United States Air and Energy Engineering
Environmental Protection Research Laboratory
Agency Research Triangle Park NC 27711
EPA/600/7-87/015
May 1987
Research and Development
&EPA
Criteria Pollutant
Emission Factors for the
1985 NAPAP
Emissions Inventory
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EPA-600/7-87-015
May 1987
CRITERIA POLLUTANT EMISSION FACTORS
FOR THE 1985 NAPAP EMISSIONS INVENTORY
By
Margie B. Stockton
John H. E. Stelling
Radian Corporation
Post Office Box 13000
Research Triangle Park, North Carolina 27709
EPA Contract No. 68-02-3994
Work Assignment No. 83
Project Officer
J. David Mobley
Air and Energy Engineering Research Laboratory
U. S. Environmental Protection Agency
Research Triangle Park, North Carolina 27711
This project was conducted
in association with the
National Acid Precipitation Assessment Program
Prepared for:
OFFICE OF RESEARCH AND DEVELOPMENT
U. S. ENVIRONMENTAL PROTECTION AGENCY
WASHINGTON, D.C. 20460
U.S. Environmental Protection Agency
Region 5.Library(PL-12J)
77 West Jackson Boulevard, J2th Floor
Chicago, IL 60604-3590
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NOTICE
This document has been reviewed in accordance with
U.S. Environmental Protection Agency policy and
approved for publication. Mention of trade names
or commercial products does not constitute endorse-
ment or recommendation for use.
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FOREWORD
This report describes the development of emission factors for volatile
organic compounds (VOC's), nitrogen oxides (NOJ, and sulfur oxides (SO )
X A
emissions for a number of source classification categories (SCC's). An
emission factor listing for five criteria pollutants (particulate matter,
nitrogen oxide, sulfur oxide, volatile organic compounds, and carbon
monoxide) is included. All emission factors reported in AP-42 through the
Fourth Edition (September 1985) and Supplement A to AP-42 (December 1986)
are presented in table format. Additionally, emission factor estimates for
VOC, NO , and SO that were developed during the current work are presented.
A A
The project was administered by the U. S. Environmental Protection Agency
(EPA) with funding from the National Acid Precipitation Assessment Program
(NAPAP) Task Group on Emissions and Controls. David J. Beecy of the U. S.
Department of Energy serves as chairman of this task group. The EPA Project
Officer was J. David Mobley. The project has been a cooperative effort with
assistance from EPA's Air and Energy Engineering Research Laboratory (AEERL)
and Emerico L. Martinez, William H. Lamason, Arch A. MacQueen,
E. Susan Kimbrough, and Charles 0. Mann of the EPA's Office of Air Quality
Planning and Standards (OAQPS).
m
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CONTENTS
Pace
Foreword ii
List of Tables vii
Executive Summary viii
Abbreviations and Symbols xiii
Conversion Factors xv
1. Introduction 1
2. NEDS SCC'S and Emission Factor Listing 3
3. State Submittals to NEDS Which Required Development of
Emission Factors 5
4. Sources of Information 7
5. Changes to NEDS Listing 18
6. Quality of New Emission Factor Estimates 19
7. Emissions Calculation Procedures 20
8. Recommendations for Further Study 23
9. Source Classification Codes and Emission Factors 27
External Combustion Boilers 29
Electric Generation 29
Industrial 30
Commercial/Institutional 33
Manufacturing Industries 36
Chemical Manufacturing 36
Food and Agriculture 63
Primary Metal Production 63
Secondary Metal Production 77
Mineral Products 84
Petroleum Industry 97
Pulp and Paper Industry 99
Rubber and Miscellaneous Plastics Products 103
Fabricated Metal Products 104
Oil and Gas Production 106
Textile Products 109
Printing and Publishing - Typesetting 110
Miscellaneous Manufacturing Industries Ill
Organic Solvent/Petroleum Product Evaporation 112
Dry Cleaning/Degreasing 112
Surface Coating Operations 114
Petroleum Product Storage/Refineries,
Oil and Gas Fields Only 122
Bulk Terminals/Plants - Petroleum
Storage Tanks 125
Printing/Publishing - Printing Processes 128
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CONTENTS (Continued)
Page
Transportation and Marketing of
Petroleum Products 129
Organic Chemical Storage 131
Organic Chemical Transportation 143
Organic Solvent Evaporation - Miscellaneous 143
Solid Waste Disposal 145
Government 145
Commercial/Institutional 145
Industrial 146
Appendices
A. Notes to the Table 149
B. Footnotes from Original NEDS Document 189
C. Summary of State Requests for Emission Factor
Development 193
D. Estimating Fugitive Emissions of VOC From Chemical
Units 203
E. Changes to the SCC Listing Since October 1985 207
VI
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LIST OF TABLES
Table Page
1 Summary of Emission Factor Development ix
2 Summary of Emissions Data Provided by States 9
C-l Emission Factor Development from State Quick Look
Reports 194
C-2 SCC's from Quick Look Reports for Which Emission
Factor Development was not Appropriate 198
D-l Example of Emissions Estimate Using the AID Approach . . . 205
E-l Changes to the SCC Listing Since the 1985 NEDS Report. . . 208
vn
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EXECUTIVE SUMMARY
As part of the National Acid Precipitation Assessment Program (MAPAP),
the Air and Energy Engineering Research Laboratory (AEERL) of the U. S.
Environmental Protection Agency (EPA) updated the October 1985 NEDS Source
Classification Codes and Emission Factor Listing that was prepared by EPA's
Office of Air Quality Planning and Standards (OAQPS). In Phase I of the
update (EPA-600/7-86-052, December 1986), volatile organic compound (VOC)
emission factor estimates were generated for those source classification
categories (SCC's) where substantial amounts of VOC emissions were expected.
The major emphasis of that effort was on organic chemical manufacturing
processes and storage of petroleum products and organic chemicals. This
report describes the second phase of the update which consisted of
developing VOC emission factor estimates for all remaining SCC's.
Additionally, State Air Offices have submitted reports to NEDS on emissions
from point sources within their States. The SCC's appearing in these
reports which previously lacked emission factors were targeted as high
priority SCC's for the development of volatile organic compound (VOC),
nitrogen oxide (NO ) and sulfur oxide (SO ) emission factors.
The SCC's and emission factors that are reported in OAQPS's 198!> NEDS
report resulted from updating all emission factor changes through AP-42,
Fourth Edition. During this effort, the SCC listing was revised to
incorporate all changes through Appendix A to AP-42 (October 1986). This
report also contains a number of new SCC's and changes to existing SCC's
that have been previously listed. A complete listing of all SCC's and
emission factors published in the 1985 NEDS document, as well as the
emission factor estimates developed during Phase I and Phase II of the
update are included in this report.
In the current work by AEERL, the primary objective was to provide VOC
emission factor estimates for all SCC's that had no current listing of VOC
emission factors. Also included in this work was the development of NOX and
SO emission factor estimates for SCC's which were included in reports
rt
vm
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submitted by States that previously lacked these factors. The new emission
factor estimates resulting from this current work are not of the same known
quality as emission factors tabulated in AP-42. They represent best
estimates which have not been subjected to rigorous quality assurance.
These factors were generated from estimates taken from the literature, from
averaging of data submitted by 13 State air quality offices, and through
technology transfer of emission factors for SCC's from similar industries.
Extensive notes and references are supplied in an appendix explaining how
the new emission factor estimates were generated. In some cases, these
notes give an indication of data quality by reporting the number of emission
tests used to develop a factor.
State Contacts
Thirteen States were contacted to obtain emissions data from emission
inventories, test reports, and permit files. States which have large
industrial sectors and potentially large emission sources were specifically
targeted during this effort. Emissions data were supplied by 12 of the
States, seven through computerized emissions inventories and five through
review of permit files. Emission factor estimates were generated by
averaging the emission data submitted for each SCC. In some cases, States
or industries were recontacted to provide more complete process descriptions
and production rates. States provided a substantial amount of emissions
data on metal operations (both primary and secondary) and on mineral
products operations.
Literature Review
A number of source specific documents, including Background Information
Documents (BIDs), Industrial Process Profiles, Source Assessments, and
chemical specific emission source survey documents were reviewed to gather
information on emissions and processes. These documents provided useful
information on process descriptions, operating parameters, raw materials,
and end products for many source categories. This information was used to
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compare similar processes in different industries in order to apply
technology transfer of emission factors across industries where appropriate.
The Industrial Process Profiles, although somewhat outdated (published in
1977 and 1980), proved especially useful for this exercise.
State Reports Requiring Emission Factor Calculations
In 1985, EPA asked States to submit emissions data for large sources of
criteria pollutants. Emphasis was placed on SO , NO , and VOC emissions
A A
from sources emitting over 100 tons/year. Source test emissions data have
been submitted, as well as emission estimates based on AP-42 emission
factors or engineering judgement. Where no emission factors were available,
States have requested that emissions be calculated for them by the National
Emissions Data System (NEDS). NEDS calculates emissions by using emission
factors already in the system for an SCC. Where no emission factors have
ever been reported, the SCC's were flagged for emission factor development
as a high priority for this work assignment.
Results
At the completion of the Phase II effort, 99 percent (2725) of the
SCC's have VOC emission factors or emission factor estimates associated with
them or do not need emission factors due to their general description. Of
these, 37 percent (1006) were developed during this effort. Emission
factors for NO and SO are Included for 75 percent of the SCC's in the
rt A
listing. Table 1 summarizes the emission factor development for the SCC's
currently contained in NEDS and shows a breakdown of progress by major
source category. During this effort, over 100 VOC emission factors were
developed in each of the following major source categories: chemical
manufacturing, primary metals operations, and secondary metals operations.
Forty-six States sent in reports on emissions for SCC's in which
emission factor development was necessary for NO , SO , and VOC. Emission
A A
factors for 293 different SCC's were included in these reports. Of the
293 SCC's for which factors were needed, 130 NOX emission factors
(98 percent of the NOV requests) were developed, 128 SO emission factors
X A
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TABLE 1. SUMMARY OF EMISSION FACTOR DEVELOPMENT
X
Major Source Category
Combustion Source*
Chemical Manufacturing
Inorganic Chemical Storage
Food and Agriculture
Primary Metal*
Secondary Metal*
Mineral Product*
Petroleum Operations
Pulp and Paper
Rubber and Plastic*
Fabricated Metal*
Oil and Cas Production
Textiles
Organic Solvent Evaporation
Petroleum Storage
Chemical Storage
Solid Haste Disposal
Other*
TOTAL
Total Number
of SCC 'a
In Category
190
723
29
151
229
215
387
56
•7
38
52
29
21
270
139
289
62
-12Z
3157
Number of SCC '3
for Which
Emission Factors
are Inappropriate
8
70
6
22
13
20
31
8
26
7
19
8
12
41
17
52
4
-35.
399
Total Number of SO
Emission Factors
(X Completed)
179 (98X)
179 (34X)
15 (7SX)
102 (82X)
142 (70S)
126 (68X)
321 (91X)
39 <84X)
51 (89X)
6 (34X)
24 (83X)
12 (69X)
0 (OX)
229 (100X)
122 (100X)
237 (100X)
45 (79X)
145 (91Z)
1974 (75X)
Total Number of NO
Emission Factors *
(X Completed)
177 (97X)
192 (361)
18 (86X)
102 (82X)
120 (60X)
131 (70X)
328 (93X)
39 (84 X)
52 (90X)
6 (34X)
26 (86X)
11 (66X)
0 (OX)
229 (100X)
122 (100X)
237 (100X)
44 (77X)
142 (90X)
1976 (75X)
Total Number of VOC
Emission Factors
(X Completed)
182 (100X)
612 (94X)C
26 (100X)
129 (100X)
210 (100X)
195 (100X)
354 (100X)
48 (100X)
65 (100X)
31 (100X)
35 (100X)
21 (100X)
9 (100X)
229 (100Z)
122 (100X)
237 (100X)
58 (100X)
162 (100X)
2725 (99X)
These Include the "General Processes* (-01) codes, the "Other/Not Classified* (-98, -99) codes, and "Specify In Coanencs" (-888) codes.
b
These percentage* Include all SCC'* for which emission factors have been developed and all SCC's for which emission factor development Is
not required (see note a).
Emission factors for fugitives can not be developed until nationwide equipment counts become available for each chemical manufacturing
Industry.
d
•Other" category Includes numerous Mull categories such as building construction, electrical equipment, printing and publishing, and
photographic equipment.
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(99 percent of the SO requests) were developed, and 169 VOC emission
^
factors (100 percent of the VOC requests) were developed. These emission
factors are based on data supplied in published literature and technology
transfer of existing emission factors from similar processes. Many of the
State submittals were received late in the project, and emission factor
development is on-going. Two States had not yet submitted emissions data to
NEDS as of April 30, 1987. In its final form, this document will address
all SCC's for which State reports on emissions require emission factor
development.
Recommendations
Recommended activities for future study include the development of
Additional NO and SO emission factor estimates. The approach would be
similar to that used for VOC's. Further review of data which have been
collected from States and the literature may help generate additional NO
A
and SO emission factor estimates. Source categories targeted are chemical
A
manufacturing industries and primary and secondary metals industries.
The emission factors developed during this effort are considered of "E"
quality by AP-42 standards primarily because they are of unknown or
uncertain quality. In some cases, the factors may be of much higher
quality; however, the data should be reviewed and verified before higher
ratings are applied. Emissions testing is recommended for improving some of
these "E" rated factors, with emphasis on testing of sources with large VOC
emission factors. Identification of the SCC's for which testing is
desirable should be included in future work.
Emission factor development needs for particulate matter (PM) and
carbon monoxide (CO) should be identified to determine the amount of
additional work necessary if filling of emission factor gaps for SCC's for
these two pollutants is desired.
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LIST OF ABBREVIATIONS AND SYMBOLS
ABBREVIATIONS
A
BBL
BOF
CHP
DCBz
DCB
DCIPE
DCP
DIPB
EAF
H.S.S.
JP-4
LDV
LPG
MBA-AP
MCB
MDI
MEK
MIBK
MOV
MMA
MMBtu/Hr
NEG
PART
PO
RVP
S
SCC
Ash content of fuel on a weight-by-percent basis
*
Barrels
Basic Oxygen Furnace
Cumene Hydroperoxide
Oichlorobenzene
Dichlorobutene
Dichloroisopropyl Ether
Dichloropropane
Di i sopropylbenzene
Electric Arc Furnace
Horizontal Stud Soderberg
Naphtha-Type Jet Fuel
Light-Duty Vehicle
Liquified Petroleum Gas
Methyl Benzyl Alcohol-Acetophenone
Monochlorobenzene
Methylenebis(4-phenyl i socyanate)
Methyl Ethyl Ketone
Methyl Isobutyl Ketone
Medium-Duty Vehicle
Methyl Methacrylate
Million British Thermal Units per Hour
Negligible emissions
Particulate
Propylene Oxide
Reid Vapor Pressure is the absolute pressure of gasoline at
100°F in psia as determined by ASTM Method D323-72.
