.10
347.50
353.60
386.50
353.60
360.00
340.00
380.00
380.00
380.00
400.00
207.30
202.70
202.70
202.70
202.70
213.40
256.00
298.70
286.50
323.10
347.50
347.50
310.90
353.60
350.20
347.50
347.50
345.90
371.90
365.80
408.40
380.00
360.00
360.00
360.00
360.00
207.30
202.70
202.70
202.70
213.40
268.20
317.00
347.50
353.60
347.50
310.90
359.70
335.30
359.70
359.70
347.50
365.80
359.70
353.60
402.30
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL,
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
External Review Draft
Do Not Cite or Quote
-------
8660.25391
12990.38090
17320.50780
25980.76170
34641.01560
43301.26560
76.60445
153.20888
229.81332
306.41779
383.02225
459.62668
536.23108
612.83557
689.44000
766.04443
957.55554
1149.06665
1340.57764
1532.08899
1723.59998
1915.11108
2298.13330
3064.17796
3830.22192
5745.33252
7660.44434
11490.66500
15320.88870
22981.33200
30641.77730
38302.22270
64.27876
128.55754
192.83629
257.11508
321.39377
385.67261
449.95132
514.23016
. 578.50885
642.78766
803.48456
964.18146
1124.87830
1285.57520
1446.27197
1606.96912
1928.36292
2571.15039
3213.93799
4820.90674
6427.87549
9641.81348
12855.75200
19283.62700
25711.50390
32139.38090
50.00000
100.00001
150.00002
200.00002
250.00002
Volume VII
Appendix VTJ-4
-5000.00049
-7500.00098
-10000.00100
-15000.00200
-20000.00200
-25000.00200
-64.27876
-128.55754
-192.83629
-257.11508
-321.39377
-385.67261
-449.95132
-514.23016
-578.50885
-642.78766
-803.48462
-964.18146
-1124.87830
-1285.57520
-1446.27209
-1606.96924
-1928.36292
-2571.15039
-3213.93823
-4820.90674
-6427.87598
-9641.81348
-12855.75290
-19283.62700
-25711.50590
-32139.38090
-76.60445
-153.20888
-229.81332
-306.41779
-383.02225
-459.62668
-536.23108
-612.83557
-689.44000
-766.04443
-957.55554
-1149.06665
-1340.57764
-1532.08899
-1723.59998
-1915.11108
-2298.13330
-3064.17798
-3830.22192
-5745.33301
-7660.44434
-11490.66600
-15320.88870
-22981.33400
-30641.77730
-38302.22270
-86.60254
-173.20508
-259.80762
-346.41016
-433.01273
1.42519
0.83092
0.60556
0.33&25
0.24605
0.19235
0.42561
0.43716
0.41605
0.37383
0.49189
1.79875
4.64597
9.38023
8.82994
8.33411
7.29032
7.00924
4.69202
5.23867
4.77284
3.16810
3.33343
2.56669
2.06776
2.03090
1.48196
0.83548
0.52174
0.37065
0.30105
0.24722
0.43359
0.44835
0.42392
0.37336
0.57794
2.43991
3.02561
4.53357
5.22348
4.11713
6.00279
5.92884
2.83832
4.79220
3.50451
3.65866
5.16026
3.89373
2.27250
1.72043
1.24257
0.51671
0.53830
0.35506
0.25348
0.18634
0.43858
0.45374
0.42329
0.40890
0.84558
396.20
380.00
380.00
-360.00
360.00
360.00
207.30
202.70
202.70
202.70
243.80
298.70
323.10
353.60
353.60
353.60
353.60
359.70
341.40
353.60
353.60
341.40
359.70
359.70
359.70
408.40
408.40
380.00
360.00
360.00
360.00
360.00
207.30
202.70
202.70
202.70
268.20
304.80
310.90
323.10
329.20
323.10
347.50
359.70
329,20
359.70
353.60
359.70
408.40
420.60
371.90
392.00
390.10
340.00
380.00
400.00
400.00
380.00
207.30
202.70
202.70
213.40 1
268.20 1
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
•HR
-HR
-HR
-HR
-HR
-HR
-HR
-HR
-HR
-HR
-HR
-HR
-HR
-HR
-HR
-HR
-HR
-HR
-HR
-HR
-HR
-HR
-HR
-HR
-HR
-HR
-HR
-HR
-HR
-HR
-HR
-HR
-HR
-HR
-HR
-HR
-HR
-HR
-HR
-HR
-HR
-HR
-HR
-HR
-HR
-HR
-HR
-HR
-HR
-HR
-HR
1-HR
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL ,
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
External Review Draft
Do Not Cite or Quote
-------
300.00003
350.00003
400.00003
450.00003
500.00003
625.00006
750.00006
875.00006
1000.00006
1125.00012
1250.00012
1500.00012
2000.00012
2500.00024
3750.00024
5000.00049
7500.00049
10000.00100
15000.00100
20000.00200
25000.00200
34.20202
68.40405
102.60606
136.80809
171.01012
205.21213
239.41414
273.61621
307.81821
342.02023
427.52527
513.03033
598.53546
684.04047
769.54547
855.05054
1026.06079
1368.08081
1710.10107
2565.15161
3420.20190
5130.30273
6840.40430
10260.60550
13680.80860
17101.01170
17.36483
34.72966
52.09449
69.45933
86.82413
104.18897
121.55380
138.91862
156.28346
173.64827
217.06036
260.47244
303.88449
347.29657
390.70868
434.12073
Volume VH
Appendix VTJ-4
-519.61517
-606.21777
-692.82031
-779.42291
-866.02539
-1082.53174
-1299.03821
-1515.54443
-1732.05090
-1948.55713
-2165.06348
-2598.07617
-3464.10156
-4330.12695
-6495.19043
-8660.25391
-12990.38090
-17320.50780
-25980.76170
-34641.01560
-43301.26560
-93.96926
-187.93851
-281 .90778
-375.87701
-469.84631
-563.81555
-657.78479
-751.75409
-845.72333
-939.69257
-1174.61572
-1409.53894
-1644.46204
-1879.38513
-2114.30835
-2349.23145
-2819.07788
-3758.77026
-4698.46289
-7047.69434
-9396.92578
-14095.38870
-18793.85350
-28190.77730
-37587.70310
-46984.62890
-98.48077
-196.96155
-295.44235
-393.92307
-492.40384
-590.88470
*XAQ 36542
-787.84613
-886.32697
-984.80774
-1231.00964
-1477.21143
-1723.41370
-1969.61548
-2215.81738
-2462.01929
1.88338
3.12102
4.47822
3.44037-
3.99676
1.15026
3.60656
3.27483
4.40008
4.42819
4.40581
4.58552
3.37671
2.77139
1.79060
1.28702
0.51393
0.47360
0.43799
0.29078
0.24275
0.44039
0.45331
0.41498
0.42574
1.00140
1.42446
1.89658
1.81961
0.56008
0.54460
1.26652
1.47459
1.08083
2.65939
4.18575
4.83353
4.71148
3.58915
3.00845
1.84514
1.42660
0.57411
0.42987
0.44024
0.29190
0.24473
0.43894
0.44718
0.41836
0.42576
0.95598
0.80975
0.59230
0.55650
0.60195
0.58568
1.00867
1.21439
1.12251
0.81909
0.77251
4.30240
298.70
310.90
323.10
323.10
329.20
298.70
341.40
341.40
359.70
365.80
371.90
408.40
420.60
408.40
408.40
396.20
340.00
360.00
420.00
400.00
400.00
207.30
202.70
202.70
207.30
268.20
292.60
304.80
304.80
286.50
286.50
304.80
310.90
304.80
335.30
359.70
378.00
396.20
402.30
411.50
402.30
408.10
360.00
360.00
420.00
400.00
420.00
207.30
202.70
202.70
202.70
249.90
286.50
280.40
274.30
286.50
286.50
298.70
304.80
304.80
298.70
298.70
365.80
-HR
-HR
-HR
-HR
-HR
-HR
-HR
-HR
-HR
-HR
-HR
-HR
-HR
-HR
-HR
-HR
-HR
-HR
-HR
-HR
-HR
-HR
-HR
-HR
-HR
-HR
-HR
-HR
-HR
-HR
-HR
-HR
-HR
-HR
-HR
-HR
-HR
-HR
-HR
-HR
-HR
-HR
1-HR
1-HR
-HR
-HR
-HR
-HR
-HR
-HR
-HR
-HR
-HR
-HR
-HR
-HR
-HR
-HR
-HR
-HR
-HR
-HR
J-HR
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL ,
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
External Review Draft
Do Not Cite or Quote
-------
520.94489
694.59320
868.24146
1302.36230
1736.48279
2604.72412
3472.96558
5209.44824
6945.93115
8682.41504
0.00002
0.00003
0.00005
0.00006
0.00008
0.00009
0.00011
0.00012
0.00014
0.00015
0.00019
0.00023
0.00026
0.00030
0.00034
0.00038
0.00045
0.00060
0.00075
0.00113
0.00151
0.00226
0.00302
0.00453
0.00604
0.00755
-17.36482
-34.72964
-52.09447
-69.45930
-86.82410
-104.18893
-121.55376
-138.91856
-156.28340
-173.64821
-217.06029
-260.47238
-303.88437
-347.29648
-390.70853
-434.12054
-520.94470
-694.59296
-868.24115
-1302.36182
-1736.48218
-2604.72314
-3472.96436
-5209.44629
-6945.92871
-8682.41113
-34.20201
Volume VH
Appendix VII-4
-2954.42285
-3939.23096
-4924.03809
-7386.05762
-9848.07715
-14772.11520
-19696.15430
-29544.23050
-39392.30860
-49240.38670
-100.00000
-200.00000
-300.00000
-400.00000
-500.00000
-600.00000
-700.00000
-800.00000
-900.00000
-1000.00000
-1250.00000
-1500.00000
-1750.00000
-2000.00000
-2250.00000
-2500.00000
-3000.00000
-4000.00000
-5000.00000
-7500.00000
-10000.00000
-15000.00000
-20000.00000
-30000.00000
-40000.00000
-50000.00000
-98.48077
-196.96155
-295.44235
-393.92307
-492.40384
-590.88470
-689.36542
-787.84613
-886.32697
-984.80774
-1231.00964
-1477.21167
-1723.41370
-1969.61548
-2215.81738
-2462.01929
-2954.42310
-3939.23096
-4924.03809
-7386.05762
-9848.07715
-14772.11520
-19696.15430
-29544.23050
-39392.30860
-49240.38670
-93.96926
4.96976
3.15816
3.16511
1.97938-
1.33800
0.72961
0.64221
0.42567
0.30186
0.24893
0.43421
0.43548
0.41014
0.41080
0.39143
0.65616
0.59292
0.57072
0.44840
1.15070
1.38798
1.27150
1.04510
0.56915
0.67898
3.83824
5.07416
4.70300
3.72727
2.34163
1.65182
1.00042
0.64804
0.56711
0.44071
0.33106
0.42628
0.41834
0.38521
0.37631
0.31955
0.37408
0.57250
0.51230
0.25795
0.89245
1.47436
0.68115
0.63180
0.55796
1.62834
6.01295
6.88369
4.99100
5.23266
3.62055
2.56038
1.33527
0.80047
0.51337
0.43789
0.41517
0.42530
402.30 1
390.10 1
414.50 1
'4108.40 1
398.10 1
380.00 1
360.00 1
400.00 1
400.00 1
400.00 1
207.30 1
202.70 1
202.70 1
202.70 1
219.50 1
274.30 1
280.40 1
274.30 1
243.80 1
298.70 1
304.80 1
304.80 1
304.80 1
292.60 1
298.70 1
365.80 1
406.30 1
402.30 1
396.20 1
390.10 1
396.20 1
380.00 1
360.00 1
380.00 1
380.00 1
400.00
207.30
202.70
202.70
202.70
202.70
225.60
274.30
274.30
237.70
292.60
304.80
286.50
292.60
280.40
304.80
353.60
384.00
396.20
415.40
390.10
392.00
360.00
340.00
340.00
360.00
380.00
213.40
-MR
-MR
-HR
-HR
-HR
-HR
-HR
-HR
-HR
•HR
-HR
-HR
-HR
-HR
-HR
-HR
-HR
-HR
-HR
-HR
-HR
-HR
-HR
-HR
-HR
-HR
-HR
-HR
-HR
-HR
-HR
-HR
-HR
-HR
-HR
-HR
-HR
-HR
-HR
-HR
-HR
-HR
-HR
-HR
-HR
-HR
-HR
-HR
-HR
-HR
-HR
-HR
-HR
-HR
-HR
-HR
-HR
-HR
-HR
-HR
-HR
1-HR
1-HR
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL r
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
External Review Draft
Do Not Cite or Quote
-------
-68.40403
-102.60605
-136.80806
-171.01009
-205.21210
-239.41411
' -273.61615
-307.81815
-342.02014
-427.52521
-513.03021
-598.53528
-684.04034
-769.54535
-855.05042
-1026.06042
-1368.08069
-1710.10083
-2565.15112
-3420.20142
-5130.30176
-6840.40332
-10260.60450
-13680.80660
-17101.00780
-50.00000
-100.00000
-150.00000
-200.00000
-250.00000
-300.00000
-350.00000
-400.00000
-450.00000
-500.00000
-625.00000
-750.00000
-875.00000
-1000.00000
-1125.00000
-1250.00000
-1500.00000
-2000.00000
-2500.00000
-3750.00000
-5000.00000
-7500.00000
-10000.00000
-15000.00000
-20000.00000
-25000.00000
-64.27876
-128.55753
-192.83627
-257.11505
-321.39377
-385.67258
-449.95129
-514.23010
-578.50873
-642.78766
-803.48456
-964.18134
Volume VII
Appendix VTJ-4
-187.93851
-281.90778
-375.87701
-469.84631
-563.81555
-657.78491
-751.75409
-845.72333
-939.69263
-1174.61572
-1409.53894
-1644.46204
-1879.38525
-2114.30835
-2349.23145
-2819.07788
-3758.77051
-4698.46289
-7047.69482
-9396.92578
-14095.38960
-18793.85350
-28190.77930
-37587.70310
-46984.62890
-86.60254