Sulfur content of fuel on a weight-by-percent basis.
Source Classification Code
xm
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LIST OF ABBREVIATIONS AND SYMBOLS (Continued)
SCFM -- Standard Cubic Feet per Minute*
Sq. Ft. -- Square Feet
TBA -- t-Butyl Alcohol
TDA -- Toluene Diamine
TDI -- Toluene Diisocyanate
VOC -- Volatile Organic Compound
V.S.S. -- Vertical Stud Soderberg
w/ -- with
w/o -- without
SYMBOLS
Ca -- Calcium
CO -- Carbon Monoxide
C02 -- Carbon Dioxide
FeSi -- Ferrosilicon
HC1 -- Hydrochloric Acid
HCN -- Hydrogen Cyanide
HN03 -- Nitric Acid
H2S04 -- Sulfuric Acid
Lb -- Pound*
MgO -- Magnesium Oxide
Na -- Sodium
NHj -- Ammonia
NOX -- Nitrogen Oxides
P205 -- Phosphorus Pentoxide
SOX -- Sulfur Oxides
Ti02 -- Titanium Dioxide
*
Readers more familiar with metric units may use the conversion table on
page xiv.
xiv
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CONVERSION FACTORS
To Convert From
To
Multiply By
Acre
Acre
Barrel (Bbl)
Barrel (Bbl)
Gallon (gal)
Inches (in)
Feet (ft)
Square feet (ft2)
Cubic feet (ft3)
Cubic feet (ft3)
Cubic feet/minute
Cubic yard (yd )
Board foot
Btu
Pound steam/hour
Btu/hour
Pounds (Ibs)
Ton
Pound/ton (Ib/ton)
Farenheit
Square Meter (m)
hectare (ha)
Gallons (gal)
Liters (1)
Liters (1)
Centimeters (cm)
Meter (m)
2
Square meter (nr)
Cubic meter (m )
Liters (1)
Cubic centimeters/second
Cubic meter (m )
Cubic meter (m )
Grams/calorie (g/cal)
Btu/hour
Watts
Kilogram (kg)
Kilogram (kg)
Gram/kilogram (g/kg)
Centigrade
4047
2.471
42
159
3.785
2.54
0.3048
0.0929
0.0283
28.316
472.0
0.77
0.0024
251.98
1400.0
0.293
0.45
907.1
0.496
(°F-32) 5/9
xv
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SECTION 1
INTRODUCTION
In October 1985, the U. S. Environmental Protection Agency (EPA) issued
the NEDS Source Classification Codes and Emission Factor Listing prepared by
EPA's Office of Air Quality Planning and Standards (OAQPS). This document
presented source classification codes (SCC's) which serve as the basis for
the National Emissions Data System (NEDS). OAQPS's 1985 document presents
emission factors for the five NEDS pollutants (particulate matter, sulfur
oxides, nitrogen oxides, volatile organic compounds, and carbon monoxide).
For many of the SCC's, no emission factors had been presented.
As part of the National Acid Precipitation Assessment Program (NAPAP),
the Air and Energy Engineering Research Laboratory (AEERL) of the U. S. EPA
updated OAQPS's 1985 document. The focus of Phase I of the update was to
supply volatile organic compound (VOC) emission factor estimates for SCC's
where substantial emissions would be expected. Minor emphasis was placed on
those SCC's where little or no VOC emissions were expected. A summary of
the work completed during Phase I of the update and a listing of VOC
emission factors is reported in VOC Emission Factors for NAPAP Emission
Inventory. EPA-600/7-86-052. The second phase of the update, described
herein, focused on the remaining SCC's where VOC emission factor estimates
were still needed. Additionally, nitrogen oxide (NO ) and sulfur oxide
(SOX) emission factor estimates were developed for SCC's where that
information had been specifically requested by States.
This report describes the Phase II effort in generating emission factor
estimates for VOC, SOX, and NOX- A complete listing of the SCC's contained
in OAQPS's 1985 NEDS document is presented in Section 9. Approximately
90 additional SCC's are included which have been added to the NEDS system
since October 1985. VOC, SO , and NO emission factors are included from
A A
the OAQPS document, as well as all emission factor estimates generated
during Phase I and Phase II of this effort. Within the table of emission
factors presented here, the SCC's for which emission factor estimates were
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added during Phase I and Phase II of the update can be identified by the
presence of a number in the NOTES column at the far right of each page, and
an asterisk in front of the estimate. Some factors listed in the 1985
Report which are not AP-42 factors also have been flagged with an asterisk.
Notes explaining how each new emission factor estimate was derived are
included in Appendix A of this report. Appendix B contains lettered
footnotes for non AP-42 factors which were included in the 1985 Report. The
new estimates, which supplement the AP-42 based factors published in
October 1985, do not meet the current requirements for development of AP-42
factors. They are based upon whatever data could be obtained from the
literature and emission factor estimates obtained from various air quality
districts within States. These emission factor estimates, however, provide
an interim means for estimating emissions until more supportable, AP-42 type
factors become available.
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SECTION 2
NEDS SCC'S AND EMISSION FACTOR LISTING
The Source Classification Codes (SCC's) presented in Section 9 comprise
the basis upon which the National Emissions Data System (NEDS) is
structured. Each SCC represents a specific process or function that is
logically associated with a point source of air pollution within a given
source category. In NEDS, any operation that causes air pollution can be
represented by one or more of these SCC's.
Also presented herein are emission factors that correspond to each SCC
from the October 1985 document for the five criteria pollutants:
particulate matter (PM), volatile organic compounds (VOC), nitrogen oxides
(NO ), sulfur oxides (SOX), and carbon monoxide (CO). These factors are
used in NEDS to automatically compute estimates of emissions associated with
a process when a more accurate estimate is not supplied to the system. Many
of these factors are taken directly from AP-42. In some cases, however,
they may be derived from information not yet incorporated into AP-42 or may
be based on the similarity of one process to another for which emissions
information does exist.
The SCC and emission factor listing reported in the October 1985 report
resulted from updating all emission factor changes through AP-42, Fourth
Edition. The 1985 report contained a number of new SCC's. Additional SCC's
have been added to NEDS subsequent to the 1985 Report at the request of
State and local agencies. Also included in the listing are changes to any
existing SCC's that appeared in the previous listing.
More information on NEDS data coding procedures may be found in AEROS
Manual Volume II: AEROS User's Manual. EPA-450/2-76-029a. Instructions for
coding specific sources may be found in the Engineering Reference Manual for
Coding NEDS and EIS/P&R Forms - Volume I: Introduction. EPA-450/4-80-007;
Volume II: Compendia of Processes. EPA-450/4-80-007; and Volume III:
Compendia of Processes. EPA-450/4-80-007. Codes used in coding NEDS data
may be found in AEROS Manual Volume V: AEROS Manual of Codes.
EPA-450/2-76-005a.
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Additional information on NEDS data retrievals may be found in the
publication NEDS National Emissions Data System Information.
EPA-450/4-80-013a. This report is an extract of a more detailed
publication: AEROS Manual Volume III: AEROS Summary and Retrieval Manual.
EPA-450/2-76-009c. AEROS Volume III contains information on not only the
NEDS system but the SAROAD (air quality) system as well.
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SECTION 3
STATE SUBMITTALS TO NEDS WHICH REQUIRED
DEVELOPMENT OF EMISSION FACTORS
Following the October 1985 NEDS/NAPAP Emission Inventory Workshop held
by EPA, a high priority was placed on States submitting emissions data to
NEDS. For NAPAP purposes, States were asked to focus on sources emitting
100 tons/year or more of SO , NO , and VOC. Various procedures may be used
A A
to calculate emissions, which are outlined in the NEDS/NAPAP Emission
Inventory Workshop Proceedings. October 1985, prepared by EPA. Source test
emissions data are considered the most accurate data. If no individual
source emissions data are available, the use of AP-42 emission factors is
recommended. AP-42 factors are not available for all sources, however. In
the absence of AP-42 emission factors, the States may use their own
judgement in estimating emissions or they may request that NEDS calculate
emissions for these sources. NEDS calculates emissions by using emission
factors already in the system for a requested SCC. If no emission factor
has ever been reported to NEDS, then resulting emissions are reported as
zero.
"Quick Look Reports" from the NEDS file were generated which flagged
those SCC's where States have indicated that NEDS calculate emissions and
NEDS has reported zero emissions. Providing NO , SO , and VOC emission
^ ^
factor estimates for these SCC's were given a high priority for this
Phase II update.
One hundred eighty-one of these requests for emission factor
calculations were addressed during this effort. The remaining 38 percent
(112) of the requests were for SCC's where it was not feasible to estimate
emission factors. These SCC's fell into two categories: "General" and
"Other/Not Specified." The "General" codes are not related to any specific
process, but rather identify, in overall terms, a category of emissions. A
listing of "General" applies to an entire category, providing a composite or
summation of emissions for the entire source. In most cases, these
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"General" SCC's are considered too general or obsolete because of the
addition to the NEDS system of more specific SCC's which represent single
vents or stacks. The second group of SCC's (which end in "97," "98," "99,"
or contain "888" as the central digits) are used to represent process
activities that may exist, but for which no specific SCC's have been
defined. These may represent very specific processes, and each reported
value from State files may represent a different process. Both the
"General" and "Other/Not Classified" SCC's are still used by many States
when process activities do not match up exactly with process descriptions of
listed SCC's. However, neither the "General" SCC's nor the "Other/Mot
Classified" SCC's were addressed during this effort. Appendix C summarizes
the State requests for emission factor calculations in more detail.
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SECTION 4
SOURCES OF INFORMATION
In the current work, the primary objective was to provide VOC emission
factor estimates for all SCC's having no VOC emission factor listed.
Additionally, NOX and SOX emission factor estimates were developed for SCC's
where that information was specifically requested by States (as explained in
Section 3). The major effort of Phase II was to obtain emissions data from
States through emissions data bases, test reports filed 1n State offices,
and emissions testing associated with permitting requirements. Emissions
data were also collected through an extensive literature search. For some
industries, literature on specific process descriptions was consulted and,
based on studies of similar processes in different industries, it was deemed
appropriate for this project to transfer emissions factors reported for
SCC's in one industry to similar SCC's in other industries. The new
emission factor estimates resulting from this current work are not of the
same known quality as emission factors tabulated in AP-42. They were
generated from sparse data from the literature and from emission factor
estimates provided by individual air quality districts within States.
The remainder of this section summarizes the sources of Information
used to generate emission factor estimates for this Phase II effort.
4.1 STAPPA/ALAPCO SURVEY
In April 1986, the State and Territorial A1r Pollution Program
Administrators and the Association of Local Air Pollution Control Officials
(STAPPA/ALAPCO) initiated a survey of all their members requesting that
emissions data be sent to the EPA for use in developing emission factors.
It was anticipated that data collected during this survey would provide
useful information for this work assignment. However, the information
submitted was of limited use in filling in emission factor gaps for NOX,
SO, and VOC.
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As of April 1, 1987, 139 State and local agencies had responded to the
survey, with 39 respondents supplying EPA with emissions data. Of the
39 agencies providing emissions data, 22 of them provided data on sewage
sludge or solid waste incinerators only for which emission factors have
already been calculated.
As part of this emission factor development task, 21 emission test
reports from the STAPPA/ALAPCO Survey were reviewed. A number of the
reports provided data for particulate emissions only and some contained
emission test summaries for SCC's for which emission factors had already
been reported in AP-42. Four emission factor estimates were developed based
on emission test reports provided through the STAPPA/ALAPCO Survey
responses.
4.2 STATE CONTACTS
A major emphasis of the Phase II work was on contacting State air
pollution control agencies in States where industries for which emission
factors had not been calculated are located. The States contacted were
selected on the basis of their having the largest portion of chemical
manufacturing industries, metals operations, and petroleum industries. It
was expected that these States would have the highest amount of
process-related emissions. During the Phase I work, six States had been
contacted; however, only one State was able to send useful data in the time
allotted. During Phase II, the other five States were recontacted along
with an additional seven States. A total of 13 States were contacted in an
attempt to gather emissions data from emission test reports and emission
inventories.
A summary of the emissions data provided through these State contacts
is presented in Table 2. Six of the States providing data do not use the
SCC system to code emission points. Data submitted were reviewed and, where
possible, SCC's were assigned based on process descriptions provided. SCC's
could not be assigned for approximately one-half of the data provided by
these States due to incomplete process descriptions or descriptions that did
8
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TABLE 2. SUMMARY OF EMISSIONS DATA PROVIDED BY STATES
State
Industrie* Data
Were Supplied For
Source of Emissions Data
State Uses
SCC System
Comments
California
Florida
Georgia
Illinois
Louisiana
New Jersey
New York
North Carolina
Ohio
Chemical manufacturing
Petroleum industry
Phosphate operations
Sulfurlc acid production
Non-metallic minerals
Mineral products
Chemical manufacturing
Secondary metal operations
Mineral products
Pulp and paper Industry
Chemical manufacturing
Petroleum industry
Phosphate operations
Mineral products
Pulp and paper industry
Secondary metal operations
Pharmaceut icals
Textiles
Mineral products
Chemical manufacturing
Secondary metal operations
Mineral products
Phosphate operations
Wood products
Textiles
Pulp and paper industry
Primary metal operations
Secondary metal operations
Mineral products
Computerized data base.
Computerized data base.
Review of emission test report
summaries.
Computerized data base
containing permit information.
Computerized data base
containing permit information.
Review of emission test report
summaries.
Computerized data base.
Review of permit files for
emissions test reports.
Computerized data base.
Yes
No
No
Yes
Yes
No
No
No
Yes
Received during Phase I effort. VOC's
Include ethane.
This was the only industry targeted
for emissions data from this State.
Other data may be available.
Data not computerized.
Report total hydrocarbons rather than
VOC's.
Additional information available in
permit files.
Data not computerized.
No production rates available.
Requires calling companies directly
to get production rates. Report
total hydrocarbons rather than VOC's.
Data not computerized.
-------
TABLE 2. SUMMARY OF EMISSIONS DATA PROVIDED BY STATES (Continued)
State
Industries Data
Were Supplied For
Source of Emissions Data
State Uses
SCC System
Comments
Pennsylvania
Texas
West Virginia
Wisconsin
Primary metal operations
Chemical manufacturing
Petroleum Industry
Mineral product*
Metals operations
Pulp and paper industry^
Computerized data base.
Review of permit files.
Computerized data base.
No
Yes
No
Yes
Limited amount of data available.
State regulates PM primarily. This
was the only Industry targeted for
emissions data from this State. Other
data may be available.
Emissions data are computerized, but
not accessible. Permit files are not
open to the public for many large
companies due to pending litigation.
Data not accessible at this time.
Limited amount of data available.
Primarily Interested In PM emissions.
-------
not match those listed in the published NEDS report. Telephone calls to
companies or a review of permit files would be necessary to acquire more
complete process descriptions.
It was assumed that States using the SCC system had assigned the SCC's
correctly. In a few cases, calculated emission factors from one State were
very different from those submitted by other States for the same SCC. This
suggests that one of the States may have assigned the SCC's incorrectly.
Emissions data for the same SCC that varied by more than an order of
magnitude were reviewed and States were recontacted to correct obvious
inconsistencies. However, no specific quality assurance measures were
employed to insure that SCC's had been correctly assigned by the States.
Computerized data provided by three of the States using the SCC system
proved to be of limited use because the States frequently use the "General"
(-01) codes and "Other/Not Classified" (-99) codes when assigning SCC's.
This is due, in part, to the age of the records in the computerized data
bases. The NEDS system of SCC's is a dynamic one with new SCC's added as
requests are received. For example, initially the "General" (-01) codes for
chemical manufacturing were the only SCC's available for each chemical
listed. Recently, the SCC system has been expanded to provide more specific
SCC's for each process vent and stack. Prior to the addition of these new
SCC's, States used the "General" (-01) codes or the "Other/Not Classified"
(-99) codes and specified the process description in the comments field.
The emissions data provided in these codes could not be readily used for
developing nation-wide emission factor estimates since different processes
were coded with the same general SCC.
4.3 TEST REPORTS ON METALS-ORIENTED OPERATIONS
A document published by JACA Corporation entitled Listing of Emission
Test Reports for the Iron and Steel Industry (updated 1986),.was reviewed
for information on NO , SO , and VOC emissions for the metals processing
A A
industry. Approximately 90 percent of the test reports addressed
particulate matter only. Although the test reports containing SO , NO , or
VOC emissions data were identified in the document, the actual data for
11
-------
these pollutants were not included. Over 50 of these test reports
maintained in the project files at JACA Corporation were reviewed resulting
in emission factor estimates for 12 SCC's.
All data extracted from these test reports were cleared for public use
through EPA Region V. Since the emissions data were extracted from
relatively old test reports (before 1980), they should be used with caution.
However, they provide emission factor estimates which are useful in the
absence of more recent data.
4.4 LITERATURE REVIEW
An extensive literature search was conducted during the Phase II work
to identify sources of NO , SO , and VOC emissions data. A number of source
^ ^
specific documents, including Background Information Documents (BIDs),
Industrial Process Profiles, Source Assessments, and chemical-specific
emission source survey documents, were used to gather information on
emissions. Some documents contained results of emission tests and presented
emission factors in table format. Others contained emission rates only and
States or companies were contacted to obtain production rates. When this
information was provided, emission factor estimates were calculated. Some
documents contained model plant specifications and associated emission
factors. All information taken directly from reports and EPA documents is
footnoted and referenced in Appendix A.
Industrial process profiles were reviewed to gain an understanding of
various processes. A series of "Industrial Process Profiles for
Environmental Use" was developed by EPA as an aid in defining the
environmental impacts of industrial activities in the United States. While
these documents are somewhat outdated (published in 1977 and again in 1980),
they provide useful information on general processes. In some cases, this
was the only literature available. Process descriptions, segmented by SCC,
are presented including information on input materials, operating
parameters, utility requirements, and waste streams. Appendices are
included with company listings, production data, and atmospheric emissions,
when available. These documents were reviewed and, where available,
12
-------
emissions data were used to calculate emission factor estimates. Where
information on emissions is not quantified for specific processes and
emissions are considered to be negligible based on the process descriptions
an emissions factor estimate of "NEG" has been assigned to the SCO. The
most useful information obtained from this series of reports was detailed
process descriptions which were used in making judgements on appropriate
technology transfers of existing emission factors (see Section 4.6).
4.5 PROCEDURES FOR CALCULATING EMISSION FACTORS
4.5.1 Storage Tanks
VOC emission factor estimates were generated using the 1986 equations
published in AP-42 Section 4.3, Fourth Edition (September 1985) for working
losses and standing losses from storage tanks. Published vapor pressure and
density data and typical tank dimensional information are supplied in an
earlier edition of AP-42 (Third Edition).
Pressure storage tanks are divided into low pressure tanks (2.5 to
15 psig) and high pressure tanks (greater than 15 psig). For high pressure
tanks, there are no atmospheric emissions from standing losses or working
losses. For low pressure tanks, losses occur only due to atmospheric
venting during filling operations. In examining emissions from pressure
storage, the vapor pressures of the chemicals in question were found in the
literature or computed using Antoine's Equation at ambient temperature
(68°F) and then compared to the 15 psig criteria. This provided a quick
check of the storage pressure of the pure component at ambient temperature.
In addition, the lower explosion limit (LEL) fraction was applied to
determine whether the chemical would be stored at high or low pressure.
Most of the chemicals listed in NEDS under the pressure storage
category have vapor pressures in excess of 15 psig and therefore would not
have emissions resulting from pressure storage. The pressure during storage
was computed assuming that the pure component chemicals are stored at
pressures associated with concentrations which are 25 percent of their lower
explosion limit for safety reasons. Some other chemicals are stored above
15 psig in pressured tanks due to their toxicity.
13
-------
4.5.2 Emissions from Combustion Sources
VOC emission factor estimates for incinerators and flares were
estimated assuming 98 percent combustion efficiencies, which is currently
accepted as achievable by EPA in its standards development activities,,
Speciated composites for ten natural gas samples were obtained from
Emissions from Refinery Process Heaters Equipped with Low-NO Burners
(KVBll-6019-1274, March 1981) and NO. Emissions from Petroleum Industry
A
Operations (API Publication No. 4311, American Petroleum Institute,
October 1979). Using these speciated profiles, natural gas was calculated
to contain between 0.5 and 1.25 percent VOC by weight. Typical densities of
natural gas were taken from the literature and emission factors were
generated. There is great variability in the operating parameters of
incinerators (i.e., temperature, residence time) which influence the
quantity of emissions and should be considered when applying these emission
factor estimates.
VOC emission factor estimates for oil-fired and process gas-fired
incinerators were estimated from emission factors presented for oil-fired
and process gas-fired heaters, because no typical speciated profiles were
obtained for these fuels. Natural gas-fired incinerators were calculated to
generate VOC emissions twice as high as the emissions from natural gas-fired
process heaters. This is due, in part, to lower temperatures and shorter
residence times of the materials in the incinerators. This same ratio of
emissions from gas-fired incinerators to emissions from gas-fired heaters
was applied to the other fuel-fired heaters to obtain emission factor
estimates for incinerators. The estimated VOC emission factors for
incinerators and flares were transferred to other industries under the
assumption that the emissions from these combustion sources depend primarily
on the type of fuel burned, rather than on the material being treated.
4.5.3 Fugitive Emissions from Organic Chemical Manufacturing
Fugitive VOC emissions or equipment leaks are not related to production
volume, as are process vent emissions. Instead, equipment leaks are related
to process unit complexity (i.e., the number of equipment components in the
14
-------
process units). Emission estimates for equipment leaks, therefore, are
presented as total annual emissions (pounds/process unit/year) for
individual process units. Estimates were prepared using data provided in
EPA's Organic Chemical Manufacturing fOCM) Series (EPA-450/3-80-025a-j),
which provided model unit equipment counts for the major sources of fugitive
emissions (pumps, valves, pressure release devices, compressors). Other
equipment types that were not listed individually were estimated from the
OCM section on fugitive emissions. The procedure used in generating these
emission factor estimates is presented in Appendix 0.
The VOC emission factor estimates for fugitive emissions which are
given in the NAPAP listing that follows are presented as pounds/process
unit/year values. In order to implement these estimates, the factor must be
coded as a user-computed estimate and the production rate given as unity.
The NEDS inventory computer program will then automatically compute the
annual emissions for equipment leaks.
4.6 TECHNOLOGY TRANSFER
Emission factors have previously been established for some groups of
sources, while factors were missing for very similar sources in other
categories. Emission factor estimates were developed for a variety of SCC's
based on the similarity of one process to another. Information gathering
involved extensive review of the literature, conversations with State air
pollution control personnel, and conversations with industry to learn more
about various processes. Descriptions of raw materials used, operating
parameters of equipment, and the manufacturing processes of products were
compared to determine the similarity of the processes. Emission factor
estimates were then generated through technology transfer.
Three categories where new emission factor estimates were generated
based on technology transfer of previously reported emission factors are
described below. A review of the footnotes (Appendix A) will identify other
areas where technology transfer was used to generate new emission factor
estimates.
15
-------
4.6.1 Process Heaters
The AP-42 background material was reviewed for calculations of emission
factors for process heaters in the oil, gas, and petroleum industry. The
emission factors listed for process heaters had been previously transferred
from those factors published for similar fuel-fired boilers. Based on the
background information, it was deemed appropriate to transfer these emission
factors to process heaters in other industries. The emissions from process
heaters depend on the type of fuel burned rather than on the material being
heated, therefore, emissions from the heater are expected to be similar in
different industries. If operating parameters (i.e., temperature and
residence time) vary greatly, emissions may be different.
4.6.2 Crushing and Grinding Operations
A series of Industrial Process Profiles for Environmental Use were
reviewed for a number of metal and mineral products industries. In many
cases, particulate matter was identified as the only atmospheric emissions
during crushing and grinding operations. The only source of VOC emissions
from crushing and grinding operations would be unbound VOC in the ore or
rock. Based on descriptions of the raw materials and the equipment used to
crush and grind the materials, it was determined that no VOC emissions would
result. Consistent with this reasoning, zero VOC emissions had been
previously reported in AP-42 for crushing and grinding of primary zinc,
secondary aluminum, bricks, cement, glass fiber, gypsum ore, lime, and sand.
4.6.3 Furnaces and Dryers
Where enough process information was available, emission factors from
various types of furnaces and dryers were transferred across industries.
For example, within the glass manufacturing industry, furnaces are listed
under wool-type glass, textile-type glass, container glass, and flat glass.
Descriptions of the different processes used to produce these types of glass
were reviewed. It was found that the operating parameters of the furnaces
16
-------
are all virtually the same. Furthermore, it was stated in Background
Information Documents that emissions from these furnaces are independent of
the type of glass produced. VOC emission factors were previously calculated
for furnaces used in producing two types of glass. These were transferred
to the other furnaces within the glass manufacturing industry.
Similar technology transfers were made for furnaces in the primary
metals industry, for dryers in the secondary metals industry, and for dryers
in the mineral products industry.
17
-------
SECTION 5
CHANGES TO NEDS LISTING
In working with the NEDS listing of SCC's and through discussions with
State agencies and industries, it was determined that some changes to the
SCC listing are needed. The SCC listing is a dynamic one with new SCC's
being added as requests are received. Some SCC's are no longer valid in
that the processes are no longer used in the United States. Other SCC's
need changes to the process descriptions or type of units listed. Final
recommendations for changes to the SCC's have resulted from working meetings
with personnel from EPA's Office of Air Quality Planning and Standards
(OAQPS) and EPA's Air and Energy Engineering Research Laboratory (AEERL).
States that had originally requested addition of some of the SCC's in
question were contacted about the recommendations.
Since the October 1985 NEDS Report, 91 new SCC's have been added to the
system and 34 SCC's have been deleted. Appendix E contains a complete
listing of the changes made to the SCC listing since the 1985 Report. Many
additions resulted from State requests for new SCC's. Other additions
represent processes that were previously listed, but with different units
for reporting emission factors. Deletions to the SCC listing resulted from
thorough review of the industry and identification of processes which are no
longer used in the United States. Examples of deleted SCC's include
oil-fired flares and chemical storage tank SCC's which were originally
misclassified. The SCC's which were deleted from this published listing
have been retained in the NEDS computer inventory, but will not be printed
in future 1istings.
18
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SECTION 6
QUALITY OF NEW EMISSION FACTOR ESTIMATES
Emission factor estimates that have been added to this NAPAP listing
are not of the known quality as the previously reported AP-42 based emission
factors. In terms of the AP-42 ratings, the estimates provided from this
effort should be considered of "E" quality because they have not been
subjected to rigorous quality assurance. In some cases, the new emission
factors may be of higher quality than this "E" rating implies. However, the
data must be extensively reviewed and verified before higher ratings could
be applied. The goal of this effort was to fill in gaps in the 1985 NEDS
document for VOC emission factors and to provide NOX and SOX emission factor
estimates for SCC's specified by States. As previously discussed,
information was gathered from a variety of sources including unverified
State data, secondary references such as draft or unpublished reports, and
personal communication.
Within the main table of this report, new emission factor estimates are
readily identified by the presence of a number in the NOTES column at the
far right of each page and an asterisk by the factor. Each new emission
factor estimate listed in this document has a note explaining the source of
information and calculation methods. These notes are found in Appendix A.
All other emission factors which do not have a number associated with them
in the NOTES column have been taken directly from the 1985 NEDS document.
Some of the factors listed in the 1985 Report are not from AP-42. These
factors have also been flagged with an asterisk and lettered footnotes in
Appendix B should be consulted to determine how these factors were derived.
19
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SECTION 7
EMISSIONS CALCULATION PROCEDURES
In order to calculate emissions using the emission factors in this
publication, certain data values must be present. These values include:
(1) an annual operating rate; (2) fuel parameter, if applicable;
(3) emission factor from the SCC file; and (4) percent (%) control
efficiency, if a control device is present. Calculated emissions are
derived as follows:
Calculated Emissions (Tons/Year) =
Annual Operating x Emission Factor x Fuel Parameter
Rate for SCC From SCC File If Applicable x 100-Control Efficiency
2,000 Pounds/Ton 100
Where:
Annual Operating Rate = SCC Units/Year
Emission Factor = Pounds/SCC Unit
Fuel Parameter = Ash or Sulfur Content of Fuel on Weight-by-Percent
(%) Basis
Control Efficiency - Pollutant Control Device Percent (%) Efficiency
7.1 FUGITIVE EMISSIONS CALCULATIONS
The NEDS SCC's were recently expanded to include many individual unit
operations within chemical process units. One additional SCC in most
chemical process units is for "Fugitive Emissions: General." Fugitive
emissions or equipment leaks are not proportional to production rate.