-173.20508
-259.80762
-346.41016
-433.01273
-519.61517
-606.21777
-692.82031
-779.42291
-866.02539
-1082.53174
-1299.03821
-1515.54443
-1732.05090
-1948.55713
-2165.06348
-2598.07617
-3464.10156
-4330.12695
-6495.19043
-8660.25391
-12990.38090
-17320.50780
-25980.76170
-34641.01560
-43301.26560
-76.60445
-153.20888
-229.81335
-306.41779
-383.02228
-459.62671
-536.23120
-612.83557
-689.44000
-766.04449
-957.55560
-1149.06689
0.39598
0.34401
0.32278
0.2*914
0.21915
0.24554
0.33595
0.21976
0.61132
0.70153
0.71219
0.60392
0.39741
1.32031
6.41596
9.63020
7.83263
6.07217
3.64463
2.56743
1.10097
0.80734
0.60040
0.46494
0.35528
0.41205
0.36889
0.28972
0.25468
0.19106
0.20399
0.14085
0.14063
0.16760
0.19979
0.30762
0.25293
0.47151
0.68794
0.68386
1.31733
8.69092
8.28013
6.06948
2.34506
2*29909
1.08108
0.92917
0.50187
0.36425
0.31747
0.39648
0.33797
0.24396
0.19603
0.18121
0.18109
0.11973
0.10332
0.14028
0.20883
0.21102
0.37988
202.70
202.70
202.70
-202.70
202.70
219.50
249.90
219.50
280.40
280.40
280.40
280.40
262.10
298.70
353.60
371.90
402.30
397.20
384.00
384.00
340.00
340.00
360.00
380.00
380.00
213.40
202.70
202.70
202.70
202.70
202.70
202.70
202.70
202.70
219.50
219.50
213.40
213.40
231.60
231.60
292.60
359.70
396.20
414.50
396.20
392.60
360.00
380.00
360.00
360.00
380.00
213.40
202.70
202.70
202.70
202.70
202.70
202.70
202.70
202.70
202.70 1
202.70 1
213.40 1
1-HR
1-HR
1-HR
-HR
-HR
-HR
-HR
-HR
-HR
-HR
-HR
-HR
-HR
-HR
-HR
-HR
-HR
-HR
-HR
-HR
-HR
-HR
-HR
-HR
-HR
-HR
-HR
-HR
-HR
-HR
-HR
-HR
-HR
-HR
-HR
-HR
-HR
-HR
-HR
-HR
-HR
-HR
-HR
-HR
-HR
-HR
-HR
-HR
-HR
-HR
-HR
-HR
-HR
-HR
-HR
-HR
-HR
-HR
-HR
-HR
-HR
-HR
-HR
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
.ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL ,
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
External Review Draft
Do Not Cite or Quote
-------
-1124.87830
-1285.57520
-1446.27185
-1606.96912
-1928.36279
-2571.15039
-3213.93774
-4820.90625
-6427.87500
-9641.81250
-12855.75100
-19283.62700
-25711.50200
-32139.37890
-76.60445
-153.20891
-229.81339
-306.41782
-383.02231
-459.62674
-536.23120
-612.83563
-689.44006
-766.04456
-957.55566
-1149.06689
-1340.57800
-1532.08911
-1723.60022
-1915.11121
-2298.13354
-3064.17847
-3830.22241
-5745.33350
-7660.44531
-11490.66700
-15320.89060
-22981.33590
-30641.78130
-38302.22660
-86.60255
-173.20509
-259.80765
-346.41019
-433.01276
-519.61530
-606.21783
-692.82037
-779.42297
-866.02551
-1082.53186
-1299.03833
-1515.54456
-1732.05090
-1948.55725
-2165.06372
-2598.07666
-3464.10181
-4330.12744
-6495.19092
-8660.25488
-12990.38180
-17320.50980
Volume VII
Appendix VTJ-4
-1340.57788
-1532.08899
-1723.60010
-1915.11121
-2298.13354
-3064.17822
-3830.22241
-5745.33301
-7660.44482
-11490.66600
-15320.88960
-22981.33400
-30641.77930
-38302.22270
-64.27876
-128.55751
-192.83624
-257.11499
-321.39371
-385.67252
-449.95123
-514.22998
-578.50867
-642.78754
-803.48444
-964.18115
-1124.87830
-1285.57483
-1446.27173
-1606.96887
-1928.36243
-2571.15015
-3213.93750
-4820.90576
-6427.87451
-9641.81250
-12855.75000
-19283.62500
-25711.50000
-32139.37700
-49.99999
-99.99998
-149.99997
-199.99994
-249.99994
-299.99991
-349.99991
-399.99988
-449.99988
-499.99988
-624.99988
-749.99988
-874.99982
-999.99982
-1124.99976
-1249.99976
-1499.99976
-1999.99963
-2499.99951
-3749.99927
-4999.99854
-7499.99805
-9999.99805
0.42113
0.33151
0.21041
072&507 ~~
10.92368
6.12952
5.59288
3.39607
2.09512
0.95523
0.79460
0.50451
0.41394
0.28435
0.37915
0.30194
0.24334
0.24787
0.15675
0.15750
0.09817
0.08347
0.19057
0.21027
0.33033
0.22863
0.08610
0.12589
0.16390
0.33260
2.51318
4.78648
5.21950
2.99722
2.12744
1.21761
1.04816
0.70586
0.49958
0.35612
0.36072
0.30806
0.30228
0.23202
0.19677
0.20100
0.11360
0.12402
0.20287
0.23053
0.29869
0.68257
5.80748
2.85526
1.02760
0.47127
0.61170
6.05994
5.13877
3.36742
2.81302
1.22740
1.05474
213.40
213.40
213.40
213.40
371.90
378.00
396.20
396.20
378.00
349.00
360.00
360.00
380.00
360.00
213.40
201.20
207.30
207.30
202.70
202.70
202.70
202.70
207.30
207.30
207.30
207.30
207.30
213.40
213.40
256.00
323.10
359.70
384.00
378.00
378.00
360.00
380.00
400.00
400.00
380.00
213.40
213.40
213.40
207.30
213.40
213.40
213.40
213.40
213.40
213.40
225.60
274.30
329.20
310.90
286.50
256.00
243.80
365.80
372.50
378.00
402.30
360.00
380.00
-HR
-HR
-HR
-HR
-HR
-HR
-HR
-HR
-HR
-HR
-HR
-HR
-HR
-HR
1-HR
1-HR
-HR
-HR
-HR
-HR
-HR
-HR
-HR
-HR
-HR
-HR
-HR
-HR
-HR
-HR
-HR
-HR
-HR
-HR
-HR
-HR
-HR
-HR
-HR
-HR
1-HR
1-HR
1-HR
1-HR
-HR
-HR
-HR
-HR
-HR
-HR
-HR
-HR
-HR
-HR
-HR
-HR
-HR
-HR
1-HR
1-HR
1-HR
1-HR
1-HR
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
External Review Draft
Do Not Cite or Quote
-------
-25980.76370
-34641.01950
-43301.27340
-93.96926
-187.93851
-281.90778
-375.87701
-469.84631
-563.81561
-657.78491
. -751.75409
-845.72339
-939.69263
-1174.61584
-1409.53894
-1644.46216
-1879.38525
-2114.30835
-2349.23145
-2819.07788
-3758.77051
-4698.46338
-7047.69482
-9396.92676
-14095.38960
-18793.85550
-28190.77930
-37587.70700
-46984.63670
-98.48077
-196.96155
-295.44235
-393.92307
-492.40384
-590.88470
-689.36542
-787.84613
-886.32697
-984.80774
-1231.00964
-1477.21167
-1723.41370
-1969.61548
-2215.81738
-2462.01929
-2954.42310
-3939.23096
-4924.03809
-7386.05762
-9848.07715
-14772.11520
-19696.15430
-29544.23050
-39392.30860
-49240.38670
-100.00000
-200.00000
-300.00000
-400.00000
-500.00000
-600.00000
-700.00000
-800.00000
Volume VII
Appendix VII-4
-14999.99710
-19999.99610
-24999.99410
-34.20201
-68.40401
-102.60602
-136.80803
-171.01004
-205.21204
-239.41403
-273.61609
-307.81805
-342.02008
-427.52509
-513.03009
-598.53516
-684.04016
-769.54517
-855.05017
-1026.06030
-1368.08020
-1710.10022
-2565.15039
-3420.20044
-5130.30029
-6840.40137
-10260.60160
•13680.80270
-17101.00390
-17.36481
-34.72963
-52.09444
-69.45926
-86.82407
-104.18888
-121.55370
-138.91849
-156.28334
-173.64813
-217.06018
-260.47223
-303.88422
-347.29630
-390.70831
-434.12033
-520.94446
-694.59253
-868.24066
-1302.36096
-1736.48120
-2604.72192
-3472.96240
-5209.44385
-6945.92480
-8682.40625
0.00000
0.00000
0.00000
0.00000
0.00001
0.00001
0.00001
0.00001
0.65071
0.50114
0.38787
07S4193-
0.27758
0.30064
0.24210
0.23461
0.15763
0.08975
0.12425
0.16871
0.20034
23.57302
17.52369
10.52689
7.80677
11.15181
2.12495
0.85507
1.22027
4.52741
2.97962
3.34343
1.78258
1.37034
0.76916
0.58259
0.37647
0.32349
0.23298
0.26115
0.25437
0.18446
0.11117
0.08299
0.05333
0.17726
30.73858
39.06137
29.75858
24.42535
24.63006
18.22574
21.34521
11.89429
9.83305
7.30066
5.14316
2.16896
1.73067
1.37949
0.82775
0.60091
0.47073
0.30609
0.19980
0.18474
0.17931
0.15481
0.11702
0.04870
0.02153
380.00
400.00
360.00
213.40
213.40
213.40
213.40
213.40
213.40
213.40
219.50
219.50
213.40
353.60
353.60
341.40
335.30
353.60
304.80
243.80
298.70
359.70
365.80
402.30
380.00
400.00
380.00
400.00
360.00
213.40
213.40
213.40
213.40
213.40
213.40
213.40
219.50
225.60
310.90
359.70
359.70
365.80
371.90
353.60
371.90
353.60
365.80
365.80
390.10
339.90
360.00
380.00
420.00
400.00
400.00
213.40
213.40
213.40
213.40
213.40
213.40
213.40
213.40
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALLV
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
External Review Draft
Do Not Cite or Quote
-------
-900.00000
-1000.00000
-1250.00000
-1500.00000
-1750.00000
-2000.00000
-2250.00000
-2500.00000
-3000.00000
-4000.00000
-5000.00000
-7500.00000
-10000.00000
-15000.00000
-20000.00000
-30000.00000
-40000.00000
-50000.00000
-98.48077
-196.96155
-295.44235
-393.92307
-492.40364
-590.88470
-689.36542
-787.84613
-886.32697
-984.80774
-1231.00964
-1477.21167
-1723.41370
-1969.61548
-2215.81738
-2462.01929
-2954.42310
-3939.23096
-4924.03809
-7386.05762
-9848.07715
-14772.11520
- -19696.15430
-29544.23050
-39392.30860
-49240.38670
-93.96926
-187.93851
-281.90778
-375.87701
-469.84631
-563.81561
-657.78491
-751.75409
-845.72339
-939.69263
-1174.61584
-1409.53894
-1644.46216
-1879.38525
-2114.30835
-2349.23145
-2819.07788
-3758.77051
-4698.46338
Volume VH
Appendix VII-4
0.00001
0.00001
0.00001
0.00002
0.00002
0.00002
0.00003
0.00003
0.00004
0.00005
0.00006
0.00009
0.00012
0.00018
0.00024
0.00036
0.00048
0.00060
17.36481
34.72963
52.09445
69.45927
86.82407
104.18890
121.55371
138.91850
156.28336
173.64815
217.06020
260.47226
303.88428
347.29633
390.70834
434.12039
520.94452
694.59259
868.24072
1302.36133
1736.48157
2604.72241
3472.96289
5209.44482
6945.92578
8682.40820
34.20201
68.40401
102.60603
136.80803
171.01004
205.21204
239.41405
273.61609
307.81808
342.02008
427.52512
513.03021
598.53522
684.04016
769.54517
855.05017
1026.06030
1368.08020
1710.10034
0.61109
102.67791
11.27636
7.M968
18.61171
16.82258
26.26138
21.94983
16.40848
11.44995
7.90828
4.61813
2.85313
1.39252
1.22709
0.83216
0.58564
0.45712
0.29029
0.17685
0.17193
0.15816
0.11901
0.24290
0.09810
0.39948
1.11855
58.00135
23.04494
5.07005
2.77523
11.35851
17.64771
10.66911
11.35334
6.09606
6.66010
4.12978
2.94577
1.82016
1.31141
0.70949
0.50243
0.41544
0.27655
0.22452
0.22175
0.22916
0.32701
0.22276
1.55947
7.63906
6.42292
10.99466
15.03052
5.45310
4.21474
18.63396
21.22736
16.85374
12.63549
8.27160
6.06803
243.80
1-HR
298.70 1-HR
304.80
1-HR
-304.80 1-HR
335
341
371
371
371
.30
.40
.90
.90
.90
378.00
371
371
360
340
360
380
380
400
213
213
213
213
213
225
225
237
243
280
317
304
298
341
371
353
365
353
378
384
389
400
420
380
380
400
213
213
213
219
225
225
243
274
286
298
317
298
298
359
384
378
378
378
378
.90
.90
.00
.00
.00
.00
.00
-HR
-HR
-HR
-HR
-HR
-HR
-HR
-HR
-HR
-HR
-HR
-HR
-HR
.00 1-HR
.40 1-HR
.40 1-HR
.40 1-HR
.40 1-HR
.40 1-HR
.60 1-HR
.60 1-HR
.70 1-HR
.80 1-HR
.40
.00
.80
.70
.40
.90
.60
.80
.60
.00
.00
.20
.00
.00
.00
.00
.00
-HR
-HR
-HR
-HR
-HR
-HR
-HR
-HR
-HR
-HR
-HR
-HR
-HR
-HR
-HR
-HR
-HR
.40 1-HR
.40 1-HR
.40
.50
.60
.60
.80
.30
-HR
-HR
-HR
-HR
-HR
-HR
.50 1-HR
.70 1-HR
.00 1-HR
.70
.70
.70
.00
.00
.00
.00
.00
-HR
-HR
-HR
-HR
-HR
-HR
-HR
-HR
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL,
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST.
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
External Review Draft
Do Not Cite or Quote
-------
-7047.69482
-9396.92676
-14095.38960
-18793.85550
-28190.77930
-37587.70700
-46984.63670
-86.60255
-173.20509
-259.80765
-346.41019
-433.01276
-519.61530
-606.21783
-692.82037
-779.42297
-866.02551
-1082.53186
-1299.03833
-1515.54456
-1732.05090
-1948.55725
-2165.06372
-2598.07666
-3464.10181
-4330.12744
-6495.19092
-8660.25488
-12990.38180
-17320.50980
-25980.76370
-34641.01950
-43301.27340
-76.60445
-153.20891
-229.81335
-306.41782
-383.02228
-459.62671
-536.23120
-612.83563
-689.44006
-766.04449
-957.55566
-1149.06689
-1340.57788
-1532.08899
-1723.60022
-1915.11121
-2298.13354
-3064.17822
-3830.22241
-5745.33350
-7660.44531
-11490.66700
-15320.89060
-22981.33590
-30641.78130
-38302.22660
-64.27877
-128.55756
-192.83632
-257.11511
Volume VII
Appendix VU.-4
2565.15063
3420.20093
5130.30078
6840.40186
10260.60250
13680.80370
17101.00390
49.99999
99.99998
149.99997
199.99997
249.99994
299.99991
349.99991
399.99991
449.99991
499.99988
624.99988
749.99988
874.99988
999.99982
1125.00000
1249.99976
1499.99976
1999.99963
2499.99951
3749.99951
4999.99854
7499.99854
9999.99805
14999.99800
19999.99610
24999.99610
64.27876
128.55751
192.83626
257.11499
321.39374
385.67255
449.95126
514.22996
578.50873
642.78760
803.48444
964.18121
1124.87830
1285.57507
1446.27173
1606.96887
1928.36255
2571.15015
3213.93750
4820.90576
6427.87451
9641.81250
12855.75000
19283.62500
25711.50000
32139.37700
76.60442
153.20885
229.81332
306.41772
2.70285
2.30539
1.35730
0771762
0.53734
0.34155
0.29475
0.26518
0.24978
0.25725
0.52660
0.28145
0.50071
2.31977
12.56153
8.51044
5.98353
4.29002
11.30454
20.21211
21.06346
17.60012
16.60686
12.78313
8.07451
6.21558
3.60204
2.36595
1.48311
1.02835
0.58675
0.43252
0.35588
0.25639
0.24495
0.38743
0.38003
0.39852
0.69673
1.79918
9.03989
8.15023
7.73161
5.19352
14.63228
14.20238
16.35767
16.28965
15.55074
13.14836
6.27995
6.76263
3.83759
2.73596
1.39739
1.30532
0.79059
0.55817
0.38014
0.25132
0.37290
0.51027
0.37028
371.90
424.90
420.00
-360.00
400.00
380.00
400.00
213.40
213.40
219.50
231.60
225.60
231.60
268.20
304.80
310.90
304.80
292.60
323.10
359.70
371.90
371.90
378.00
378.00
378.00
384.00
384.00
426.70
400.00
400.00
420.00
400.00
350.00
213.40
213.40
225.60
231.60
225.60
231.60
268.20
304.80
316.40
317,00
304.80
341.40
353.60
365.80
371.90
378.00
384.00
359.70
384.00
378.00
379.20
360.00
400.00
400.00
400.00
370.00
213.40
225.60
231.60
231.60
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL *
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
External Review Draft
Do Not Cite or Quote
-------
-321.39383
-385.67267
-449.95 H2
-514.23022
-578.50897
-642.78772
' -803.48474
-964.18152
-1124.87854
-1285.57532
71446.27222
-1606.96936
-1928.36328
-2571.15088
-3213.93872
-4820.90771
-6427.87695
-9641 .81543
-12855.75490
-19283.63090
-25711.50980
-32139.38670
-50.00002
-100.00003
-150.00005
-200.00006
-250.00009
-300.00009
-350.00012
-400.00012
-450.00015
-500.00018
-625.00024
-750.00024
-875.00031
-1000.00037
-1125.00037
-1250.00049
-1500.00049
-2000.00073
-2500.00098
-3750.00122
-5000.00195
-7500.00244
-10000.00390
-15000.00490
-20000.00780
-25000.00780
-34.20204
-68.40408
-102.60610
-136.80815
-171.01018
-205.21220
-239.41423
-273.61633
-307.81833
-342.02036
-427.52545
-513.03052
-598.53571
-684.04065
-769.54584
Volume VII
Appendix VII-4
383.02216
459.62665
536.23102
612.83551
ooy«%39oo
766.04431
957.55542
1149.06653
1340.57751
1532.08862
1723.59973
1915.11084
2298.13306
3064.17749
3830.22144
5745.33203
7660.44336
11490.66410
15320.88670
22981.33010
30641.77340
38302.21880
86.60253
173.20506
259.80756
346.41013
433.01270
519.61517
606.21771
692.82025
779.42279
866.02533
1082.53162
1299.03784
1515.54431
1732.05066
1948.55701
2165.06323
2598.07593
3464.10132
4330.12646
6495.18994
8660.25293
12990.37990
17320.50590
25980.75980
34641.01170
43301.26170
93.96925
187.93851
281.90778
375.87698
469.84631
563.81555
657.78479
751.75403
845.72327
939.69257
1174.61572
1409.53894
1644.46191
1879.38513
2114.30811
0.38429
0.73814
1.48122
T^ttjiy?
f .i^OOrr
3.96963
4.83195
5.33894
13.79714
12.62711
10.85368
10.94782
10.99058
11.80894
8.64943
6.14799
3.76806
2.67099
1.66352
1.29685
0.78718
0.63766
0.57366
0.26007
0.35202
0.47222
0.42356
0.38405
1.12187
1.26270
0.76838
6.07096
2.61061
1.14350
6.37388
10.03524
9.18170
7.92651
9.35033
11.11055
7.92565
5.68018
3.04864
2.38825
1.32433
0.99726
0.52098
0.51678
0.40135
0.26499
0.34356
0.35157
0.33849
0.37139
0.97750
0.98373
2.66439
1.44381
2.72251
5.24013
11.87981
12.02114
10.61821
4.87317
225.60
231.60
274.30
-304.80
310.90
310.90
317.00
347.50
353.60
353.60
359.70
365.80
384.00
384.00
378.00
378.00
378.00
380.00
400.00
400.00
360.00
360.00
213.40
225.60
231.60
231.60
225.60
243.80
249.90
243.80
304.80
304.80
286.50
329.20
347.50
353.60
353.60
384.00
384.00
384.00
378.00
365.80
371.90
360.00
360.00
340.00
380.00
350.00
213.40
225.60
225.60
225.60
225.60
243.80
262.10
286.50
280.40
292.60
323.10
353.60
359.70
359.70
329.20
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL'
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
External Review Draft
Do Not Cite or Quote
-------
-855.05090
-1026.06104
-1368.08130
-1710.10181
-2565.15283
-3420.20337
-5130.30518
-6840.40674
-10260.61040
-13680.81450
-17101.01760
-17.36484
-34.72969
-52.09453
-69.45937
-86.82422
-104.18906
-121.55391
-138.91873
-156.28360
-173.64844
-217.06055
-260.47269
-303.88474
-347.29691
-390.70898
-434.12109
-520.94531
-694.59375
-868.24219
-1302.36353
-1736.48438
-2604.72656
-3472.96875
-5209.45264
-6945.93701
-8682.42188
-0.00003
-0.00006
-0.00009
-0.00012
-0.00015
-0.00018
-0.00021
-0.00024
-0.00027
-0.00030
-0.00038
-0.00045
-0.00053
-0.00060
-0.00068
-0.00075
-0.00091
-0.00121
-0.00151
-0.00226
-0.00302
-0.00453
-0.00604
-0.00906
-0.01208
-0.01510
Volume VH
Appendix VII-4
2349.23145
2819.07764
3758.77026
4698.46289
7047.69385
9396.92578
14095.38770
18793.85350
28190.77540
37587.70310
46984.62890
98.48077
196.96155
295.44235
393.92307
492.40381
590.88470
689.36542
787.84613
886.32697
984.80768
1231.00964
1477.21143
1723.41345
1969.61523
2215.81738
2462.01929
2954.42285
3939.23071
4924.03809
7386.05713
9848.07715
14772.11430
19696.15430
29544.22850
39392.30860
49240.38670
100.00000
200.00000
300.00000
400.00000
500.00000
600.00000
700.00000
800.00000
900.00000
1000.00000
1250.00000
1500.00000
1750.00000
2000.00000
2250.00000
2500.00000
3000.00000
4000.00000
5000.00000
7500.00000
10000.00000
15000.00000
20000.00000
30000.00000
40000.00000
50000.00000
6.00507
6.19100
5.26502
5.05579
1.51796
1.71593
1.31072
0.96014
0.54107
0.48135
0.32325
0.26755
0.34247
0.34539
0.31623
0.38416
0.77512
0.97966
3.52680
4.63940
3.76347
11.53791
14.17996
10.98341
9.79691
5.64667
11.07024
9.95431
6.14093
2.86053
1.43443
0.99675
0.71643
0.68092
0.39902
0.29454
0.22617
0.26872
0.33562
0.35192
0.32039
0.38591
0.54373
0.88000
1.56852
4.25868
3.02284
13.86225
6.68559
4.83731
2.67474
8.25474
7.53438
8.70597
6.97202
3.94968
3.12449
2.49004
1.14165
0.50949
0.54475
0.30209
0.27912
347.50
378.00
385.00
-371.90
329.20
349.00
360.00
360.00
340.00
370.00
350.00
213.40
225.60
225.60
225.60
225.60
243.80
262.10
292.60
298.70
298.70
335.30
365.80
359.70
359.70
341.40
378.00
384.00
378.00
365.80
341.40
339.90
340.00
360.00
340.00
330.00
320.00
213.40
225.60
225.60
225.60
225.60
237.70
256.00
280.40
298.70
292.60
353.60
323.10
341.40
317.00
359.70
359.70
378.00
383.40
359.70
371.90
380.10
360.00
340.00
380.00
350.00
350.00
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
1-HR
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL ,
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
1ST
External Review Draft
Do Not Cite or Quote
-------
* ISCST2 (94227): WTI Truck Accident Off-Site, ISCOMDEP -- OFFSITE
* MODELING OPTIONS USED:
* CONC RURAL ELEV ^GRDRIS NOSTD
* PLOT FILE OF PERIOD VALUES FOR SOURCE GROUP: ALL
* FOR A TOTAL OF 936
*
*
*
FORMAT:
X
17.36482
34.72963
52.09445
69.45927
86.82409
104.18890
121.55373
138.91852
156.28337
173.64818
217.06021
260.47229
303.88428
347.29639
390.70837
434.12042
520.94452
694.59271
868.24084
1302.36133
1736.48169
2604.72241
3472.96313
5209.44531
6945.92627
8682.40820
34.20201
68.40403
102.60603
136.80806
171.01007
205.21207
239.41408
273.61615
307.81812
342.02011
427.52518
513.03021
598.53522
684.04022
769.54523
855.05035
1026.06042
1368.08057
1710.10071
2565.15112
3420.20142
5130.30176
6840.40283
10260.60450
13680.80570
17101.00590
50.00000
100.00000
(3(1X,F13.5)
Y
98.48077
196.96155
295.44235
393.92307
492.40384
590.88470
689.36542
787.84613
886.32697
984.80774
1231.00964
1477.21167
1723.41370
1969.61548
2215.81738
2462.01929
2954.42310
3939.23096
4924.03809
7386.05762
9848.07715
14772.11520
19696.15430
29544.23050
39392.30860
49240.38670
93.96926
187.93851
281.90778
375.87701
469.84631
563.81555
657.78491
751.75409
845.72339
939.69263
1174.61572
1409.53894
1644.46204
1879.38525
2114.30835
2349.23145
2819.07788
3758.77051
4698.46289
7047.69482
9396.92578
14095.38960
18793.85350
28190.77930
37587.70310
46984.63670
86.60254
173.20508
RECEPTORS.