Rather, they are associated with process unit complexity (i.e., the number
of equipment components in the process unit). As a result, the emissions
from equipment leaks are presented in terms of pounds/year, not pounds per
SCC unit as with the other SCC's. To implement the fugitive emissions
estimate given in the listing, the source must be coded with NEDS emission
20
-------
estimation method code 3 (emissions to be calculated by a computerized
method) with an associated production volume of unity. This permits the
NEDS inventory computer program to automatically calculate emissions.
Emission estimates are presented for equipment leaks in a limited
number of chemical process unit types. Additional discussions of estimating
fugitive emissions is presented in Appendix D.
7.2 VOC EMISSIONS CALCULATION
Per agency policy and EPA guidance to States for the preparation of
emission inventories of VOC, certain VOC's that are considered to be
photochemically nonreactive under atmospheric conditions should not be
included in emission inventories for ozone SIP development. This subject is
discussed further in the report Procedures for the Preparation of Emission
Inventories for Volatile Organic Compounds, Volume I (Second Edition)
(EPA-450/2-77-028). However, some of these photochemically nonreactive VOC
are toxic (e.g., methylene chloride) and should be included in air toxics
inventories. Air toxics are not addressed specifically in this document.
Therefore, needs and requirements may differ when toxics inventories are
compiled.
Nonreactive VOC components are identified per data given in the VOC
Species Data Manual (Second Edition) (EPA-450/4-80-015) and the publication
Compilation of Air Pollutant Emission Factors. AP-42. However, some
categories do not have VOC species data. These categories use the AP-42
nonmethane VOC emission factors to represent reactive VOC emission factors.
The following compounds are considered to be photochemically nonreactive:
Methane
Ethane
Trichlorotrifluoroethane (Freon 113)
Methylene Chloride
1,1,1-Trichloroethane (Methyl Chloroform)
Tri chlorof1uoromethane
Di chlorodi f1uoromethane
21
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Chiorodi f1uoromethane
Trifluoromethane
Dichlorotetrafluoroethane
Chioropentaf1uoroethane
In some State-based data (for example, California, New York, and
Illinois), emissions of organic compounds are viewed as total organic:; or
total hydrocarbons. California also reports the fraction of reactive
organic compounds. While the classification of reactive organic compounds
is similar to EPA's definition of VOC, this classification is somewhat
different (at least in California) in that it includes ethane. In compiling
emission factors for the SCC's in the organic chemical manufacturing
section, the effect of this definition on the emission factor was deemed
negligible. The footnotes associated with emission factors reported under
VOC's should be read carefully to determine what compounds are included in
the emission factor.
7.3 S0¥ AND NOV EMISSION FACTOR CALCULATIONS
^ J\
Emissions of sulfur dioxide represent the total weight of gaseous
sulfur oxide emissions expressed as the equivalent weight of SO-. Emissions
of S03 are adjusted to the equivalent weight of SO,, by multiplying the SO,
emissions by the ratio of molecular weights (64/80) to express as the
equivalent weight of S02. The weight of S02 and S03 adjusted to an
equivalent weight of S02 are then added together and reported as S02
emissions. Particulate sulfate is reported as particulates rather than SO-.
For NOX emissions, the emissions are expressed as the equivalent weight
of N02, regardless of what nitrogen oxide species are actually emitted.
Molecular weight adjustments to an N02 basis are appropriate. The emission
factors that appear in the NEDS SCC and Emission Factor Listing are all
expressed as the equivalent weight of S02 and N02 as described above.
Normally, AP-42 emission factors for NO are expressed as N02, unless
indicated otherwise in an AP-42 footnote.
22
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SECTION 8
RECOMMENDATIONS FOR FURTHER STUDY
This section discusses the portions of the SCC listing for which
criteria pollutant emission factor estimates are still needed. In examining
those areas that are deficient in emissions data, recommendations are made
for further study to complete the emission factor estimates for the majority
of the SCC's that currently have no estimates. Potential data sources,
estimation procedures, and resource requirements are given.
The emphasis of this work assignment was on calculating VOC emission
factors for all SCC's previously lacking this information. NO and SO
A A
emission factors were also generated, but only for those SCC's that States
had used to report emissions. In future studies, emphasis should be placed
on calculating NO and SO emission factors for the remaining SCC's
n A
requiring this information. Sources of emissions data have been identified
during this effort which can be reviewed in greater detail to extract the
information needed to calculate many NO and SO emission factors.
Additional State contacts may provide emissions data for source categories
where data are still lacking.
Deficiencies in the emission factor listing for the other criteria
pollutants (particulate matter and carbon monoxide) should also be addressed
in future studies.
8.1 N0¥ AND S0¥ EMISSION FACTORS
A^ A
Source categories that States specifically used to report NO and SO
A A
emissions which still require emission factor calculations are the highest
priority areas for future studies. EPA is still receiving reports from
States which must be addressed as they are received. Useful data were
obtained for calculating many NO and SO emission factors during the
/\ A
Phase II update, but due to time and resource limitations these emissions
data have not been thoroughly reviewed.
23
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8.1.1 State Data
Five of the thirteen States (Illinois, New York, Louisiana, Ohio, and
Texas) submitting information during the Phase II effort provided NO and
A
SO data which may be useful in calculating additional emission factor
y\
estimates. It will be necessary to recontact the States to acquire more
complete process descriptions in order to assign SCC's or to acquire the
production data necessary to calculate emission factors from the emissions
test data already supplied. In some cases, the States can not supply this
information due to confidentiality agreements with companies. The States
have suggested contacting companies directly to gain access to the necessary
information.
These State data may be useful in calculating NO and SO emission
factor estimates for the chemical manufacturing industry (Illinois, Texas,
and Louisiana) and for metal processing operations and mineral products
manufacturing (Illinois, New York, and Ohio).
8.1.2 Additional State Contacts
States in the western United States may be able to provide additional
information on metals processing, mining operations, and logging operations.
Additional contacts should be made to States where these operations are
large sources of atmospheric emissions (e.g., New Mexico and Arizona for
mining, Oregon and Washington for logging). Other States had been contacted
previously for information on one specific process (i.e., Wyoming for sodium
carbonate, Montana for vermiculite production, and Tennessee for explosives
manufacturing). Initial contacts have been made at these States and it may
be possible to obtain additional data through follow-up contacts.
California provided large quantities of emissions data on VOC as part of the
Phase I work. This State could possibly provide as much information on SO
/\
and NO emissions.
24
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8.1.3 Literature Review
Pertinent literature on atmospheric emissions from many source
categories has been obtained during the Phase I and Phase II work. These
reports and documents were extensively reviewed to extract VOC emissions
data. They should be reviewed a second time to identify SOX and NOX
emissions data. The published literature also provided valuable information
on process descriptions, operating parameters, raw materials, and end
products for many source categories. This information was useful in
comparing similar processes in different industries and applying technology
transfer of emission factors across industries. The technology transfers
were applied primarily for VCC emission factors. Additional work is needed
to apply technology transfer for NO and SO emission factors.
/\ A
8.2 PARTICULATE MATTER (PM) AND CARBON MONOXIDE (CO) EMISSION FACTORS
Future studies should also address gaps in the NEDS listing for
particulate matter (PM) and carbon monoxide (CO). Initially, the NEDS
listing would need to be reviewed to identify which industries and source
categories are lacking in PM and CO emission factors. At the same time,
literature should be reviewed to identify the industries and source
categories where large PM or CO emissions are expected. This information
would help to determine the initial focus.
Many emission factors for PM have already been incorporated from AP-42
Fourth Edition and Supplement A to AP-42. Information from numerous EPA
standards setting activities (i.e., New Source Performance Standards) has
been reviewed, and AP-42 emission factors have been generated. Process
descriptions and details concerning equipment types and materials used in
various processes should be reviewed in an effort to apply technology
transfer of PM emission factors from one industry to another.
CO emission factors have not been developed for as many categories as
the other criteria pollutants. Emission estimates for this pollutant have
been given lower priority in factor development work. The NEDS listing
should be reviewed along with literature on CO emissions to determine which
source categories are large emitters of CO.
25
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8.3 VOC EMISSION FACTORS
The emission factor estimates developed during Phase I and Phase II of
this work are of unknown or uncertain quality and do not meet AP-42
standards. They are based on a variety of sources including unverified
State data, secondary references such as draft or unpublished reports, and
personal communication. The information supplied here provides a strong
base on which to develop AP-42 emission factors in the future. Future work
should include identification of source categories for which high quality
data have been collected. In some cases, emissions testing is recommended
for improving the poorest quality factors with the larger impact on total
emissions. Emphasis should be placed on testing of sources with large VOC
emission factors where emissions are expected to be significant.
26
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SECTION 9
SOURCE CLASSIFICATION CODES AND EMISSION FACTORS
This section contains emission factors previously reported in OAQPS's
1985 document, NEDS Source Classification Codes and Emission Factor Listing,
and emission factors recently developed by the Air and Energy Engineering
Research Laboratory (AEERL) of the U. S. Environmental Protection Agency.
Emission factor estimates which have been added as a result of the Phase I
and Phase II effort can be identified by an asterisk and by the presence of
a number in the NOTES column to the far right of each page. Notes
explaining how each new emission factor estimate was derived are included in
Appendix A of this report. All other emission factors listed have been
extracted directly from OAQPS's 1985 NEDS document. Lettered footnotes
appearing in the table were reprinted directly from the 1985 NEDS document
and are included in Appendix B of this report. Some of these lettered
footnotes identify non AP-42 factor which were included in the 1985 Report.
These non AP-42 factors have also been flagged with an asterisk.
Some emission factors have been presented as negligible (NEG) in the
table. For SCC's where no quantitative data were available and a review of
the process and raw materials indicate that the source is a minor emission
source (less than 100 tons/year), a "NEG" has been assigned. Before using
any emission factors from this table the footnotes and notes reported in the
appendices should be consulted to give the user an indication of how the
emission factors were derived.
27
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(Intentionally Blank)
28
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ro
sec
Process
EXTERNAL COMBUSTION BOILERS - ELECTRIC GENERATION
PART
Lbs/Unlt
- 4911*
SO
Lbs/unit
NO
Lbs/flnit
VOC
Lbs/Unit
CO
Lbs/Unit
Units Notes
Anthracite Coal
1-01-001-01 -
1-01-001-02 -
Pulverized Coal
Traveling Grave Stokers
10.0 A
9.1
39
39
.0
.0
S
S
18.0
10.0
0
0.
.07
,07
0.
0,
.6
.6
Tons Burned
Tons Burned
Bituminous Coal
1-01-002-01 -
1-01-002-02 -
1-01-002-03 -
1-01-002-04 -
1-01-002-05 -
1-01-002-12 -
1-01-002-17 -
Subbituminous
1-01-002-21 -
1-01-002-22 -
1-01-002-23 -
1-01-002-24 -
1-01-002-25 -
1-01-002-26 -
Lignite
1-01-003-01 -
1-01-003-02 -
1-01-003-03 -
1-01-003-04 -
1-01-003-06 -
Residual Oil
1-01-004-01 -
1-01-004-04 -
1-01-004-05 -
1-01-004-06 -
Distillate Oil
1-01-005-01 -
1-01-005-04 -
1-01-005-05 -
Pulverized Coal: Wet Bottom
Pulverized Coal: Dry Bottom
Cyclone
Spreader Stoker
Traveling Grate (Overfeed) Stoker
Pulverized Coal: Dry Bottom
(Tangential Firing)
Atmospheric Fluidlzed Bed
Coal
Pulverized Coal: Wet Bottom
Pulverized Coal: Dry Bottom
Cyclone
Spreader Stoker
Traveling Grate (Overfeed) Stoker
Pulverized Coal: Dry Bottom
(Tangential Firing)
Pulverized Coal
Pulverized Coal: Tangential
Firing
Cyclone
Traveling Grate (Overfeed) Stoker
Spreader Stoker
Grade 6 Oil : Normal Firing
(Includes horizontally, opposed
and front wall firing)
Grade 6 Oil: Tangential Firing
Grade 5 Oil: Normal Firing
Grade 5 Oil: Tangential Firing
Grades 1 and 2 Oil
Grade 4 Oil: Normal Firing
Grade 4 Oil: Tangential Firing
7.0 A
10.0 A
2.0 A
60.0
16.0
10.0 A
7.0 A
10.0 A
2.0 A
60.0
16.0
10.0 A
6.3 A
6.3 A
6.7 A
2.9 A
6.8 A
*13.0 Sb
I.
*13.0 S
10.0
10.0
2.0
7.0
7.0
39
39
39
39
39
39
*14
35
35
35
35
35
35
30,
30.
30,
30.
30.
159.
159.
159.
159.
143.
*150
•150.
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
,0
,0
.0
3
3
3
3
6
0
0
S
S
S
S
S
S
S
S
S
S
S
S
S
S
S
S
S
S
S
S
S
S
sc
sc
34.0
21.0
37.0
14.0
7.5
15.0
*13.0
34.0
21.0
37.0
14.0
7.5
15.0
14.0
8.0
17.0
6.0
6.0
67.0
42.0
67.0
42.0
24.0
67.0
42.0
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.
,07
.07
.07
,07
,07
,07
.07
.07
.07
.07
,07
.07
,07
.07
,07
.07
07
07
76
76
76
76
2
76
76
0.
0
0
5,
6
0
0
0
0
5
6
0
0
0
0
6
5
5
5
5
5
5
5
5
.6
.6
.6
.0
.0
.6
.6
.6
.6
.0
.0
.6
.6
.6
.6
.0
.0
.0
.0
.0
.0
.0
.0
.0
Tons Burned
Tons Burned
Tons Burned
Tons Burned
Tons Burned
Tons Burned
Tons Burned 279
Tons Burned
Tons Burned
Tons Burned
Tons Burned
Tons Burned
Tons Burned
Tons Burned
Tons Burned
Tons Burned
Tons Burned
Tons Burned
3
10 Gallons Burned
3
10 Gallons Burned
10 Gallons Burned
10 Gallons Burned
3
10 Gallons Burned
10 Gallons Burned
10 Gallons Burned
*Refer to numbered notes in Appendix A or lettered notes in Appendix B: lactors without asterisks are from AP-'.Z.