,1X,F8.2,2X,A6,
CONC
0.00119
0.00207
0.00195
0.00187
0.00193
0.00210
- 0.00500
0.00827
0.01379
0.01560
0.06360
0.04269
0.01242
0.02092
0.02022
0.01824
0.01368
0.01053
0.00938
0.00856
0.00615
0.00361
0.00269
0.00187
0.00134
0.00109
0.00121
0.00210
0.00198
0.00187
0.00185
0.00197
0.00359
0.00514
0.00874
0.01711
0.04696
0.05825
0,03797
0.03427
0.02760
0.02720
0.02144
0.00999
0.01111
0.00855
0.00779
0.00419
0.00318
0.00231
0.00178
0.00144
0.00123
0.00160
2X,A8,2X,I8)
ZELEV
213.40
225.60
225.60
225.60
225.60
225.60
243.80
256.00
280.40
286.50
353.60
353.60
310.90
347.50
353.60
359.70
347.50
341.40
341.40
365.80
360.00
340.00
340.00
360.00
350.00
360.00
213.40
225.60
225.60
225.60
225.60
225.60
237.70
243.80
256.00
286.50
329.20
347.50
335.30
347.50
353.60
359.70
362.40
329.20
359.70
369.70
385.90
340.00
340.00
360.00
380.00
390.00
213.40
219.50
AVE
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
GRP
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL,
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
NUN HRS
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
Volume VII
Appendix VTJ-4
External Review Draft
Do Not Cite or Quote
-------
150.00000
200.00000
250.00000
300.00000
350.00000
400.00000
450.00000
500.00000
625.00000
750.00000
875.00000
1000.00000
1125.00000
1250.00000
1500.00000
2000.00000
2500.00000
3750.00000
5000.00000
7500.00000
10000.00000
15000.00000
20000.00000
25000.00000
64.27876
128.55754
192.83627
257.11508
321.39377
385.67258
449.95132
514.23016
578.50885
642.78766
803.48456
964.18140
1124.87830
1285.57520
1446.27197
1606.96912
- 1928.36292
2571.15039
3213.93799
4820.90625
6427.87549
9641.81250
12855.75200
19283.62700
25711.50390
32139.37890
76.60445
153.20888
229.81335
306.41779
383.02225
459.62671
536.23120
612.83557
689.44000
766.04443
957.55554
1149.06665
1340.57764
Volume VII
Appendix VII-4
259.80762
346.41016
433.01273
519.61517
606.21777
692.82031
779.42291
866.02539
1082.53174
1299.03821
1515.54443
1732.05090
1948.55713
2165.06348
2598.07617
3464.10156
4330.12695
6495.19043
8660.25391
12990.38090
17320.50780
25980.76170
34641.01560
43301.26560
76.60445
153.20888
229.81335
306.41779
383.02225
459.62671
536.23120
612.83557
689.44000
766.04443
957.55554
1149.06665
1340.57764
1532.08899
1723.59998
1915.11108
2296.13330
3064.17798
3830.22192
5745.33301
7660.44434
11490.66600
15320.88870
22981.33400
30641.77730
38302.22270
64.27876
128.55754
192.83629
257.11508
321.39377
385.67261
449.95132
514.23016
578.50885
642.78766
803.48456
964.18140
1124.87830
0.00201
0.00191
0.00187
0700192
0.00214
0.00303
0.00530
0.00950
0.00374
0.06222
0.06612
0.05434
0.04729
0.03102
0.02198
0.02231
0.01692
0.01208
0.00847
0.00436
0.00361
0.00240
0.00181
0.00145
0.00125
0.00124
0.00207
0.00201
0.00198
0.00205
0.00218
0.00235
0.00257
0.00529
0.01397
0.06933
0.07158
0.05866
0.05599
0.05104
0.03614
0.03260
0.02655
0.01971
0.01550
0.00936
0.00650
0.00386
0.00278
0.00214
0.00127
0.00098
0.00127
0.00166
0.00170
0.00179
0.00190
0.00201
0.00263
0.00230
0.00271
0.03282
0.05449
225.60
225.60
225.60
- 225.60
225.60
231.60
243.80
262.10
225.60
347.50
359.70
353.60
353.60
329.20
323.10
361.20
366.70
378.00
396.20
320.00
360.00
380.00
370.00
400.00
213.40
213.40
225.60
225.60
225.60
225.60
225.60
225.60
225.60
243.80
280.40
353.60
361.50
353.60
353.60
353.60
335.30
353.90
353.00
378.00
398.40
376.00
380.00
360.00
420.00
420.00
213.40
207.30
213.40
219.50
219.50
219.50
219.50
219.50
225.60
219.50
219.50
323.10
353.60
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL ^
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
6760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
External Review Draft
Do Not Cite or Quote
-------
1532.08899
1723.59998
1915.11108
2298.13330
3064.17798
3830.22192
5745.33301
7660.44434
11490.66600
15320.88870
.22981.33400
30641.77730
38302.22270
86.60254
173.20508
259.80762
346.41016
433.01273
519.61517
606.21777
692.82031
779.42291
866.02539
1082.53174
1299.03821
1515.54443
1732.05090
1948.55725
2165.06348
2598.07617
3464.10156
4330.12695
6495.19043
8660.25391
12990.38090
17320.50780
25980.76170
34641.01560
43301.26560
93.96926
187.93851
281 .90778
375.87701
469.84631
563.81555
657.78491
751.75409
845.72333
939.69263
1174.61572
1409.53894
1644.46204
1879.38525
2114.30835
2349.23145
2819.07788
3758.77051
4698.46289
7047.69482
9396.92578
14095.38960
18793.85350
28190.77930
Volume VII
Appendix VII-4
1285.57520
1446.27197
1606.96912
1928.36292
2571.15039
3213.93799
4820.90674
6427.87549
9641.81348
12855.75200
19283.62700
25711.50390
32139.38090
50.00000
99.99999
150.00000
199.99997
249.99997
300.00000
349.99994
TOO OOOQ£
JYT • 9 9 W JH
449.99994
499.99994
625.00000
750.00000
875.00000
1000.00000
1125.00000
1250.00000
1500.00000
2000.00000
2499.99976
3749.99976
4999.99902
7499.99902
9999.99902
14999.99900
19999.99800
24999.99800
34.20201
68.40403
102.60603
136.80806
171.01007
205.21207
239.41411
273.61615
307.81815
342.02011
427.52518
513.03021
598.53528
684.04022
769.54535
855.05035
1026.06042
1368.08057
1710.10071
2565.15112
3420.20142
5130.30176
6840.40283
10260.60450
0.05026
0.03801
0.04494
0^»1"83-
0.03345
0.02669
0.02484
0.01910
0.01182
0.00949
0.00593
0.00405
0.00297
0.00129
0.00102
0.00104
0.00087
0.00118
0.00156
0.00169
0.00181
0.00193
0.00249
0.00336
0.00315
0.00632
0.01629
0.02254
0.02680
0.02348
0.02227
0.02923
0.02324
0.01981
0.01295
0.00905
0.00619
0.00438
0.00329
0.00100
0.00082
0.00092
0.00100
0.00129
0.00140
0.00152
0.00200
0.00212
0.00225
0.00256
0.00285
0.00313
0.00338
0.00360
0.00557
0.00576
0.01818
0.03402
0.02356
0.01780
0.01099
0.00904
0.00575
353.60
335.30
347.50
347.50
341.40
335.30
373.10
396.20
360.00
380.00
380.00
420.00
420.00
213.40
207.30
207.30
201.20
207.30
213.40
213.40
213.40
213.40
219.50
225.60
219.50
243.80
292.60
310.90
323.10
317.00
323.10
359.70
378.90
408.70
380.00
360.00
380.00
380.00
420.00
207.30
201.20
202.70
202.70
207.30
207.30
207.30
213.40
213.40
213.40
213.40
213.40
213.40
213.40
213.40
231.60
231.60
310.90
384.00
384.00
370.30
360.00
380.00
400.00
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL,
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
External Review Draft
Do Not Cite or Quote
-------
37587.70310
46984.63670
98.48077
196.96155
295.44235
393.92307
492.40384
590.88470
689.36542
787.84613
886.32697
984.80774
1231.00964
1477.21167
1723.41370
1969.61548
2215.81738
2462.01929
2954.42310
3939.23096
4924.03809
7386.05762
9848.07715
14772.11520
19696.15430
29544.23050
39392.30860
49240.38670
100.00000
200.00000
300.00000
400.00000
500.00000
600.00000
700.00000
800.00000
900.00000
1000.00000
1250.00000
1500.00000
1750.00000
2000.00000
2250.00000
2500.00000
3000.00000
4000.00000
5000.00000
7500.00000
10000.00000
15000.00000
20000.00000
30000.00000
40000.00000
50000.00000
98.48077
196.96155
295.44235
393.92307
492.40384
590.88470
689.36542
787.84613
886.32697
Volume VH
Appendix VII-4
13680.80570
17101.00780
17.36482
34.72964
52.09447
69.45930
86.82410
104.18893
121.55376
138.91856
156.28340
173.64821
.217.06027
260.47235
303.88434
347.29648
390.70850
434.12051
520.94470
694.59296
868.24103
1302.36169
1736.48218
2604.72290
3472.96411
5209.44580
6945.92822
8682.41113
0.00001
0.00002
0.00002
0.00003
0.00004
0.00005
0.00005
0.00006
0.00007
0.00008
0.00009
0.00011
0.00013
0.00015
0.00017
0.00019
0.00023
0.00030
0.00038
0.00057
0.00075
0.00113
0.00151
0.00226
0.00302
0.00377
-17.36482
-34.72964
-52.09446
-69.45927
-86.82410
-104.18891
-121.55373
-138.91853
-156.28339
0.00394
0.00324
0.00102
0780090-
0.00097
0.00106
0.00117
0.00129
0.00142
0.00155
0.00167
0.00180
0.00211
0.00239
0.00345
0.00320
0.00340
0.00609
0.02047
0.03276
0.03220
0.02586
0.01941
0.01019
0.00895
0.00615
0.00448
0.00350
0.00103
0.00092
0.00101
0.00111
0.00124
0.00137
0.00151
0.00165
0.00179
0.00194
0.00774
0.05510
0.03593
0.04748
0.02438
0.01977
0.02616
0.04243
0.04706
0.02397
0.02280
0.01462
0.01137
0.00788
0.00584
0.00437
0.00104
0.00094
0.00103
0.00115
0.00128
0.00142
0.00156
0.00292
0.00380
360.00
400.00
207.30
202.70
202.70
202.70
202.70
202.70
202.70
202.70
202.70
202.70
202.70
202.70
213.40
207.30
207.30
231.60
304.80
346.60
365.80
384.00
371.90
320.00
360.00
380.00
380.00
400.00
207.30
202.70
202.70
202.70
202.70
202.70
202.70
202.70
202.70
202.70
243.80
341.40
323.10
341.40
304.80
292.60
310.90
359.70
402.30
347.50
380.10
360.00
360.00
380.00
400.00
360.00
207.30
202.70
202.70
202.70
202.70
202.70
202.70
219.50
225.60
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD.
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL,
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
.8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
External Review Draft
Do Not Cite or Quote
-------
984.80774
1231.00964
1477.21167
1723.41370
1969.61548
2215.81738
2462.01929
2954.42310
3939.23096
4924.03809
7386.05762
9848.07715
14772.11520
19696.15430
29544.23050
39392.30860
49240.38670
93.96926
187.93851
281.90778
375.87701
469.84631
563.81555
657.78491
751.75409
845.72339
939.69263
1174.61584
1409.53894
1644.46216
1879.38525
2114.30835
2349.23145
2819.07788
3758.77051
4698.46338
7047.69482
9396.92676
14095.38960
18793.85550
28190.77930
37587.70700
46984.63670
86.60254
173.20508
259.80762
346.41016
433.01273
519.61517
606.21777
692.82031
779.42291
866.02539
1082.53174
1299.03821
1515.54443
1732.05090
1948.55713
2165.06348
2598.07617
3464.10156
4330.12695
6495.19043
Volume VII
Appendix VH-4
-173.64819
-217.06023
-260.47232
-303.88431
-347.29642
-390.70840
-434.12045
-520.94458
-694.59277
-868.24091
-1302.36145 .
-1736.48181
-2604.72290
-3472.96338
-5209.44580
-6945.92676
-8682.40918
-34.20201
-68.40402
-102.60603
-136.80804
-171.01006
-205.21207
-239.41406
-273.61612
-307.81812
-342.02008
-427.52515
-513.03021
-598.53522
-684.04016
-769.54523
-855.05023
-1026.06030
-1368.08032
-1710.10059
-2565.15088
-3420.20093
-5130.30127
-6840.40234
-10260.60350
-13680.80470
-17101.00590
-50.00000
-100.00001
-150.00002
-200.00002
-250.00003
-300.00003
-350.00003
-400.00003
-450.00003
-500.00006
-625.00006
-750.00006
-875.00006
-1000.00012
-1125.00012
-1250.00012
-1500.00012
-2000.00024
-2500.00024
-3750.00049
0.04641
0.06475
0.06638
0.03500
0.04653
0.04435
0.03190
0.04333
0.03981
0.04436
0.02554
0.02136
0.01372
0.01286
0.00842
0.00618
0.00492
0.00104
0.00095
0.00105
0.00115
0.00128
0.00200
0.00905
0.02126
0.01533
0.03866
0.05768
0.05280
0.02572
0.05061
0.04555
0.04289
0.03547
0.03100
0.03265
0.02283
0.02178
0.01389
0.00965
0.00653
0.00488
0.00387
0.00104
0.00095
0.00104
0.00113
0.00176
0.00964
0.03294
0.06026
0.06335
0.05492
0.02247
0.05446
0.03277
0.04736
0.04368
0.03224
0.03797
0.02757
0.02329
0.02125
329.20
347.50
353.60
"323.10
341.40
341.40
323.10
347.50
353.60
386.50
353.60
360.00
340.00
380.00
380.00
380.00
400.00
207.30
202.70
202.70
202.70
202.70
213.40
256.00
298.70
286.50
323.10
347.50
347.50
310.90
353.60
350.20
347.50
347.50
345.90
371.90
365.80
408.40
380.00
360.00
360.00
360.00
360.00
207.30
202.70
202.70
202.70
213.40
268.20
317.00
347.50
353.60
347.50
310.90
359.70
335.30
359.70
359.70
347.50
365.80
359.70
353.60
402.30
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL ,
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
External Review Draft
Do Not Cite or Quote
-------
/ 8660.25391
( 12990.38090
V ^ 17320.50780
25980.76170
34641.01560
43301.26560
76.60445
153.20888
229.81332
306.41779
383.02225
459.62668
536.23108
612.83557
689.44000
766.04443
957.55554
1149.06665
1340.57764
1532.08899
1723.59998
1915.11108
2298.13330
3064.17798
3830.22192
5745.33252
7660.44434
11490.66500
15320.88870
•"" 22981.33200
30641 .77730
% ,. 38302.22270
64.27876
128.55754
192.83629
257.11508
321.39377
385.67261
449.95132
514.23016
578.50885
642.78766
803.48456
964.18146
1124.87830
1285.57520
1446.27197
1606.96912
1928.36292
2571.15039
3213.93799
4820.90674
6427.87549
9641.81348
12855.75200
19283.62700
25711.50390
32139.38090
50.00000
100.00001
150.00002
200.00002
250.00002
Volume VD.
Appendix VU-4
-5000.00049
-7500.00098
-10000.00100
-15000.00200
-20000.00200
-25000.00200
-64.27876
-128.55754
-192.83629
-257.11508
-321.39377
-385.67261
-449.95132
-514.23016
-578.50885
-642.78766
-803.48462
-964.18146
-1124.87830
-1285.57520
-1446.27209
-1606.96924
-1928.36292
-2571.15039
-3213.93823
-4820.90674
-6427.87598
-9641.81348
-12855.75290
-19283.62700
-25711.50590
-32139.38090
-76.60445
-153.20888
-229.81332
-306.41779
-383.02225
-459.62668
-536.23108
-612.83557
-689.44000
-766.04443
-957.55554
-1149.06665
-1340.57764
-1532.08899
-1723.59998
-1915.11108
-2298.13330
-3064.17798
-3830.22192
-5745.33301
-7660.44434
-11490.66600
-15320.88870
-22981.33400
-30641.77730
-38302.22270
-86.60254
-173.20508
-259.80762
-346.41016
-433.01273
0.01653
0.01040
0.00813
0.00492
0.00368
0.00292
0.00104
0.00095
0.00102
0.00110
0.00496
0.01780
0.03371
0.06255
0.05933
0.05308
0.04604
0.04724
0.03173
0.03579
0.03246
0.02528
0.02883
0.02149
0.01828
0.01620
0.01258
0.00768
0.00517
0.00367
0.00262
0.00209
0.00103
0.00093
0.00099
0.00106
0.00792
0.01921
0.02076
0.02798
0.03000
0.02427
0.03828
0.03784
0.01963
0.03018
0.02462
0.02448
0.03379
0.02699
0.01680
0.01339
0.01004
0.00526
0.00505
0.00343
0.00254
0.00187
0.00102
0.00091
0.00097
0.00145
0.00742
396.20
380.00
380.00
""340.00
360.00
360.00
207.30
202.70
202.70
202.70
243.80
298.70
323.10
353.60
353.60
353.60
353.60
359.70
341.40
353.60
353.60
341.40
359.70
359.70
359.70
408.40
408.40
380.00
360.00
360.00
360.00
360.00
207.30
202.70
202.70
202.70
268.20
304.80
310.90
323.10
329.20
323.10
347.50
359.70
329.20
359.70
353.60
359.70
408.40
420.60
371.90
392.00
390.10
340.00
380.00
400.00
400.00
380.00
207.30
202.70
202.70
213.40
268.20
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL ,
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
External Review Draft
Do Not Cite or Quote
-------
300.
350.
400.
450.
500.
625.
750.
875.
1000.
1125.
1250.
1500.
2000.
2500.
3750.
5000.
7500.
10000.
15000.
20000.
25000.
34.
68.
102.
136.
171.
205.
239.
273.
307.
342.
427.
513.
598.
684.
769.
855.
1026.
1368.
1710.
2565.
00003
00003
00003
00003
00003
00006
00006
00006
00006
00012
00012
00012
00012
00024
00024
00049
00049
00100
00100
00200
00200
20202
40405
60606
80809
01012
21213
41414
61621
81821
02023
52527
03033
53546
04047
54547
05054
06079
08081
10107
15161
3420.20190
5130.
6840.
10260.
13680.
17101.
17.
34.
52.
69.
86.
104.
121.
138.
156.
173.
217.
260.
303.
347.
390.
434.
Volume
Appendix
30273
40430
60550
80860
01170
36483
72966
09449
45933
82413
18897
55380
91862
28346
64827
06036
47244
88449
29657
70868
12073
vn
VIM
-519
•606
•692
-779
-866
-1082
-1299
-1515
-1732
-1948
.61517
.21777
.82031
.42291
.02539
.53174
.03821
.54443
.05090
.55713
-2165.06348
-2598
-3464
-4330
-6495
-8660
-12990
-17320
-25980
-34641
-43301
-93
-187
-281
-375
-469
-563
-657
-751
-845
-939
-1174
-1409
-1644
-1879
-2114
-2349
-2819
-3758
-4698
-7047
•9396
-14095
-18793
-28190
-37587
-46984
-98
-196
-295
-393
-492
-590
•689
-787
-886
-984
-1231
•1477
-1723
-1969
-2215
-2462
.07617
.10156
.12695
.19043
.25391
.38090
.50780
.76170
.01560
.26560
.96926
.93851
.90778
.87701
.84631
.81555
.78479
.75409
.72333
.69257
.61572
.53894
.46204
.38513
.30835
.23145
.07788
.77026
.46289
.69434
.92578
.38870
.85350
.77730
.70310
.62890
.48077
.96155
.44235
.92307
.40384
.88470
.36542
.84613
.32697
.80774
.00964
.21143
.41370
.61548
.81738
.01929
0
0
0
.01396
.01881
.02424
07tt2099~
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
.02441
.00981
.02313
.02187
.02752
.02884
.02916
.03120
.02296
.01869
.01278
.00902
.00491
.00417
.00305
.00236
0.00187
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
.00100
.00089
.00094
.00112
.00671
.01102
.01327
.01272
.00679
.00673
.01057
.01107
.00889
.01666
.02358
.02780
.02527
.02143
.01714
.01214
.00829
.00498
.00365
.00279
.00218
.00170
0.00099
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
.00086
.00090
.00090
.00413
.00789
.00586
.00460
.00628
.00603
.00742
.00919
.00808
.00651
.00654
.02242
298.70
310.90
323.10
323.10
329.20
298.70
341.40
341.40
359.70
365.80
371.90
408.40
420.60
408.40
408.40
396.20
340.00
360.00
420.00
400.00
400.00
207.30
202.70
202.70
207.30
268.20
292.60
304.80
304.80
286.50
286.50
304.80
310.90
304.80
335.30
359.70
378.00
396.20
402.30
411.50
402.30
408.10
360.00
360.00
420.00
400.00
420.00
207.30
202.70
202.70
202.70
249.90
286.50
280.40
274.30
286.50
286.50
298.70
304.80
304.80
298.70
298.70
365.80