-------
SCC Process
Natural Gas
1-01-006-01 - Boilers over 100 MMBtu/Hr except
tangentially fired units
1-01-006-02 - Boilers under 100 MMBtu/Hr except
tangentially fired units
1-01-006-04 - Tangentially Fired Boilers
c
Process Gas (Specify Gas in Comments)
1-01-007-01 - Boilers over 100 MMBtu/Hr
1-01-007-02 - Boilers under 100 MMBtu/Hr
Coke°
1-01-008-01 - All Boiler Sizes
Wood/Bark Waste
1-01-009-01 - Bark-Fired Boiler
1-01-009-02 - Uood/Bark-Flred Boiler
1-01-009-03 - Wood-Fired Boiler
Liquified Petroleum Gas (LPG)
1-01-010-01 - Butane
1-01-010-02 - Propane
GO
0 Bagasse
1-01-011-01 - All Boiler Sizes
Solid Waste
1-01-012-01 - Specify Waste Material in
Comments
Liquid Waste
1-01-013-01 - Specify Waste Material in
Comments
1-01-013-02 - Waste Oil
EXTERNAL COMBUSTION BOILERS - INDUSTRIAL*
Anthracite Coal
1-02-001-01 - Pulverized Coal
1-02-001-04 - Traveling Grate Stokers
1-02-001-07 - Hand-Fired
O Li. LUIllllOUS IjOi A.
1-02-002-01 - Pulverized Coal: Wet Bottom
1-02-002-02 - Pulverized Coal: Dry Bottom
PART
Lbs/Unit
3.0
3.0
3.0
3.0
3.0
10.0 A
47.0
7.2
8.0
0.28
0.26
16.0
19.0*
10.0 A
9.1
10.0
7.0 A
10.0 A
SO
Lbs/finit
0.6
0.6
0.6
950.0 S
950.0 S
39.0 S
0.15
0.15
0.15
*86.5 S°
£
*86.5 S
0.0
*160
39.0 S
39.0 S
39.0 S
39.0 S
39.0 S
NO
Lbs/Onit
550.0
140.0
275.0
550.0
140.0
21.0
2.8
2.8
2.8
13.2
12.4
1.2
*3.8
*67
18.0
10.0
3.0
34.0
21.0
VOC
Lbs/Unit
1.4
2.8
1.4
1.4
2.8
0.07
1.4
1.4
1.4
0.26
0.25
A
•2.0
*2.0
*1.0
*1.0
0.07
0.07
10.0
0.07
0.07
CO
Lbs/Unit Units Notes
40.0 10 Cubic Feet Burned
6
35.0 10 Cubic Feet Burned
6
40.0 10 Cubic Feet Burned
40.0 10 Cubic Feet Burned
35.0 10 Cubic Feet Burned
0 . 6 Tons Burned
4 . 0 Tons Burned
4 . 0 Tons Burned
4 . 0 Tons Burned
3
3.3 10 Gallons Burned
3.1 10 Gallons Burned
4
*2 . 0 Tons Burned
Tons Burned 137, 236
3
10 Gallons Burned 236
3
10 Gallons Burned 236
0.6 Tons Burned
0.6 Tons Burned
90.0 Tons Burned
0 . 6 Tons Burned
0.6 Tons Burned
*Refer to numbered notes in Appendix A or lettered notes in Appendix B; factors without asterisks are from AP-42.
-------
sec
Process
PART
Lbs/Unit
SO
Lbs/dnit
NO
Lbs/5nit
VOC
Lbs/Unit
CO
Lbs/Unit
Units Notes
Bituminous Coal (Continued)
1-02-002-03 -
1-02-002-04 -
1-02-002-05 -
1-02-002-06 -
1-02-002-12 -
1-02-002-13 -
1-02-002-17 -
1-02-002-19 -
Subbituminous
1-02-002-21 -
1-02-002-22 -
1-02-002-23 -
1-02-002-24 -
1-02-002-25 -
1-02-002-26 -
1-02-002-29 -
Lignite
1-02-003-01 -
1-02-003-02 -
1-02-003-03 -
1-02-003-04 -
1-02-003-06 -
1-02-003-07 -
Residual Oil
1-02-004-01 -
1-02-004-04 -
1-02-004-05 -
Distillate Oil
1-02-005-01 -
1-02-005-04 -
1-02-005-05 -
Natural Gas
1-02-006-01 -
1-02-006-02 -
1-02-006-03 -
1-02-006-04 -
Cyclone
Spreader Stoker
Overfeed Stoker
Underfeed Stoker
Pulverized Coal : Dry Bottom
(Tangential Firing)
Coal Slurry
Atmospheric Fluidized Bed
Cogeneration
Coal
Pulverized Coal: Wet Bottom
Pulverized Coal: Dry Bottom
Cyclone
Spreader Stoker
Traveling Grate (Overfeed) Stoker
Pulverized Coal : Dry Bottom
(Tangential Firing)
Cogeneration
Pulverized Coal
Pulverized Coal: Tangential
Firing
Cyclone
Traveling Grate (Overfeed) Stoker
Spreader Stoker
Cogene rat ion
Grade 6 Oil
Grade 5 Oil
Cogeneration
Grades 1 and 2 Oil
Grade 4 Oil
Cogeneration
Over 100 MMBtu/Hr
10-100 MMBtu/Hr
Less Than 10 MMBtu/Hr
Cogeneration
2.0 A
60.0
16.0
15.0
10.0 A
10.0 A
7.0 A
10.0 A
2.0 A
60.0
16.0
10.0 A
10.0 A
6.3 A
6.3 A
6.7 A
2.9 A
6.8 A
6.3 A
*12.0 Sb
10.0
*12.0 S
2.0
7.0
2.0
3.0
3.0
3.0
3.0
39.
39.
39.
31.
39.
*44.
*14.
39.
35.
35.
35.
35.
35.
35.
35.
30.
30.
30.
30.
30.
30.
158.
158.
158.
143.
•150.
143.
0.
0.
0.
0.
0
0
0
0
0
3
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
6
6
6
6
0
6
6
6
6
6
S
S
S
S
S
S
S
S
S
S
S
S
S
S
S
S
S
S
S
S
S
S
S
sc
S
37.0
14.0
7.5
9.5
15.0
*9.3
*13.0
15.0
34.0
21.0
37.0
14.0
7.5
15.0
15.0
14.0
8.0
17.0
6.0
6.0
8.0
55.0
55.0
55.0
20.0
20.0
20.0
550.0
140.0
100.0
275.0
0
0
0
1
0
• 0
*0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
1
2
5
1
.07
.07
.07
.3
.07
.4
.07
.07
.07
.07
.07
.07
.07
.07
.07
.07
.07
.07
.07
.07
.07
.28
.28
.28
.2
.2
.2
.4
.8
.3
.4
0
5
6
11
0
0.
0.
0.
0.
5,
6.
0.
0
0.
0.
0.
6.
5
0.
5.
5.
5.
5.
5.
5.
40.
35.
20.
40.
.6
.0
.0
.0
.6
.6
.6
.6
.6
.0
.0
.6
.6
6
.6
.6
.0
.0
.6
.0
0
0
.0
.0
0
0
0
0
0
Tons Burned
Tons Burned
Tons Burned
Tons Burned
Tons Burned
Tons Burned 337
Tons Burned 279
Tons Burned
Tons Burned
Tons Burned
Tons Burned
Tons Burned
Tons Burned
Tons Burned
Tons Burned
Tons Burned
Tons Burned
Tons Burned
Tons Burned
Tons Burned
Tons Burned
3
10 Gallons Burned
10 Gallons Burned
10 Gallons Burned
3
10 Gallons Burned
10 Gallons Burned
10 Gallons Burned
5
10 Cubic Feet Burned
10 Cubic Feet Burned
10 Cubic Feet Burned
10 Cubic Feet Burned
Refer to numbered notes in Appendix A or lettered notes in Appendix B; factors without asterisks are from AP-42.
-------
sec
Process Gas
1-02-007-01
1-02-007-04
1-02-007-07
1-02-007-10
1-02-007-99
Coke°
1-02-008-02
1-02-008-04
Process
- Petroleum Refinery Gas
- Blast Furnace Gas
- Coke Oven Gas
- Cogeneration
- Other: Specify in Comments
- All Boiler Sizes
- Cogeneration
PART
Lbs/Unit
3
•2
•6
7
7
.0
.9°
.2°
.0 A
.0 A
SO
Lbs/Unit
950.0 S
•950.0 S°
•680.0 S°
•950.0 S°
•950.0 S°
39.0 S
39.0 S
NO
Lbs/flnlt
140
•23
•80
14
14
.0
.0
.0
.0
.0
VOC
Lbs/Unit
2
•0
•1
•2
0
0
•8d
.2d
.8
.07
.07
CO
Lbs/Unit
35.0
•13.7
•18.4
0.6
0.6
Units
10 Cubic Feet Burned
10 Cubic Feet Burned
10 Cubic Feet Burned
10 Cubic Feet Burned
10 Cubic Feet Burned
Tons Burned
Tons Burned
Notes
373
Wood /Bark- Waste
1-02-009-01
1-02-009-02
1-02-009-03
1-02-009-04
OJ 1-02-009-05
ro
1-02-009-06
1-02-009-07
- Bark-Fired Boiler (Greater than
50,000 LB Steam)
- Wood/Bark-Fired Boiler (Greater
than 50,000 LB Steam)
- Wood-Fired Boiler (Greater than
50,000 LB Steam)
- Bark-Fired Boiler (Less than
50,000 LB Steam)
- Wood/Bark-Fired Boiler (Less
than 50,000 LB Steam)
- Wood-Fired Boiler (Less than
50,000 LB Steam)
- Wood Cogeneration
47
7
8
47
7
8
7
.0
.2
.8
.0
.2
.8
.2
Liquified Petroleum Gas (LPG)
1-02-010-01
1-02-010-02
Baggase
1-02-011-01
Solid Waste
1-02-012-01
Liauid Waste
1-02-013-01
, „„ „,„ „„
CO Boiler0
1-02-014-01
1-02-014-02
- Butane
- Propane
- All Boiler Sizes
- Specify Waste Material in
Comments
(See Malor Group 26. SCC 3-07-001-04
- Specify Waste Material in
Comments
u «. „ r\t 1
- Natural Gas
- Process Gas
0
0
16
.28
.26
.0
for Pulp Mill
19
3
3
ne
.0
.0
0.15
0.15
0.15
0.15
0.15
0.15
0.15
•86.5 S°
•86.5 S°
0.0
•1.6
2
2
2
0
0
0
2
13
12
1
•5
.8
.8
.8
.68
.68
.68
.8
.2
.4
.2
.9
1
1
1
1
1
1
1
0
0
•2
•2
.4
.4
.4
.4
.4
.4
.4
.26
.25
.od
.0
4.0
4.0
4.0
4.0
4.0
4.0
4.0
3.3
3.1
*2.0d
Recovery Boilers)
•28.0
•no.o
0.6
950.0 S
•23
•60
140
140
.0
.0
.0
.0
•1
•1
2
2
.0
.0
.8
.8
35.0
35.0
Tons Burned
Tons Burned
Tons Burned
Tons Burned
Tons Burned
Tons Burned
Tons Burned
3
10 Gallons Burned
10 Gallons Burned
Tons Burned
Tons Burned
10 Gallons Burned
3
10 Gallons Burned
10 Cubic Feet Burned
10 Cubic Feet Burned
342
343
343
*Refer to numbered notes in Appendix A or lettered notes in Appendix B; factors without asterisks are
from AP-42.
-------
CO
CO
SCC Process
CO Boiler (Continued)"
1-02-014-03 - Distillate Oil
1-02-014-04 - Residual Oil
EXTERNAL COMBUSTION BOILERS - COMMERCIAL/ INSTITUT
Anthracite Coal
1-03-001-01 - Pulverized Coal
1-03-001-02 - Traveling Crate Stokers
1-03-001-03 - Hand-Fired
Bituminous Coal
1-03-002-05 - Pulverized Coal: Net Bottom
1-03-002-06 - Pulverized Coal: Dry Bottom
1-03-002-07 - Overfeed Stoker
1-03-002-08 - Underfeed Stoker
1-03-002-09 - Spreader Stoker
1-03-002-14 - Hand-Fired
1-03-002-16 - Pulverized Coal: Dry Bottom
(Tangential Firing)
1-03-002-17 - Atmospheric Fluidized Bed
SubbltiifTilnous Co&l
1-03-002-21 - Pulverized Coal: Wet Bottom
1-03-002-22 - Pulverized Coal: Dry Bottom
1-03-002-23 - Cyclone
1-03-002-24 - Spreader Stoker
1-03-002-25 - Traveling Grate (Overfeed) Stoker
1-03-002-26 - Pulverized Coal: Dry Bottom
(Tangential Firing)
Lignite
1-03-003-05 - Pulverized Coal
1-03-003-06 - Pulverized Coal: Tangential
Firing
1-03-003-07 - Traveling Grate (Overfeed) Stoker
1-03-003-09 - Spreader Stoker
Residual 011°
1-03-004-01 - Grade 6 Oil
1-03-004-04 - Grade 5 Oil
Distillate Oil
1-03-005-01 - Grades 1 and 2 Oil
1-03-005-04 - Grade 4 Oil
PART
Lbs/Unit
2.0
12.0 S
10.0 A
9.1
10.0
7.0 A
10.0 A
16.0
15.0
60.0
15.0
10.0 A
7.0 A
10.0 A
2.0 A
60.0
16.0
10.0 A
6.3 A
6.3 A
2.9 A
6.8 A
•12.0 Sb
*10.0
2.0
7.0
SO
Lbs/finit
144.0 S
159.0 S
39.0 S
39.0 S
39.0 S
39.0 S
39.0 S
39.0 S
31.0 S
39.0 S
31.0 S
39.0 S
*14.0
35.0 S
35.0 S
35.0 S
35.0 S
35.0 S
35.0 S
30.0 S
30.0 S
30.0 S
30.0 S
158.6 S
158.6 S
143.6 S
*150.0 S°
NO
Lbs/finit
20.0
55.0
18.0
10.0
3.0
34.0
21.0
7.5
9.5
14.0
3.0
15.0
*13.0
34.0
21.0
37.0
14.0
7.5
15.0
14.0
8.0
6.0
6.0
55.0
55.0
20.0
20.0
VOC
Lbs/Unit
0.2
0.28
0.07
0.07
10.0
0.07
0.07
0.07
1.3
0.07
10.0
0.07
•0.07
0.07
0.07
0.07
0.07
0.07
0.07
0.07
0.07
0.07
0.07
1.13
1.13
0.34
0.34
CO
Lbs/Unit
5.0
5.0
0.6
0.6
90.0
0.6
0.6
6.0
11.0
5.0
90.0
0.6
0.6
0.6
0.6
5.0
6.0
0.6
0.6
0.6
6.0
5.0
5.0
5.0
5.0
5.0
Units Notes
10 Gallons Burned
10 Gallons Burned
Tons Burned
Tons Burned
Tons Burned
Tons Burned
Tons Burned
Tons Burned
Tons Burned
Tons Burned
Tons Burned
Tons Burned
Tons Burned 139, 366
Tons Burned
Tons Burned
Tons Burned
Tons Burned
Tons Burned
Tons Burned
Tons Burned
Tons Burned
Tons Burned
Tons Burned
3
10 Gallons Burned
10 Gallons Burned
3
10 Gallons Burned
10 Gallons Burned
Refer to numbered notes In Appendix A or lettered notes in Appendix B; factors without asterisks are from AP-42.
-------
sec
Natural Gas
1-03-006-01
1-03-006-02
1-03-006-03
Process Gas
1-03-007-01
1-03-007-99
Process
- Over 100 MMBtu/Hr
- 10-100 MHBtu/Hr
- Less Than 10 MMBtu/Hr
- Sewage Gas
- Other Not Classified
PART
Lbs/Unlt
3
3.
3.
.0
.0
.0
SO
Lbs/unlt
0,
0.
0.
*4.
.6
.6
6
,5
NO
Lbs/unit
550.0
140.0
100.0
voc
Lbs/Unit
1.
2
5,
*3
.4
.8
.3
.0
CO
Lbs/Unlt
40.
35
20.
.0
.0
.0
Units Notes
6
10 Cubic Feet Burned
10 Cubic Feet Burned
10 Cubic Feet Burned
£
10" Cubic Feet Burned 140
10 Cubic Feet Burned
Wood/Bark Waste
1-03-009-01
1-03-009-02
1-03-009-03
Ll.au Id Petr
1-03-010-01
1-03-010-02
- Bark-Fired Boiler
- Wood/Bark-Fired Boiler
- Wood-Fired Boiler
oleum Gas (LPG)
- Butane
- Propane
47.
7.
8.
0.
0.
,0
2
8
28
.26
0.
0.
0.
*86
*86.
,15
15
.15
5 SC
5 SC
0.68
0.68
0.68
9.4
8.8
1
1.
1
0
0
.4
.4
.4
.5
.47
4
4
4
1
1.
.0
.0
.0
.9
.8
Tons Burned
Tons Burned
Tons Burned
3
10 Gallons Burned
10 Gallons Burned
00
-c*
Solid Haste
1-03-012-01 - Specify Waste Material in
Comments
Liquid Waste
1-03-013-01 - Specify Waste Material in
Comments
*1.6
*5.9
*2.0
*1.0
Tons Burned
10 Gallons Burned
*Refer to numbered notes in Appendix A or lettered notes in Appendix Bi factors without asterisks are from AP-42.
236
236
1-03-013-02 - Waste Oil
1-03-013-03 - Sewage Grease Skimmings
EXTERNAL COMBUSTION - SPACE HEATERS
Industrial Space Heaters
1-05-001-05 - Distillate Oil
1-05-001-06 - Natural Gas
1-05-001-10 - Liquified Petroleum Gas (LPG)
Commercial Space Beaters
1-05-002-05 - Distillate 011°
1-05-002-06 - Natural Gas°
1-05-002-09 - Hood c
i-05-OGz-iu - Liquified Petroleum Gas (L?G)
INTERNAL COMBUSTION ENGINES - ELECTRIC GENERATION -
Distillate Oil (Diesel)
2-01-001-01 - Turbine
2-01-001-02 - Reciprocating
19.0*
2.50
3.00
1.85
2.50
3.00
25.00
1.B5
4911
5.0
33.5
*160
144.0 S
0.6
86.5 S
144.0 S
0.6
0.5
86.5 S
140.0 S
31.2
*55
18.0
100.0
7.5
18.0
100.0
1.0
7.5
67.8
469.0
*1.0
0.7
5.3
0.5
0.7
5.3
1.7
0.5
4.77
32.1
5.00
20.00
1.95
5.00
20.00
150.00
1.95
15.4
102.0
10 Gallons Burned 236
10 Gallons Burned
3
10 Gallons Burned
10 Cubic Feet Burned
10 Gallons Burned
10 Gallons Burned
10 Cubic Feet Burned
Tons Burned
10 Gallons Burned
10 Gallons Burned
10 Gallons Burned
-------
CO
en
SCC Process
Natural Gas
2-01-002-01 - Turbine
2-01-002-02 - Reciprocating
Process Gas
2-01-007-02 - Reciprocating
Kerosene /Naohtha (Jet Fuel)C
2-01-009-01 - Turbine
2-01-009-02 - Reciprocating
Geysers /Geothennal
2-01-010-01 - Steam Engine
INTERNAL COMBUSTION - INDUSTRIAL
Distillate Oil (Diesel)
2-02-001-01 - Turbine
2-02-001-02 - Reciprocating
2-02-001-03 - Turbine: Cogeneration
2-02-001-04 - Engine: Cogeneration
Natural Gas
2-02-002-01 - Turbine
2-02-002-02 - Reciprocating
2-02-002-03 - Turbine: Cogeneration
2-02-002-04 - Engine: Cogeneration
Gasoline
2-02-003-01 - Reciprocating
Large Bore Ermine
2-02-004-01 - Diesel
2-02-004-02 - Dual Fuel (Oil/Gas)
2-02-004-03 - Dual Fuel (Cogeneration)
Res idual /Crude 011°
2-02-005-01 - Reciprocating
Kerosene /Naphtha (Jet Fuel)"
2-02-009-01 - Turbine
2-02-009-02 - Reciprocating
Liquified Petroleum Gas (LPG)d
2-02-010-01 - Propane: Reciprocating
2-02-010-02 - Butane: Reciprocating
PART
Lbs/Unlt
14.0
MO.O
5.0
33.5
5.0
33.5
5.0
33.5
14.0
*io. od
14.0
•10.0
6.47
50.0
•2.2
*0.035
33.5
5.0
33.5
*5.0
*5.0
SO
Lbs/Unlt
•0.6°
0.6
6.2
6.2
140.0 S
31.2
140.0 S
31.2
0.6
0.6
0.6
0.6
5.31
*150.0 SC
0.7
155.0 S
6.2
6.2
*0.35
*0.35
NO
Lbs/Unlt
413.0
3400.0
67.8
469.0
67.8
469.0
67.8
469.0
300.0
3400.0
413.0
3400.0
102.0
500.0
18.0
*31.7
469.0
67.8
469.0
•139.0
*139.0
VOC
Lbs/Unit
12.6
82.9
*83
4.77
32.1
*HEG
4.77
32.1
4.77
32.1
6.9
82.9
12.6
82.9
*147.7°
13.0
1.5
M..32
32.1
4.77
32.1
•83.0
*83.0
CO
Lbs/Unlt
115.0
430.0
15.4
102.0
15.4
102.0
15.4
102.0
120.0
430.0
115.0
430.0
3,940.0
130.0
5.9
*1.05
102.0
15.4
102.0
*129.0
*129.0
Units Notes
$
10 Cubic Feet Burned
10 Cubic Feet Burned
6
10 Cubic Feet Burned 373
10 Gallons Burned
3
10 Gallons Burned
Tons Steam Produced 285
10 Gallons Burned
10 Gallons Burned
10. Gallons Burned
3
10 Gallons Burned
6
10 Cubic Feet Burned
10 Cubic Feet Burned
10 Cubic Feet Burned
10 Cubic Feet Burned
10 Gallons Burned
10 Gallons Burned
10 Horsepower-Hours
10 Brake HP-Hours
3
10 Gallons Burned
3
10. Gallons Burned
3
10 Gallons Burned
10 Gallons Burned
10 Gallons Burned
Refer to numbered notes in Appendix A or lettered notes in Appendix B; factors without asterisks are from AP-42.
-------
en
SCC Process
INTERNAL COMBUSTION - COMMERCIAL/ INSTITUTIONAL
Distillate Oil (Diesel)
2-03-001-01 - Reciprocating
2-03-001-02 - Turbine
Natural Gas
2-03-002-01 - Reciprocating
2-03-002-02 - Turbine
Gasoline
2-03-003-01 - Reciprocating
Liquified Petroleum Gas (LPG)
2-03-010-01 - Propane: Reciprocating
2-03-010-02 - Butane: Reciprocating
INTERNAL COMBUSTION - ENGINE TESTING
Aircraft
2-04-001-01 - Turbojet
2-04-001-02 - Turboshaft
Turbine
2-04-003-01 - Natural Gas
2-04-003-02 - Diesel /Kerosene
Reciprocating
2-04-004-01 - Gasoline
2-04-004-02 - Diesel /Kerosene
PART
Lbs/Unit
33.5
5.0
•10. Od
14.0
6.47
*5.0
*5.0
11.8
11.8
14.0
5.0
6.47
33.5
SO
Lbs/9nlt
31.2
140.0 S
0.6
0.6
5.31
•0.35
*0.35
13.0
13.0
0.6
6.2
5.31
31.2
NO
Lbs/finlt
469.0
67.8
3400.0
413.0
102.0
*139.0
*139.0
14.6
14.6
300.0
67.8
102.0
469.0
VOC
Lbs/Unit
32.1
4.77
82.9
12.6
147.7
*83.0
*83.0
46.0
46.0
6.9
4.77
148.0
32.1
CO
Lbs/Unit
102.0
15.4
430.0
115.0
3,940.0
•129.0
•129.0
32.7
32.7
120.0
15.4
3,940.0
102.0
Units Notes
10 Gallons Burned
10 Gallons Burned
6
10 Cubic Feet Burned
10 Cubic Feet Burned
10 Gallons Burned
10 Gallons Burned
10 Gallons Burned
10 Gallons Fuel
10 Gallons Fuel
10 Cubic Feet Burned
10 Gallons Burned
3
10 Gallons Burned
10 Gallons Burned
INTERNAL COMBUSTION - FUGITIVE EMISSIONS
Other Not Classified
2-88-888-01 - Specify in Comments
2-88-888-02 - Specify in Comments
2-88-888-03 - Specify in Comments
10 Gallons Burned
10 Cubic Feet Burned
10 Horsepower-Hours
CHEMICAL MANUFACTURING - MAJOR GROUP 28
3-01-001-01
3-01-001-02
3-01-001-03
3-01-001-04
- General
- Raw Material
- Cyclohexane
- Nitric Acid
Storage
Ox idat Ion
Reaction
0
0
0.
0.
.9
.0
0
0
0.0
0.0
0.0
0.0
53
0
0
53,
.6
.0
.0
.0
42.7
2.2
40.0
0.0
115.0
0.0
115.0
0.0
Tons
Tons
Tons
Tons
of Product
of Product
of Product
of Product
*Refer to numbered notes In Appendix A or lettered notes in Appendix B: factors without asterisks are from AP-42.
-------
sec
Adlplc Acid -
3-01-001-05 -
3-01-001-06 -
3-01-001-07 -
3-01-001-08 -
3-01-001-09 -
3-01-001-80 -
Process
2869 (Continued)
Adiplc Acid Refining
Adlpic Acid Dry Ing /Load ing and
Storage
Absorber
Dryer
Cooler
Fugitive Emissions: General!
PART
Lbs/Unit
0
0
.1
.8
so
Lbs/5nlt
0.0
0.0
NO VOC
Lbs/Unit Lbs/Unit
0.6
0.0
*9.5
0.5
0.0
*0.4
*NEG
•NEC
*62,000
CO
Lbs/Unit
0
0
.0
.0
Tons
Tons
Tons
Tons
Tons
Units
of Product
of Product
of Product
of Product
of Product
Process Unit-Year
Notes
103
103
103
1, 2
Ammonia Production - 2873
3-01-003-05 -
3-01-003-06 -
3-01-003-07 -
3-01-003-08 -
3-01-003-09 -
Carbon Black
3-01-005-01 -
3-01-005-02 -
3-01-005-03 -
3-01-005-04 -
3-01-005-06 -
3-01-005-07 -
3-01-005-08 -
3-01-005-09 -
Feedstock Desulfurication
Primary Reformer: Natural Gas
Fired
Primary Reformer: Oil Fired
Carbon Dioxide Regenerator
Condensate Stripper
Production - 2895
Channel Process
Thermal Process
Gas Furnace Process (Main
Process Vent)
Oil Furnace Process (Main
Process Vent)
Transport Air Vent
Pellet Dryer
Bagging /Loading
Furnace Process Fugitive
Emissions
0
0
0
0
2,300
0
3.
6.
0.
0.
0.
0.
.144
.9
.0
.0
.0
.0
.2
.53
.58
.45
.06
2
•
0.019
0.0048
2.6
0.0
0.0
0.0
0.0
0.0
0.0
0.0
0.1
0.0
0.0
5.4
5.4
0.0
0.0
0.0
0.0
0.0
0.56
0.0
0.73
0.0
0.0
7.2
0.012
0.38
1.04
1.2
8,943.0
0.0
1,400.0
100.0
0.0
*0.3
0.0
0.0
13
0
0
2
33,500
0
5,300
2,800
0
0
0
.8
.136
.24
.0
.0
.0
.0
.0
.0
.0
.0
Tons
Tons
Tons
Tons
Tons
Tons
Tons
Tons
Tons
Tons
Tons
Tons
Tons
Produced
Produced
Produced
Produced
Produced
Produced
Produced
Produced
Produced
Produced
Produced
Produced
Produced
298
166
Charcoal Manufacture - 2861
3-01-006-01 -
3-01-006-03 -
3-01-006-04 -
3-01-006-05 -
3-01-006-99 -
Chloro-Alkali
General
Batch Kiln
Continuous Furnace
Briquet ting
Other Not Classified (Specify
in Comments)
Production - 2812
266.
266.
266.
56.
0
0
0
0
0.0
24.0
24.0
24.0
0.0
314.0
314.0
314.0
0.0
344.
344
344.