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL ,
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL,
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
6760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
External Review Draft
Do Not Cite or Quote
-------
520.94489
694.59320
868.24146
1302.36230
1736.48279
2604.72412
3472.96558
5209.44824
6945.93115
8682.41504
0.00002
0.00003
0.00005
0.00006
0.00008
0.00009
0.00011
0.00012
0.00014
0.00015
0.00019
0.00023
0.00026
0.00030
0.00034
0.00038
0.00045
0.00060
0.00075
0.00113
0.00151
0.00226
0.00302
0.00453
0.00604
0.00755
-17.36482
-34.72964
-52.09447
-69.45930
-86.82410
-104.18893
-121.55376
-138.91856
-156.28340
-173.64821
-217.06029
-260.47238
-303.88437
-347.29648
-390.70853
-434.12054
-520.94470
-694.59296
-868.24115
-1302.36182
-1736.48218
-2604.72314
-3472.96436
-5209.44629
-6945.92871
-8682.41113
-34.20201
Volume VII
Appendix VII-4
-2954.42285
-3939.23096
-4924.03809
-7386.05762
-9848.07715
-14772.11520
-19696.15430
-29544.23050
-39392.30860
-49240.38670
-100.00000
-200.00000
-300.00000
-400.00000
-500.00000
-600.00000
-700.00000
-800.00000
-900.00000
-1000.00000
-1250.00000
-1500.00000
-1750.00000
-2000.00000
-2250.00000
-2500.00000
-3000.00000
-4000.00000
-5000.00000
-7500.00000
-10000.00000
-15000.00000
-20000.00000
-30000.00000
-40000.00000
-50000.00000
-98.48077
-196.96155
-295.44235
-393.92307
-492.40384
-590.88470
-689.36542
-787.84613
-886.32697
-984.80774
-1231.00964
-1477.21167
-1723.41370
-1969.61548
-2215.81738
-2462.01929
-2954.42310
-3939.23096
-4924.03809
-7386.05762
-9848.07715
-14772.11520
-19696.15430
-29544.23050
-39392.30860
-49240.38670
-93.96926
0.02731
0.01930
0.01846
07fl294-
0.00970
0.00592
0.00431
0.00331
0.00248
0.00209
0.00097
0.00083
0.00085
0.00082
0.00123
0.00511
0.00528
0.00444
0.00201
0.00789
0.00820
0.00809
0.00760
0.00543
0.00623
0.02398
0.03236
0.02645
0.02152
0.01482
0.01208
0.00701
0.00480
0.00347
0.00259
0.00217
0.00095
0.00080
0.00080
0.00074
0.00063
0.00113
0.00425
0.00389
0.00145
0.00586
0.00807
0.00453
0.00599
0.00449
0.00851
0.02468
0.03526
0.03135
0.02653
0.01653
0.01200
0.00632
0.00407
0.00282
0.00230
0.00199
0.00122
402.30
390.10
414.50
S08.40
398.10
380.00
360.00
400.00
400.00
400.00
207.30
202.70
202.70
202.70
219.50
274.30
280.40
274.30
243.80
298.70
304.80
304.80
304.80
292.60
298.70
365.80
406.30
402.30
396.20
390.10
396.20
380.00
360.00
380.00
380.00
400.00
207.30
202.70
202.70
202.70
202.70
225.60
274.30
274.30
237.70
292.60
304.80
286.50
292.60
280.40
304.80
353.60
384.00
396.20
415.40
390.10
392.00
360.00
340.00
340.00
360.00
380.00
213.40
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL,
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
External Review Draft
Do Not Cite or Quote
-------
-68.40403
-102.60605
-136.80806
-171.01009
-205.21210
-239.41411
-273.61615
-307.81815
-342.02014
-427.52521
-513.03021
-598.53528
-684.04034
-769.54535
-855.05042
-1026.06042
-1368.08069
-1710.10083
-2565.15112
-3420.20142
-5130.30176
-6840.40332
-10260.60450
-13680.80660
-17101.00780
-50.00000
-100.00000
-150.00000
-200.00000
-250.00000
-300.00000
-350.00000
-400.00000
-450.00000
-500.00000
-625.00000
-750.00000
-875.00000
-1000.00000
-1125.00000
-1250.00000
-1500.00000
-2000.00000
-2500.00000
-3750.00000
-5000.00000
-7500.00000
-10000.00000
-15000.00000
-20000.00000
-25000.00000
-64.27876
-128.55753
-192.83627
-257.11505
-321.39377
-385.67258
-449.95129
-514.23010
-578.50873
-642.78766
-803.48456
-964.18134
Volume VII
Appendix VII-4
-187.93851
-281.90778
-375.87701
-469.84631
-563.81555
-657.78491
-751.75409
-845.72333
-939.69263
-1174.61572
-1409.53894
-1644.46204
-1879.38525
-2114.30835
-2349.23145
-2819.07788
-3758.77051
-4698.46289
-7047.69482
-9396.92578
-14095.38960
-18793.85350
-28190.77930
•37587.70310
-46984.62890
•86.60254
-173.20508
-259.80762
-346.41016
-433.01273
-519.61517
-606.21777
-692.82031
-779.42291
-866.02539
-1082.53174
-1299.03821
-1515.54443
-1732.05090
-1948.55713
-2165.06348
-2598.07617
-3464.10156
-4330.12695
-6495.19043
-8660.25391
-12990.38090
-17320.50780
-25980.76170
-34641.01560
-43301.26560
-76.60445
•153.20888
-229.81335
-306.41779
-383.02228
-459.62671
-536.23120
-612.83557
-689.44000
-766.04449
-957.55560
-1149.06689
0.00077
0.00075
0.00067
0.00055 ~
0.00048
0.00076
0.00216
0.00069
0.00404
0.00400
0.00441
0.00486
0.00377
0.00901
0.03169
0.03623
0.03386
0.02467
0.01501
0.01020
0.00451
0.00327
0.00250
0.00200
0.00165
0.00120
0.00074
0.00071
0.00061
0.00049
0.00043
0.00039
0.00036
0.00036
0.00062
0.00074
0.00082
0.00106
0.00186
0.00196
0.00749
0.02988
0.03053
0.02433
0.01181
0.00864
0.00425
0.00350
0.00197
0.00153
0.00131
0.00119
0.00072
0.00068
0.00058
0.00046
0.00039
0.00035
0.00033
0.00033
0.00037
0.00048
0.00075
202.70
202.70
202.70
202.70
202.70
219.50
249.90
219.50
280.40
280.40
280.40
280.40
262.10
298.70
353.60
371.90
402.30
397.20
384.00
384.00
340.00
340.00
360.00
380.00
380.00
213.40
202.70
202.70
202.70
202.70
202.70
202.70
202.70
202.70
219.50
219.50
213.40
213.40
231.60
231.60
292.60
359.70
396.20
414.50
396.20
392.60
360.00
380.00
360.00
360.00
380.00
213.40
202.70
202.70
202.70
202.70
202.70
202.70
202.70
202.70
202.70
202.70
213.40
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL *
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
. 8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
External Review Draft
Do Not Cite or Quote
-------
-1124.87830
-1285.57520
-1446.27185
-1606.96912
-1928.36279
-2571.15039
-3213.93774
-4820.90625
-6427.87500
-9641.81250
-12855.75100
-19283.62700
-25711.50200
-32139.37890
-76.60445
-153.20891
-229.81339
-306.41782
-383.02231
-459.62674
-536.23120
-612.83563
-689.44006
-766.04456
-957.55566
-1149.06689
-1340.57800
-1532.08911
-1723.60022
-1915.11121
-2298.13354
-3064.17847
-3830.22241
-5745.33350
-7660.44531
-11490.66700
-15320.89060
-22981.33590
-30641.78130
-38302.22660
-86.60255
-173.20509
-259.80765
-346.41019
-433.01276
-519.61530
-606.21783
-692.82037
-779.42297
-866.02551
-1082.53186
-1299.03833
-1515.54456
-1732.05090
-1948.55725
-2165.06372
-2598.07666
-3464.10181
-4330.12744
-6495.19092
-8660.25488
-12990.38180
-17320.50980
Volume VII
Appendix VII-4
-1340.57788
-1532.08899
-1723.60010
-1915.11121
•2298.13354
-3064.17822
-3830.22241
-5745.33301
-7660.44482
-11490.66600
-15320.88960
-22981 .33400
-30641.77930
-38302.22270
-64.27876
-128.55751
-192.83624
-257.11499
-321.39371
-385.67252
-449.95123
-514.22998
-578.50867
-642.78754
-803.48444
-964.18115
-1124.87830
-1285.57483
-1446.27173
-1606.96887
-1928.36243
-2571.15015
-3213.93750
-4820.90576
-6427.87451
-9641.81250
-12855.75000
-19283.62500
-25711.50000
-32139.37700
-49.99999
"99.99998
-149.99997
-199.99994
•249.99994
-299.99991
-349.99991
•399.99988
-449.99988
•499.99988
•624.99988
-749.99988
•874.99982
•999.99982
-1124.99976
-1249.99976
-1499.99976
-1999.99963
-2499.99951
-3749.99927
-4999.99854
-7499.99805
-9999.99805
0.00081
0.00076
0.00068
0.00064'
0.03071
0.02086
0.01728
0.01068
0.00654
0.00353
0.00305
0.00193
0.00165
0.00118
0.00118
0.00065
0.00078
0.00068
0.00044
0.00037
0.00032
0.00030
0.00039
0.00045
0.00051
0.00039
0.00028
0.00033
0.00037
0.00156
0.00789
0.01669
0.01971
0.01305
0.01018
0.00561
0.00490
0.00320
0.00244
0.00186
0.00117
0.00108
0.00101
0.00068
0.00073
0.00059
0.00051
0.00047
0.00053
0.00059
0.00068
0.00280
0.01623
0.00812
0.00400
0.00178
0.00155
0.03177
0.02768
0.02001
0.01754
0.00870
0.00688
213.40
213.40
213.40
213.40
371.90
378.00
396.20
396.20
378.00
349.00
360.00
360.00
380.00
360.00
213.40
201.20
207.30
207.30
202.70
202.70
202.70
202.70
207.30
207.30
207.30
207.30
207.30
213.40
213.40
256.00
323.10
359.70
384.00
378.00
378.00
360.00
380.00
400.00
400.00
380.00
213.40
213.40
213.40
207.30
213.40
213.40
213.40
213.40
213.40
213.40
225.60
274.30
329.20
310.90
286.50
256.00
243.80
365.80
372.50
378.00
402.30
360.00
380.00
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD.