0
.0
.0
.0
.0
Tons
Tons
Tons
Tons
Tons
Produced
Produced
Produced
Produced
Product
3-01-008-01 - Liquefaction (Diaphragm Ceil
Process)
3-01-008-02 - Liquefaction (Mercury Cell
Process)
0.0
0.0
*0.0
*0.0
100 Tons Chlorine Liquified 166
100 Tons Chlorine Liquified 166
*Note that fugitive emissions are reported In units of Ibs/process unit-year rather than Ibs/ton product as In the NEDS Source Classification Codes
and Emission Factor Listing dated October 1985.
Refer to numbered notes In Appendix A or lettered notes In Appendix B; factors without asterisks are from AP-42.
-------
PART
SCC Process Lbs/Unit
Chloro-Alkali Production - 2812 (Continued)
3-01-008-03 - Chlorine Loading: Tank Car Vents 0.0
3-01-008-04 - Chlorine Loading: Storage Tank 0.0
Vents
3-01-008-05 - Air Blowing of Mercury Cell Brine 0.0
Cleaning Chemicals - 2841. 2842
3-01-009-01 - Spray Drying: Soaps and 90.0
Detergents
3-01-009-02 - Speciality Cleaners
3-01-009-99 - Other Mot Classified (Specify
in Comments)
ExDloslves - Trinitrotoluene - 2892
3-01-010-11 - Batch Process: Nitration Reactors
Fume Recovery
3-01-010-12 - Batch Process: Nitration Reactors
Acid Recovery
3-01-010-13 - Batch Process: Nitric Acid
Concentrators
3-01-010-14 - Batch Process: Sulfurle Acid
Concentrators - Electrostatic
Precipltators (Exit)
3-01-010-15 - Batch Process: Red Hater 25.0
Incinerator
3-01-010-21 - Continuous Process: Nitration
Reactors - (Fume Recovery)
3-01-010-22 - Continuous Process: Nitration
Reactors - (Acid Recovery)
3-01-010-23 - Continuous Process: Red Hater 0.25
Incinerator
3-01-010-30 - Open Burning: Haste 180.0
Hydrochloric Acid - 2819
3-01-011-01 - By-Product Process
3-01-011-98 - Handling and Storage (99.91
Removal)
Hydrofluoric Acid - 2819
3-01-012-02 - Rotary Kiln (Acid Reactor) 0.0
3-01-012-03 - Fluorspar Grinding/Drying 75.0
3-01-012-04 - Fluorspar Handling Silos 60.0
3-01-012-05 - Fluorspar Transfer 6.0
3-01-012-06 - Tail Cas Vent
SO NO
Lbs/unit Lbs/unit
0.0 0.0
0.0 0.0
0.0 0.0
25.0
55.0
37.0
14.0 40.0
2.0 26.0
8.0
3.0
0.24 7.0
150.0
0.0 *0.0
•2.7 *0.07
*0.0 *0.15
0.0 0.0
0.0 0.0
45.0
VOC
Lbs/Unit
0.0
0.0
0.0
*0.06
*1500
•NEC
*HEG
*HEG
•MEG
•1.1
•NEC
•NEC
•1.1
1.1
•0.0
•0.02
•0.0
0.0
0.0
CO
Lbs/Unit Units
0.0 100 Tons Chlorine
0.0 100 Tons Chlorine
0.0 100 Tons Chlorine
Tons Produced
Tons Product
Tons Produced
Tons Produced
Tons Produced
Tons Produced
Tons Produced
Tons Produced
Tons Produced
Tons Produced
Tons Produced
56.0 Tons TNT Burned
Tons Final Acid
10 Gallons Acid
Tons Acid Produced
Tons Fluorspar
0.0 Tons Fluorspar
0.0 Tons Fluorspar
Tons Acid Produced
Notes
Liquified
Liquified
Liquified
3
3
231
231
231
231
231
231
231
231
167
201, 107
209, 317. 368
Refer to numbered notes in Appendix A or lettered notes in Appendix Bi factors vlthout asterisks are from AP-42.
-------
CO
10
PART
SCC Process Lbs/Unit
Nitric Acid - 2873
3-01-013-01 - Absorber T«U Gas (Pre-1970
Facilities)
3-01-013-02 - Absorber Tall CM (Poit-1970
Facilities)
3-01-013-03 - Nitric Acid Concentration
(Pre-1970 Facilities)
3-01-013-04 - Nitric Acid Concentration
(Po*t-1970 Paellltle*)
Paint Manufacture - 2851 *
3-01-014-01 - General Mixing and Handling *5.5
3-01-014-02 - Pigment Handling 20.0
3-01-014-99 - Other Hot Classified (Specify
In Comments)
Varnish Manufacture - 2851
3-01-015-01 - Bodying Oil
3-01-015-02 - Oleoreslnous
3-01-015-03 - Alkyd
3-01-015-05 - Acrylic
3-01-015-99 - Other Not Classified (Specify
In Comments)
Phosohorlc Acid: Wet Process - 2874
3-01-016-01 - Reactor 0.0
3-01-016-02 - Gypsum Pond 0.0
3-01-016-03 - Condenser 0.0
Phosphoric Acid * Thcmwi Process — 2874
3-01-017-02 - Absorber: General
3-01-017-03 - Absorber with Packed Tower 2.14
3-01-017-04 - Absorber with Venturl Scrubber 2.53
3-01-017-05 - Absorber with Glass Mist 0.69
Eliminator
3-01-017-06 - Absorber with Wire Mist Eliminator 5.46
3-01-017-07 - Absorber with High-pressure Mist 0.11
Eliminator
3-01-017-08 - Absorber with Electrostatic 1.66
Preclpltator
Plastics Production - Specific Products - 2821
3-01-018-01 - Polyvlnyl Chlorides and Copolymers 35.0
3-01-018-02 - Polypropylene and Copolymers 3.0
3-01-018-03 - Ethylene-Propylene Copolymera
SO
Lbs/Bnlt
*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
*0.025
NO
Lbs/9nlt
43.0
1.8
10.0
10.0
0.0
0.0
*NEG
*HEC
*NEC
*HEG
*0.0
•NEC
•NEC
•NEC
*NEG
•NEC
*HEG
*NEG
*200
*131
voc
Lbs/Unlt
*0.0
•0.0
•0.0
*0.0
30.0
0.0
40.0
150.0
160.0
20.0
*0.0
*NEG
•NEC
*NEG
*HEG
*NEC
*NEG
*HEG
*HEG
•NEC
17.0
0.7
CO
Lbs/Unlt Units
Tons Pure Acid Produced
Tons Pure Acid Produced
Tons Pure Acid Produced
Tons Pure Acid Produced
0.0 Tons Paint Produced
0.0 Tons Pigment Processed
Tons Product
Tons Produced
Tons Produced
Tons Produced
Tons Produced
Tons Produced
Tons Phosphate Rock
Tons Phosphate Rock
Tons Phosphate Rock
Tons Phosphorous Burned
Tons P,O Produced
Tons P,O, Produced
Tons P_O Produced
2 5
Tons P.O. Produced
2 5
Tons P,0 Produced
Tons P.O Produced
Tons Product
Tons Product
Tons Product
Notes
4, 317
4, 317
4, 317
4, 317
316
316
316
316
72, 167
72
72
72, 161
72, 161
72, 161
72, 161
72, 161
72, 161
72, 161
149, 203
1*1
Refer to numbered notes In Appendix A or lettered notes In Appendix B; factors without asterisks are from AP-42.
-------
sec
PART
Process Lbs/Unlt
SO
Lbs/flnlt
NO
Lbs/Onlt
voc
Lbs/Unit
CO
Lbs/Unit
Units
Plastics Production - Specific Products - 2821 (Continued)
3-01-018-05 -
3-01-018-07 -
3-01-018-08 -
3-01-018-09 -
3-01-018-10 -
3-01-018-11 -
3-01-018-12 -
3-01-018-13 -
3-01-018-14 -
3-01-018-15 -
3-01-018-16 -
3-01-018-17 -
3-01-018-18 -
3-01-018-19 -
3-01-018-20 -
3-01-018-21 -
3-01-018-22 -
3-01-018-27 -
3-01-018-32 -
0 . 3-01-018-37 -
3-01-018-38 -
3-01-018-39 -
3-01-018-40 -
3-01-018-42 -
3-01-018-47 -
3-01-018-49 -
3-01-018-52 -
Polyethylene
3-01-018-60 -
3-01-018-61 -
3-01-018-63 -
3-01-018-64 -
3-01-018-65 -
3-01-018-66 -
Phenolic Resins
Polyethylene (High Density)
Monomer and Solvent Recovery
Extruder
Conveying
Storage
Polyethylene (Low Density)
Recovery and Purification System
Extruder
Pellet Silo
Transfer /Handling/ Loading /Packing
Polystyrene
Reactor
Solvent Recovery
Polymer Drying
Extruding /Pellet izing/ Convey ing/
Storage
Acrylic Resins
Polyamide Resins
Urea-Formaldehyde Resins
Polyester Resins: General
Polyester/ Alkyd Resins: Reactor
Kettle
Polyester /Alkyd Resins: Resin 0.0
Thinning Tank
Polyester /Alkyd Resins: Resin 0.0
Storage Tank
Melamine Resins
Epoxy Resins
Acrylonitrlle-Butadiene-Styrene
(ABS) Resin
Polyfluorocarbons
- 2821J
Recovery System
Purification System
Extruder
Pellet Silo/Storage
Transfer /Convey ing
Packing/Shipping
*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
*14.
*36
*25.
*11.
*0,
*0.
*7,
*60.
*60,
6
,4
,0
46
.01
.7
,0
.0
*NEG
*0.
*11.
,0
.1
*NEG
*0,
*0,
0.
0
0.
.0
.0
.0
.0
.0
*0.
*0,
*1.
0,
0,
0.
.0
.0
.0
.0
.0
.0
•1.
.6
*NEG
*NEG
*1
*1.
*20
*0
*4
*6
*11.
.2
.6
.0
.5
.8
.7
.1
Tons
Tons
Tons
Tons
Tons
Tons
Tons
Tons
Tons
Tons
Tons
Tons
Tons
Tons
Tons
Tons
Tons
Tons
Tons
Tons
0 . 0 Tons
0 . 0 Tons
Product
Product
Product
Product
Product
Product
Product
Product
Product
Product
Product
Product
Product
Product
Product
Product
Product
Product
Product
Product
Resin Produced
Thinning Solvent Used
0.0 103 Gallons Thinned Resin
Stored
0
0
0
0.
.0
0
.0
.0
0
0
0
0
.0
.0
.0
.0
Polyether Resins - 2821J
3-01-018-70 -
3-01-018-71 -
3-01-018-72 -
Reactor
Blowing Agent - Freon
Miscellaneous
*50
*6
*60
.0
.8
• 40
*30
*30
*HEG
*0.0
*0.0
•50
*HEG
Tons
Tons
Tons
Tons
Tons
Tons
Tons
Tons
Tons
Tons
Tons
Tons
Tons
Product
Product
Produced
Product
Product
Product
Product
Product
Product
Product
Product
Product
Product
Notes
85
50
178,
5,
178,
178,
85
5,
5,
5,
5,
87
5
179,
5
5,
87
85,
3
87
88
88
88
5
7
5
50
50
50,
50,
310,
310,
5
339
316
316
316
316
316
316
316
316
316
316
141
316
316
316
316
*Refer to numbered notes in Appendix A or lettered notes in Appendix B; factors without asterisks are from AP 42.
-------
SCC Process
Polyur« thane - 2821^
3-01-018-80 - Reactor
3-01-018-81 - Blowing Agent - Freon
3-01-018-82 - Blowing Agent - Methylene Chloride
3-01-018-83 - Transfer/Conveying/Storage
3-01-018-84 - Packaging /Shipping
3-01-018-85 - Other Not Classified (Specify
in Cement j)
Plastics Production - General Processes - 2821
3-01-018-90 - Catalyst Preparation
3-01-018-91 - Reactor Vents
3-01-018-92 - Separation Processes
3-01-018-93 - Raw Material Storage
3-01-018-94 - Solvent Storage
3-01-018-99 - Other Not Classified (Specify
in Comments)
Phthallc Anhydride - 2865
3-01-019-01 - o-Xylene Oxidation: Main Process
Stream (Reactor Condensers)
3-01-019-02 - o-Xylene Oxidation:
Pre-treatJDent
3-01-019-0* - o-Xylene Oxidation: Distillation
3-01-019-05 - Naphthalene Oxidation: Main
Process Stream (Reactor/
Condensers )
3-01-019-06 - Naphthalene Oxidation:
Pre-treatmant
3-01-019-07 - Naphthalene Oxidation:
Distillation
Printing Ink Manufacture - 2893
3-01-020-01 - Vehicle Cooking: General
3-01-020-02 - Vehicle Cooking: Oils
3-01-020-03 - Vehicle Cooking: Oleoresin
3-01-020-04 - Vehicle Cooking: Alkyds
3-01-020-05 - Pigment Mixing
Sodium Carbonate - 2812
3-01-021-01 - Solvay Process: NH Recovery
3-01-021-02 - Solvay: Handling
3-01-021-03 - Trona Crushing/Screening
3-01-021-04 - Calciner: Gas-Fired
3-01-021-05 - Calciner: Coal-Fired
PART
Lbs/Unit
138.0
13.0
89.0
56.0
5.0
38.0
0.0
0.0
0.0
0.0
2.0
0.0
50.0
368.0
390.0
SO NO VOC
Lbs/finit Lbs/Unit Lbs/Unit
•52
*NEG
*NEG
*0.0 *0.0 *0.0
*0 . 0 *0 . 0 *0 . 0
•0.47
•0.4
*2.0
*0.0 *0.0 *0.034
•o.o *o.o *o.oia
9.4 0.0 0.0
0.0 0.0 0.0
0.0 0.0 2.4
0.0 0.0 0.0
0.0 0.0 0.0
0.0 0.0 10.0
120.0
40.0
150.0
160.0
•6.2
*0.0
•0.0
*0.0 *0.0 *0.0
*0.0 *0.2
*0.01 *2.45 *0.07
CO
Lbs/Unlt Units
Tons Product
Tons Agent Used
Tons Agent Used
Tons Product
Tons Product
Tons Product
Tons Product
Tons Product
Tons Product
Tons Raw Material
Tons Solvent
Tons Product
301.0 Tons Produced
0.0 Tons Produced
0.0 Tons Produced
100.0 Tons Produced
0.0 Tons Produced
0.0 Tons Produced
Tons Produced
Tons Produced
Tons Produced
Tons Produced
Tons Pigment
Tons Produced
Tons Produced
Tons Ore Processed
Tons Ore Processed
Tons Ore Processed
Notes
5
339
339
310, 316
310, 316
86
88
143
86, 316
88, 316
3
8
8
8, 80
8, 80
8, 80
Refer to numbered notes in Appendix A or lettered notes in Appendix B; factors without asterisks are from AP-42.