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL,
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
External Review Draft
Do Not Cite or Quote
-------
-25980
-34641
-43301
-93
-187
-281
' -375
-469
-563
-657
. -751
-845
-939
-1174
-1409
-1644
-1879
-2114
-2349
-2819
-3758
-4698
-7047
-9396
-14095
-18793
-28190
-37587
-46984
-98
-196
-295
-393
-492
-590
-689
-787
-886
-984
-1231
-1477
-1723
-1969
-2215
-2462
-2954
-3939
-4924
-7386
-9848
-14772
-19696
-29544
-39392
-49240
-100
-200
-300
-400
-500
-600
-700
-800
.76370
.01950
.27340
.96926
.93851
.90778
.87701
.84631
.81561
.78491
.75409
.72339
.69263
.61584
.53894
.46216
.38525
.30835
.23145
.07788
.77051
.46338
.69482
.92676
.38960
.85550
.77930
.70700
.63670
.48077
.96155
.44235
.92307
.40384
.88470
.36542
.84613
.32697
.80774
.00964
.21167
.41370
.61548
.81738
.01929
.42310
.23096
.03809
.05762
.07715
.11520
.15430
.23050
.30860
.38670
.00000
.00000
.00000
.00000
.00000
.00000
.00000
.00000
-14999
-19999
-24999
-34
-68
-102
-136
-171
-205
-239
-273
-307
-342
-427
-513
-598
-684
-769
-855
-1026
-1368
-1710
-2565
-3420
-5130
-6840
-10260
-13680
-17101
-17
-34
-52
-69
-86
-104
-121
-138
-156
-173
-217
-260
-303
-347
-390
-434
-520
-694
-868
-1302
-1736
-2604
-3472
-5209
-6945
-8682
0
0
0
0
0
0
0
0
.99710
.99610
.99410
.20201
.40401
.60602
.80803
.01004
.21204
.41403
.61609
.81805
.02008
.52509
.03009
.53516
.04016
.54517
.05017
.06030
.08020
.10022
.15039
.20044
.30029
.40137
.60160
.80270
.00390
.36481
.72963
.09444
.45926
.82407
.18888
.55370
.91849
.28334
.64813
.06018
.47223
.88422
.29630
.70831
.12033
.94446
.59253
.24066
.36096
.48120
.72192
.96240
.44385
.92480
.40625
.00000
.00000
.00000
.00000
.00001
.00001
.00001
.00001
0.00450
0.00340
0.00240
o~6oii6-
0.00108
0.00100
0.00093
0.00081
0.00063
0.00053
0.00068
0.00077
0.00053
0.07633
0.05945
0.04463
0.03991
0.06316
0.01553
0.00269
0.01064
0.02829
0.01835
0.01661
0.00960
0.00748
0.00456
0.00326
0.00240
0.00116
0.00108
0.00100
0.00095
0.00089
0.00075
0.00058
0.00072
0.00124
0.06814
0.16513
0.17465
0.14016
0.12010
0.10686
0.12781
0.07013
0.06004
0.04532
0.03536
0.01428
0.01262
0.01046
0.00747
0.00533
0.00420
0.00115
0.00107
0.00101
0.00095
0.00090
0.00082
0.00068
0.00044
380.00
400.00
360.00
213.40
213.40
213.40
213.40
213.40
213.40
213.40
219.50
219.50
213.40
353.60
353.60
341.40
335.30
353.60
304.80
243.80
298.70
359.70
365.80
402.30
380.00
400.00
380.00
400.00
360.00
213.40
213.40
213.40
213.40
213.40
213.40
213.40
219.50
225.60
310.90
359.70
359.70
365.80
371.90
353.60
371.90
353.60
365.80
365.80
390.10
339.90
360.00
380.00
420.00
400.00
400.00
213.40
213.40
213.40
213.40
213.40
213.40
213.40
213.40
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD'
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL ,
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
Volume VH
Appendix VII-4
External Review Draft
Do Not Cite or Quote
-------
•900.00000
-1000.00000
-1250.00000
-1500.00000
-1750.00000
-2000.00000
-2250.00000
-2500.00000
-3000.00000
-4000.00000
-5000.00000
-7500.00000
-10000.00000
-15000.00000
-20000.00000
-30000.00000
-40000.00000
-50000.00000
-98.48077
-196.96155
-295.44235
-393.92307
-492.40384
-590.88470
-689.36542
-787.84613
-886.32697
-984.80774
-1231.00964
-1477.21167
-1723.41370
-1969.61548
-2215.81738
-2462.01929
-2954.42310
-3939.23096
-4924.03809
-7386.05762
-9848.07715
-14772.11520
-19696.15430
-29544.23050
-39392.30860
-49240.38670
-93.96926
-187.93851
-281.90778
-375.87701
-469.84631
-563.81561
-657.78491
-751.75409
-645.72339
•939.69263
-1174.61584
-1409.53894
-1644.46216
-1679.36525
-2114.30835
-2349.23145
-2819.07788
-3758.77051
-4698.46338
Volume VII
Appendix VII-4
0.00001
0.00001
0.00001
0.00002
0.00002
0.00002
0.00003
0.00003
0.00004
0.00005
0.00006
0.00009
0.00012
0.00018
0.00024
0.00036
0.00048
0.00060
17.36481
34.72963
52.09445
69.45927
86.82407
104.18890
121.55371
138.91850
156.28336
173.64815
217.06020
260.47226
303.88428
347.29633
390.70834
434.12039
520.94452
694.59259
868.24072
1302.36133
1736.48157
2604.72241
3472.96289
5209.44482
6945.92578
8682.40820
34.20201
68.40401
102.60603
136.80803
171.01004
205.21204
239.41405
273.61609
307.81808
342.02008
427.52512
513.03021
598.53522
664.04016
769.54517
855.05017
1026.06030
1368.08020
1710.10034
0.01595
0.24859
0.07379
0.04421
0.09983
0.09515
0.14702
0.12716
0.09674
0.06938
0.04935
0.02917
0.01887
0.01025
0.00941
0.00685
0.00502
0.00409
0.00115
0.00107
0.00100
0.00093
0.00084
0.00204
0.00170
0.00729
0.01254
0.04935
0.05729
0.01524
0.00860
0.03665
0.05462
0.03651
0.04048
0.02321
0.02681
0.01621
0.01202
0.00787
0.00589
0.00363
0.00267
0.00215
0.00115
0.00106
0.00098
0.00134
0.00195
0.00184
0.01372
0.02947
0.02077
0.03183
0.04720
0.01909
0.01417
0.07458
0.08170
0.06108
0.04173
0.02828
0.02233
243.80
298.70
304.80
~ 304.80
335.30
341.40
371.90
371.90
371.90
378.00
371.90
371.90
360.00
340.00
360.00
380.00
380.00
400.00
213.40
213.40
213.40
213.40
213.40
225.60
225.60
237.70
243.80
280.40
317.00
304.60
298.70
341.40
371.90
353.60
365.80
353.60
378.00
384.00
389.20
400.00
420.00
380.00
380.00
400.00
213.40
213.40
213.40
219.50
225.60
225.60
243.80
274.30
286.50
298.70
317.00
298.70
298.70
359.70
384.00
378.00
378.00
378.00
378.00
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
.ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL ,
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
6760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760.
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
External Review Draft
Do Not Cite or Quote
-------
-7047.69482
-9396.92676
-14095.38960
-18793.85550
-28190.77930
-37587.70700
-46984.63670
-86.60255
-173.20509
-259.80765
-346.41019
-433.01276
-519.61530
-606.21783
-692.82037
-779.42297
-866.02551
-1082.53186
-1299.03833
-1515.54456
-1732.05090
-1948.55725
-2165.06372
-2598.07666
-3464.10181
-4330.12744
-6495.19092
-8660.25488
-12990.38180
-17320.50980
-25980.76370
-34641.01950
-43301 .27340
-76.60445
-153.20891
-229.81335
-306.41782
-383.02228
-459.62671
-536.23120
-612.83563
-689.44006
-766.04449
-957.55566
-1149.06689
-1340.57788
-1532.08899
-1723.60022
-1915.11121
-2298.13354
-3064.17822
-3830.22241
-5745.33350
-7660.44531
-11490.66700
-15320.89060
-22981.33590
-30641.78130
-38302.22660
-64.27877
-128.55756
-192.83632
-257.11511
Volume VH
Appendix VII-4
2565.15063
3420.20093
5130.30078
6840.40186
10260.60250
13680.80370
17101.00390
49.99999
99.99998
149.99997
199.99997
249.99994
299.99991
349.99991
399.99991
449.99991
499.99988
624.99988
749.99988
874.99988
999.99982
1125.00000
1249.99976
1499.99976
1999.99963
2499.99951
3749.99951
4999.99854
7499.99854
9999.99805
14999.99800
19999.99610
24999.99610
64.27876
128.55751
192.83626
257.11499
321.39374
385.67255
449.95126
514.22998
578.50873
642.78760
803.48444
964.18121
1124.87830
1285.57507
1446.27173
1606.96887
1928.36255
2571.15015
3213.93750
4820.90576
6427.87451
9641.81250
12855.75000
19283.62500
25711.50000
32139.37700
76.60442
153.20885
229.81332
306.41772
0.01337
0.01180
0.00769
0760461-
0.00345
0.00247
0.00201
0.00115
0.00106
0.00140
0.00301
0.00194
0.00360
0.01984
0.04027
0.03107
0.01833
0.00996
0.02939
0.07222
0.08052
0.06944
0.06679
0.05579
0.03589
0.02691
0.01673
0.01391
0.00802
0.00599
0.00383
0.00275
0.00201
0.00115
0.00106
0.00201
0.00290
0.00212
0.00354
0.01355
0.02567
0.02815
0.02289
0.01224
0.03837
0.04391
0.04394
0.04976
0.04571
0.04507
0.02772
0.02629
0.01584
0.01195
0.00697
0.00556
0.00377
0.00271
0.00202
0.00115
0.00207
0.00282
0.00284
371.90
424.90
420.00
360.00
400.00
380.00
400.00
213.40
213.40
219.50
231.60
225.60
231.60
268.20
304.80
310.90
304.80
292.60
323.10
359.70
371.90
371.90
378.00
378.00
378.00
384.00
384.00
426.70
400.00
400.00
420.00
400.00
350.00
213.40
213.40
225.60
231.60
225.60
231.60
268.20
304.80
316.40
317.00
304.80
341.40
353.60
365.80
371.90
378.00
384.00
359.70
384.00
378.00
379.20
360.00
400.00
400.00
400.00
370.00
213.40
225.60
231.60
231.60
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL,
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
External Review Draft
Do Not Cite or Quote
-------
-321.39383
-385.67267
-449.95142
-514.23022
-578.50897
-642.78772
-803.48474
-964.18152
-1124.87854
-1285.57532
-1446.27222
-1606.96936
-1928.36328
-2571.15088
-3213.93872
-4820.90771
-6427.87695
-9641.81543
-12855.75490
-19283.63090
-25711.50980
-32139.38670
-50.00002
-100.00003
-150.00005
-200.00006
-250.00009
-300.00009
-350.00012
-400.00012
-450.00015
-500.00018
-625.00024
-750.00024
-875.00031
-1000.00037
-1125.00037
-1250.00049
-1500.00049
-2000.00073
- -2500.00098
-3750.00122
-5000.00195
-7500.00244
-10000.00390
-15000.00490
-20000.00780
-25000.00780
-34.20204
-68.40408
-102.60610
-136.80815
-171.01018
-205.21220
-239.41423
-273.61633
-307.81833
-342.02036
-427.52545
-513.03052
-598.53571
-684.04065
-769.54584
Volume VII
Appendix VH-4
383.02216
459.62665
536.23102
612.83551
689.43988
766.04431
957.55542
1149.06653
1340.57751
1532.08862
1723.59973
1915.11084
2298.13306
3064.17749
3830.22144
5745.33203
7660.44336
11490.66410
15320.88670
22981.33010
30641.77340
38302.21880
86.60253
173.20506
259.80756
346.41013
433.01270
519.61517
606.21771
692.82025
779.42279
866.02533
1082.53162
1299.03784
1515.54431
1732.05066
1948.55701
2165.06323
2598.07593
3464.10132
4330.12646
6495.18994
8660.25293
12990.37990
17320.50590
25980.75980
34641.01170
43301.26170
93.96925
187.93851
281.90778
375.87698
469.84631
563.81555
657.78479
751.75403
845.72327
939.69257
1174.61572
1409.53894
1644.46191
1879.38513
2114.30811
0.00223
0.00336
0.01332
O.U2030
0.01651
0.01459
0.01385
0.03184
0.03945
0.02816
0.03179
0.03032
0.02829
0.02444
0.01789
0.01153
0.00958
0.00579
0.00454
0.00283
0.00210
0.00164
0.00115
0.00205
0.00275
0.00279
0.00226
0.00635
0.00713
0.00373
0.01468
0.00992
0.00459
0.01560
0.02205
0.02488
0.02400
0.03322
0.02752
0.01996
0.01401
0.00852
0.00633
0.00424
0.00334
0.00202
0.00179
0.00136
0.00116
0.00204
0.00193
0.00196
0.00221
0.00595
0.00876
0.01381
0.00743
0.00781
0.01575
0.02653
0.02600
0.02324
0.01219
225.60
231.60
274.30
-304.80
310.90
310.90
317.00
347.50
353.60
353.60
359.70
365.80
384.00
384.00
378.00
378.00
378.00
380.00
400.00
400.00
360.00
360.00
213.40
225.60
231.60
231.60
225.60
243.80
249.90
243.80
304.80
304.80
286.50
329.20
347.50
353.60
353.60
384.00
384.00
384.00
378.00
365.80
371.90
360.00
360.00
340.00
380.00
350.00
213.40
225.60
225.60
225.60
225.60
243.80
262.10
286.50
280.40
292.60
323.10
353.60
359.70
359.70
329.20
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
.ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL ,
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
External Review Draft
Do Not Cite or Quote
-------
-855.05090
-1026.06104
-1368.08130
-1710.10181
-2565.15283
-3420.20337
-5130.30518
-6840.40674
-10260.61040
-13680.81450
-17101.01760
-17.36484
-34.72969
-52.09453
-69.45937
-86.82422
-104.18906
-121.55391
-138.91873
-156.28360
-173.64844
-217.06055
-260.47269
-303.88474
-347.29691
-390.70898
-434.12109
-520.94531
-694.59375
-868.24219
-1302.36353
-1736.48438
-2604.72656
-3472.96875
-5209.45264
-6945.93701
-8682.42188
-0.00003
-0.00006
-0.00009
-0.00012
-0.00015
-0.00018
-0.00021
-0.00024
-0.00027
-0.00030
-0.00038
-0.00045
-0.00053
-0.00060
-0.00068
-0.00075
-0.00091
-0.00121
-0.00151
-0.00226
-0.00302
-0.00453
-0.00604
-0.00906
-0.01208
-0.01510
Volume VH
Appendix VII-4
2349.23145
2819.07764
3758.77026
4698.46289
7047.69385
9396.92578
14095.38770
18793.85350
28190.77540
37587.70310
46984.62890
98.48077
196.96155
295.44235
393.92307
492.40381
590.88470
689.36542
787.84613
886.32697
984.80768
1231.00964
1477.21143
1723.41345
1969.61523
2215.81738
2462.01929
2954.42285
3939.23071
4924.03809
7386.05713
9848.07715
14772.11430
19696.15430
29544.22850
39392.30860
49240.38670
100.00000
200.00000
300.00000
400.00000
500.00000
600.00000
700.00000
800.00000
900.00000
1000.00000
1250.00000
1500.00000
1750.00000
2000.00000
2250.00000
2500.00000
3000.00000
4000.00000
5000.00000
7500.00000
10000.00000
15000.00000
20000.00000
30000.00000
40000.00000
50000.00000
0.01592
0.02119
0.01957
O."0ft09 -
0.00596
0.00551
0.00387
0.00283
0.00174
0.00152
0.00116
0.00117
0.00204
0.00193
0.00193
0.00214
0.00563
0.00902
0.01994
0.01919
0.01263
0.02377
0.03509
0.02532
0.02231
0.01469
0.02307
0.02015
0.01530
0.01077
0.00640
0.00497
0.00343
0.00302
0.00183
0.00133
0.00106
0.00118
0.00205
0.00193
0.00190
0.00206
0.00392
0.00820
0.01354
0.02341
0.01513
0.04249
0.01430
0.01720
0.01011
0.02035
0.01846
0.02003
0.01555
0.00990
0.00784
0.00627
0.00337
0.00239
0.00179
0.00125
0.00101
347.50
378.00
385.00
371.90
329.20
349.00
360.00
360.00
340.00
370.00
350.00
213.40
225.60
225.60
225.60
225.60
243.80
262.10
292.60
298.70
298.70
335.30
365.80
359.70
359.70
341.40
378.00
384.00
378.00
365.80
341.40
339.90
340.00
360.00
340.00
330.00
320.00
213.40
225.60
225.60
225.60
225.60
237.7D
256.00
280.40
298.70
292.60
353.60
323.10
341.40
317.00
359.70
359.70
378.00
383.40
359.70
371.90
380.10
360.00
340.00
380.00
350.00
350.00
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PER I »
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
PERIOD
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL ,
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
ALL
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
8760
External Review Draft
Do Not Cite or Quote
-------
APPENDIX VH-5
Off-Site Accident and Spill Frequency Analysis
-------
OFF-SITE ACCIDENT AND SPILL FREQUENCY ANALYSIS
FOR THE WTI FACILITY
Summary
Spills may occur during waste transport as a result of both major accidents and
minor valve and fitting leaks. Based on an evaluation of site-specific traffic accident
data, a collision-related spill involving trucks bringing waste to the WTI facility is
estimated to have about a 1 in 60 chance of occurring each year on State Route 39 (SR
39) in East Liverpool, Ohio. Non-collision related are estimated to have about a 1 in 40
chance of occurring each year over the same route. Considering both collision and non-
collision releases, a spill of greater than 100 gallons is estimated to have a 1 in 60 chance
of occurring each year along SR39 in East Liverpool. A spill of greater than 5,000
gallons is estimated to have a 1 in 295 chance of occurring each year.
I. Collision-related Spill Frequency
The collision-related spill frequency for WTI trucks was derived using the equation
shown in Table 1 and described below.
The potential number of spills each year on SR 39 involving trucks carrying waste to
WTI is estimated by multiplying the number of accidents each year involving trucks
carrying waste to WTI by the probability of a spill occurring during a truck accident:
where:
Sw
A.
Ps =
Number of spills involving trucks carrying waste to WTI (spills/year);
Number of accidents involving trucks carrying waste to WTI
(accidents/year); and
Probability of a spill resulting from a collision (unitless).
Volume VII
Appendix VII-5
-1-
External Review Draft
Do not cite or quote
-------
According to FEMA (1993) the number of spills per truck accident (P.) is approximately
0.2, or about 1 spill for every five collisions. The potential number of collisions each
year on SR 39 involving trucks carrying waste to WTI (Aw) is calculated by multiplying
the overall truck accident frequency on SR 39 by the annual vehicle miles travelled
(AVMT) on SR 39 by trucks carrying waste to WTI:
Aw = AFt x AVMTW
where:
AFt = Overall truck accident frequency on SR 39 (accidents/vehicle-
miles); and
AVMTW = Annual vehicle miles travelled on SR 39 by trucks carrying
waste to WTI (vehicle-miles/year).
The overall truck accident frequency on SR 39 (AF,) is equal to the total number of
truck accidents on SR 39 (A,) each year divided by the AVMT on SR 39 by all trucks
(AVMT,):
AF, = At + AVMT,
where:
A, = Number of overall truck accidents on SR 39 (accidents/year);
and
AVMT, = Overall truck AVMT (vehicle-miles/year).
The AVMTW is equal to the number of trucks carrying waste to WTI on SR 39 annually
(Nw) multiplied by the length of SR 39 in East Liverpool (D):
AVMT = tf x D
where:
Nw = Number of trucks carrying waste to WTI on SR 39 (trucks/year); and
D = Length of SR 39 in East Liverpool (miles/truck).
The Traffic Crash Records Division of the Ohio Department of Public Safety (ODPS)
provided the number of truck accidents on SR 39 (At) in East Liverpool between 1990
Volume VII External Review Draft
Appendix VII-5 -2- Do not cite or quote
-------
and 1995 (see Attachment 1). These figures include pickup trucks and vans as well as
tractor trailer trucks. The number of trucks carrying waste to WTI on SR 39 (Nw) was
estimated to be 3,850, based on the tons of waste shipped to WTI annually (77,000
tons/year) and the assumption that each truck transports 20 tons at a time (77,000
tons/year * 20 tons/truck = 3,850 trucks/year). According to ODPS, the length Of SR
39 in East Liverpool (D) is 339 miles. The calculation of A, is summarized in Table 2.
The AVMT on SR 39 by all trucks (AVMT,) was calculated using the equation
shown in Table 3. AVMT, is equal to the product of the general vehicle daily miles
travelled (DVMTGV), the fraction of truck DVMT to general vehicle DVMT in Ohio
State (F), and a conversion factor of 365 days/year:
AVMTt = DVMTfjy x F x 365 days/year
where:
DVMTov = General vehicle DVMT (vehicle-miles); and
F = Fraction of truck DVMT to general vehicle DVMT (unitless).
The ODOT provided general vehicle DVMT for SR 39 in East Liverpool (see
Attachment 2), but was unable to provide similar data for trucks on this route.
However, such data are available for other portions of SR 39. Between 1990 and 1994,
the fraction of truck DVMT to general vehicle DVMT on SR 39 (F) was approximately
0.06 in Columbiana County, and 0.08 in the State. Although the traffic in Columbiana
County is likely to be more representative of traffic in East Liverpool, the fraction of
truck DVMT to general vehicle DVMT from Ohio State was used as a conservative
measure. The truck DVMT was converted to truck AVMT by multiplying by 365
days/year.
On the basis of the foregoing assessment, it is estimated that the frequency of collision-
related spills on the local access route is 0.017 per year, or about once in 60 years.
II. Non Collision-Related Spill Frequency
According to FEMA (1993), the likelihood of a transportation spill resulting from all
causes including minor valve and fitting leaks as well as collisions, is about 2 1/2-fold
higher than the likelihood of a collision-related spill. Thus, the combined collision and
non-collision related spill frequency is about 0.043 per year (once in about 25 years), and
the non-collision related spill is approximately 0.026 per year (once in 40 years).
Volume VII External Review Draft
Appendix VII-5 -3- Do not cite or quote
-------
HI. Frequency of a Specific Size Spill
Two different spill sizes were chosen for evaluation in the Accident Analysis: 100
gallons and 5,000 gallons.
According to FEMA (1993), based on available information on spill sizes, and
considering the likely causes of accidents, it can be assumed that 20% of collision-related
spills will result in the loss of the entire tanker contents. In the Accident Analysis the
off-site spill scenario is assumed to involve a 5,000 gallon tanker. On this basis, it has
been assumed that 20% of all collision-related spills would be 5,000 gallons. The
frequency of a 5,000 gallon spill on the local access routes is thus 0.0034 per year, or
approximately once in 295 years.
The distribution of liquid releases from full size tankers (minimum 4,000 gallon
capacity) during highway transit between 1971 and 1986 is presented in Table 4. As
shown in Table 4, when all spills are considered, approximately 40% are 100 gallons or
larger. On this basis, it has been assumed that 40% of all spills (including both collision
and non-collision related spills) would be 100 gallons or larger. The frequency of a 100
gallon spill on the local access route is thus 0.017 per year, or approximately once in 60
years.
The calculation of frequency for 5000 gallon and 100 gallon spills is summarized in
Table 5.
3999OPCOOQA7F.W51
Volume VII External Review Draft
Appendix VII-5 -4- Do not cite or quote
-------
TABLE 1
Number of Spills from WTI Truck Accidents
Sw = AwxPs
Parameter
Sv = Number of Spills Involving Trucks Carrying Waste
to WTI (spills/year)
1990
1991
1992
1993
1994
Average 1990-1994
A, = Number of Accidents Involving Trucks Carrying
Waste to WTI (accidents/year)
1990
1991
1992
1993
1994
Average 1990-1994
P, = Probability of a Spill Resulting from a Collision
(unitless)
Value
0.012
0.014
0.022
0.008
0.026
0.017
0.06
0.07
0.11
0.04
0.13
0.08
02
Reference
Calculated
•
Calculated -
See Table 2
FEMA1993
Volume VII
Appendix VII-5
-5-
External Review Draft
Do not cite or quote
-------
•
TABLE 2
Number of WTI Trucks Accidents
Aw = AF, x AVMTW
where:
AF, = A, * AVMT,
and
AVMTW = Nw x D
Parameter
A» = Number of Accidents Involving Trucks Carrying
Waste to WTI (accidents/year)
A, = Number of Overall
AVMT, = Overall Truck
(vehicle-miles per year)
Nw * Number of Trucks
(trucks/year)
1990
1991
1992
1993
1994
Average 1990-1994
Truck Accidents (accidents/year)
1990
1991
1992
1993
1994
Average 1990-1994
AVMT in East Liverpool
1990
1991
1992
1993
1994
Average 1990-1994
Carrying Waste to WTI on SR 39
D = Length of SR 39 in East Liverpool (miles)
Value
0.06
0.07
0.11
0.04
0.13
0.08
5
6
8
3
10
6
1,155^97
1,163,448
929,436
948,883
989,208
985,780
3,850
339
Reference
Calculated
ODPS 1995
Calculated -
See Table 3
Calculated -
see text
ODOT 1995
Volume VII
Appendix VII-5
-6-
External Review Draft
Do not cite or quote
-------
TABLE 3
Overall Truck YVMT
AVMT, = DVMTcv x F x 365 days/year
Parameter
AVMT, = Overall Truck AVMT in East Liverpool (vehicle-miles
per year)
1990
1991
1992
1993
1994
Average 1990-1994
DVMTcv = General Vehicle DVMT in East Liverpool
(vehicle-miles per day)
1990
1991
1992
1993
1994
Average 1990-1994
F = Fraction of Truck DVMT to General Vehicle DVMT in Ohio
State (unitless)
1990
1991
1992
1993
1994
Average 1990-1994
365 (days/year)
Value
1,155,597
1,163,448
929,436
948,883
989,208
985,780
35,178
35,417
31,830
32,496
33,877
• 33,760
0.09
0.09
0.08
0.08
0.08
0.08
Reference
Calculated
ODOT 1995
Calculated from
ODOT 1995
Conversion Factor
Volume VII
Appendix VII-5
-7-
Draft
Do not cite or quote
-------
TABLE 4
Distribution of Cargo Losses from Full Size Tankers
During Highway Transit in the U.S. from 1971 to October 1986
Size of Spill
(gallons)
l
10
20
40
60
100
400
700
3,000
5,000
8,000
15,000
Number of Incidents
Less Than or Equal
to Size of Spill
452
2,937
4378
6,017
7340
8,695
10,866
11^17
13,097
13,740
14,247
14,475
Cumulative
Frequency
of Spill
0.03
0.20
030
0.42
0.51
0.60
0.75
0.80
0.90
0.95
0.98
1.00
Source: USDOT. 1986.
Volume VII
Appendix VII-5
-8-
Draft
Do not cite or quote
-------
» TABLES
Frequency of Specific Size Spill Occurring on SR 39
Size of Spill
(gallons)
100
5,000
Number of Spills
Each Year
Involving Trucks
Carrying Waste
to WTI (S.)
(spills/year)
0.043
0.017
Frequency of
Specific Size
Spill Occurring
0.40
020
Frequency of
Size Spill
Occurring on
SR 39 (per year)
0.017
0.0034
Recurrence
Interval (Years)
of Specific
Size Spill
Occurring on
SR39
60
295
Volume VII
Appendix VII-5
-9-
Draft
Do not cite or quote
-------
REFERENCES
ENVIRON Corporation, Inc. (ENVIRON). 1988. Site assessment phase 4B: Risk
assessment, Volume 2, Appendices A through D. January. Page C-136.
Federal Emergency Management Agency (FEMA). 1993. Handbook of chemical hazard
analysis procedures. NTIS PB93-158756.
Ohio Department of Public Safety (ODPS). 1995. Traffic Crash Records Section.
Facsimile on totals of crashes occurring on SR 39 by years. August 24.
Ohio Department of Transportation (ODOT). 1995. Office of Technical Services.
Letter on Travel Data for SR 39 in East Liverpool, Columbiana County. August 31.
United States Department of Transportation (USDOT). 1986. Hazardous Materials
Information System.
3999CPCCOOA7F.W51
Volume VII Draft
Appendix VII-5 «1Q_ Do not cite or quote
------- |