-------
sec
3-01-021-06
3-01-021-07
3-01-021-08
3-01-021-12
3-01-021-13
3-01-021-99
_
-
-
-
.
-
Sulfuric Acid
3-01-022-01
-
Sulfuric Acid
3-01-023-01
3-01-023-04
3-01-023-06
3-01-023-08
3-01-023-10
3-01-023-12
3-01-023-14
3-01-023-16
3-01-023-18
3-01-023-19
3-01-023-20
3-01-023-21
3-01-023-22
_
_
_
_
_
-
_
-
_
-
-
PART
Process Lbs/Unit
ite - 2812 (Continued)
Rotary Dryer: Gas-Fired 67.0
Fluid Bed Dryer: Indirect Seated 146.0
Dlssolver
Rotary Predryer 3 . 1
Bleacher: Gas-Fired 311.0
Other Mot Classified (Specify
in Comments)
Chamber Process - 2819
General
- Contact Process - 2819 ^
Absorber/8 99. 9X Conversion *2.5k
Absorber/* 99. SX Conversion *2'\
Absorber /« 99. OX Conversion *2-5k
Absorber /« 98. OX Conversion *2>Sk
Absorber It 97. OX Conversion *2'\
Absorber /0 96. OX Conversion *2'*k
Absorber/C 95. OX Conversion *2.5fc
Absorber/ « 94. OX Conversion *2-5k
Absorber/8 93. OX Conversion *2.5
Concentrator
Tank Car and Truck Unloading
Storage Tank Vents
Leaks in Process Equipment
SO
Lbs/flnit
•0
*0
*0
4,
7
14
27
40
55
70
82
96
*0.
*0
.0
.0
.0
.0
.0
.0
.0
.0
.0
,0
.0
.0
.1
,1
NO
Lbs/ftnlt
*0.
*0.
*0.
*0.
*0.
•0.
*0.
*0.
*0.
*0.
*0.
0
0
004
004
004
004
004
004
004
004
004
Synthetic Orcanlc Fiber Production - Soeciflc Products - 2824
3-01-024-01
3-01-024-02
3-01-024-05
3-01-024-10
3-01-024-14
3-01-024-15
3-01-024-16
_
-
-
Polyamlde (e.g.. Nylon)
Polyesters (e.g., Dacron)
Polyf luorocarbons (e.g., Teflon)
Acrylics (e.g., Orion)
Polyoleflns (e.g.. Polypropylene)
Vinyls (e.g., Saran)
Aranld
*NEC
*NEG
Synthetic Organic Fiber Production - General Processes - 2824
3-01-024-21
3-01-024-22
3-01-024-23
3-01-024-24
3-01-024-25
3-01-024-26
3-01-024-27
-
Dope Preparation
Filtration
Fiber Extrusion
Washing/Dry Ing/Flnlshing
Fiber Storage
Equipment Cleanup
Solvent Storage
"0,
*0.
*0.
,0
0
,0
*0.
*0.
*0.
*0.
-u.
*0.
*0.
0
0
0
0
0
0
0
voc
Lbs/Unit
*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
7.0
*90
*90
*73.0
*7
10
*6.0
10
•96
*SEG
*NEG
*34
CO
Lbs/Unit
Tons
Tons
Tons
Tons
Tons
Tons
Tons
Tons
Tons
Tons
Tons
Tons
Tons
Tons
Tons
Tons
Tons
Tons
Tons
Tons
Tons
Tons
Tons
Tons
Tons
•»__._
ions
Tons
Tons
Tons
Tons
Tons
Tons
Tons
Tons
Units
Product
Product
Product
Dry NaHCO Feed
Dry Feed
Produced
of Pure Acid Produced
100X H SO
100X H^SO
100X HjS04
100X H SO
100X H-SO
100X H SO
ioox irso*
100X KSO
IOOX H,SO4
IOOX H SO
IOOX 8 SO Loaded
IOOX H^SO Stored
IOOX B SO^
Fiber
Fiber
Product
Product
Product
Product
Product
Product
Product
Product
Product
Product
Product
Solvent
Notes
8
8
8
9,
9,
9,
9,
9,
9,
9,
9,
9,
9,
9,
110
111
110
112
110
110
113
, 80
, 80
, 80
8
8
204
204
204
204
204
204
204
204
204
9
146
122
9
316
75
110
10
75
, 316
, 316
. 316
, 316
, 316
, 316
, 316
*Refer to numbered notes in Appendix A or lettered notes in Appendix B: factors without asterisks are from AP-42.
-------
u>
sec
Process
Cellulosic Fiber Production - 2823
3-01-025-01 - Viscose (e.g., Rayon)
3-01-025-05 - Acetate
Synthetic Rubber Production (Manufacturing Only)
3-01-026-01
3-01-026-02
3-01-026-08
3-01-026-09
3-01-026-10
3-01-026-11
3-01-026-12
3-01-026-13
3-01-026-14
3-01-026-15
3-01-026-16
3-01-026-17
3-01-026-25
3-01-026-30
3-01-026-99
- General
- Butyl (Isobutylene)
- Acrylonitrlle
- Dryers
- Slowdown Tank
- Steam Stripper
- Prestorage Tank
- Monomer Recovery (Absorber Vent)
- Blending Tanks
- Isoprene
- Latex: Monomer Removal
- Latex: Blending Tank
- Chloroprene
- Sillcone Rubber
- Other Not Classified (Specify
in Comments)
PART SO
Lbs/Unit Lbs/unit
- 2822
NO VOC CO
Lbs/Unit Lbs/Unit Lbs/Unit
0.
*290
83.
*20.
5.
0
0
0
0
*NEG
*NEG
*NEG
0.
0.
17.
0.
52
84
0
2
Tons
Tons
Tons
Tons
Tons
Tons
Tons
Tons
Tons
Tons
Tons
Tons
Tons
Tons
Tons
Tons
Tons
Ammonium Nitrate Production - 2873
3-01-027-04
3-01-027-07
3-01-027-08
3-01-027-09
3-01-027-10
3-01-027-11
3-01-027-12
3-01-027-14
3-01-027-17
3-01-027-18
3-01-027-20
3-01-027-21
3-01-027-22
3-01-027-24
3-01-027-25
3-01-027-27
3-01-027-28
3-01-027-29
3-01-027-30
- Neutralizer
- Rotary Drum Granulator
- Pan Granulator
- Bulk Loading (General)
- Bagging Product
- Neutralizer (High Density)
- Prilling Tower (High Density)
- Prill Coolers (High Density)
- Evaporator /Concentrator (High
Density)
- Coating (High Density)
- Solids Screening
- Neutralizer (Low Density)
- Prilling Towers (Low Density)
- Prill Coolers (Low Density)
- Prill Dryer (Low Density)
- Evaporator/Concentrator (Low
Density)
- Coating (Low Density)
- Rotary Drum Granulator Coolers
- Pan Granulator Cooler
4
292
2
0
0
4
3
1
0
4
4
0
51
114
0
4
16
36
.35
.0
.68
.02
.19
.35
.18
.6
.52
.0
.35
.92
.6
.4
.52
.0
.2
.6
*0,
*0,
*0
*0,
*0
*0.
*0
*0
*0
*0
*0
*0
*0
*0
*0
*0
*0
*o
*0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
Tons
Tons
Tons
Tons
Tons
Tons
Tons
Tons
Tons
Tons
Tons
Tons
Tons
Tons
Tons
Tons
Tons
Tons
Tons
Units
Fiber
Produced
Product
Product
Product
Product
Product
Product
Product
Product
Product
Product
Product
Product
Product
Product
Product
Produced
Produced
Produced
Produced
Produced
Produced
Produced
Produced
Produced
Produced
Produced
Produced
Produced
Produced
Produced
Produced
Produced
Produced
Produced
Notes
110
200
368
114
114
11
11
11
11
11
11
11
11
11
11
11
11
11
11
11
11
11
11
11
*Refer to numbered notes In Appendix A or lettered notes in Appendix B; factors without asterisks are from AP-42.
-------
SCC Process
Normal SuoerDhosohate - 2874
3-01-028-01 - Grinding and Drying
3-01-028-03 - Rock Unloading
3-01-028-04 - Rock Feeder System
3-01-028-05 - Mixer/Den
3-01-028-06 - Curing Building
3-01-028-07 - Bagging/Handling
3-01-028-20 - Mixing
3-01-028-21 - Den
3-01-028-22 - Curing
3-01-028-23 - Aomoniator/Granulator
3-01-028-24 - Dryer
3-01-028-25 - Cooler
PART SO
Lbs/Unit Lbs/uhit
9.0 0.0
0.56 0.0
0.11 0.0
0.52 0.0
7.2 0.0
0.0
3-01-029-03 - Rock Unloading
3-01-029-04 - Rock Feeder System
3-01-029-05 - Run-of-Plle: Mlxer/Den/Curlng
3-01-029-06 - Granular: Reactor /Dryer
3-01-029-07 - Granular: Curing
3-01-029-08 - Bagging/Handling
3-01-029-20 - Mixing
3-01-029-21 - Den
3-01-029-22 - Curing
3-01-029-23 - Aomoniator/Granulator
3-01-029-24 - Dryer
3-01-029-25 - Cooler
Ammonium Phosphates — 2874
3-01-030-01 - Dryers and Coolers
3-01-030-02 - Amnoniator/Granulator
3-01-030-03 - Screening/Transfer
3-01-030-04 - Bagging/Handling
3-01-030-20 - Mixing
3-01-030-21 - Den
3-01-030-22 - Curing
3-01-030-23 - Ammoniator/Granulator
3-01-030-24 - Dryer
3-01-030-25 - Cooler
Terephthallc Acid/Dimethyl Tereohthalate - 2869
3-01-031-01 - HNO - Paraxylene - General
3-01-031-02 - Reactor Vent
3-01-031-03 - Crystallization, Separation and
Drying Vent
0.16 0.0
0.03 0.0
0.03 0.0
0.1
0.2 0.0
0.0
1.5 *3.1
1.52 *0.3
0.06 0.0
0.0
*NEG
*0.0
*0.0
*0.0
0.0
0.0
0.0
NO
Lbs/unit
0.0
0.0
0.0
0.0
0.0
0.0
2874
0.0
0.0
0.0
0.0
0.0
*1.7
"NEC
0.0
0.0
*NEG
*0.0
*0.0
•0.0
*0.06
*0.0
*0.0
VOC
Lbs/Unit
0.0
0.0
0.0
0.0
0.0
0.0
0.0
*NEG
*NEG
*NEG
*NEG
•NEC
0.0
0.0
0.0
•NEC
0.0
0.0
*NEG
*NEG
*NEG
*NEG
•NEC
•NEC
*0.03
*NEG
0.0
0.0
*NEG
•NEC
*NEG
*NEG
*NEG
*NEG
39.6
30.0
3.8
CO
Lbs/Unit
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
38.0
34.0
0.0
Units
Tons Produced
Tons P-0 Produced
2 5
Tons P.O Produced
Tons P-0, Produced
Tons P.0. Produced
Tons P.O Produced
Tons Fertilizer Produced
Tons Fertilizer Produced
Tons Fertilizer Produced
Tons Fertilizer Granulated
Tons Fertilizer Granulated
Tons Fertilizer Granulated
Tons P-0 Produced
Tons P.O Produced
2 5
Tons P.O Produced
Tons P.O Produced
Tons P-0 Produced
Tons P-O, Produced
Tons Fertilizer Produced
Tons Fertilizer Produced
Tons Fertilizer Produced
Tons Fertilizer Granulated
Tons Fertilizer Granulated
Tons Fertilizer Granulated
Tons P-0 Produced
Tons P.O Produced 72,
Tons P.O Produced
Tons P.O Produced
Tons Fertilizer Produced
Tons Fertilizer Produced
Tons Fertilizer Produced
Tons Fertilizer Produced
Tons P.O Produced
Tons P 0 Produced
Tons Produced
Tons Produced
Tons Produced
Notes
72
72
72
72
72
72
72
72
72
72
72
72
205
122, 303
72
72, 316
72
72, 121
72, 121
72, 121
109
295
295
Refer to numbered notes in Appendix A or lettered notes in Appendix B: factors without asterisks are from AP-A2.
-------
sec
Process
PART
Lbs/Unit
SO
Lbs/Unit
NO
Lbs/flnlt
VOC
Lbs/Unit
CO
Lbs/Unit
Units
Notes
tn
Terephthalic Acid/Dimethyl Terephthalate - 2869 (Continued)
3-01-031-04 - Distillation and Recovery Vent
3-01-031-05 - Product Transfer Vent
3-01-031-99 - Other Not Classified (Specify
in Commentj)
Elemental Sulfur Production - 2819
3-01-032-01 - Modified Claus: 2 Stage without
Control (92-951 Removal)
3-01-032-02 - Modified Claus: 3 Stage without
Control (95-961 Removal)
3-01-032-03 - Modified Claus: 4 Stage without
Control (96-97Z Removal)
3-01-032-04 - Sulfur Removal Process (99.9X
Removal)
Pesticides - 2879
3-01-033-01 - Malathion
3-01-033-11 - Agricultural Pesticides: General
3-01-033-12 - Agricultural Pesticides: General
3-01-033-99 - Other Not Classified (Specify
in Comments)
Amines/Amides Production - 2869
0.0
0.0
*0.0
*0.0
2.2
3.6
280.0
189.0
145.0
4.0
*0.35
*0.1
•0.1
*0.1
•3.0
*2.1
•2.1
*2.1
*0.05
0.0
4.0
Tons Produced
Tons Produced
Tons Produced
Tons 100X Sulfur
Tons 100X Sulfur
Tons 100X Sulfur
Tons 100X Sulfur
Gallons of Product
Gallons Stored
Pounds Stored
Tons Produced
295
295
141
12, 142
12, 142
12, 142
Aniline - 2869
3-01-034-02
3-01-034-03
3-01-034-04
3-01-034-05
3-01-034-06
Ethanolamin«
3-01-034-10
3-01-034-11
3-01-034-12
3-01-034-14
3-01-034-15
3-01-034-20
3-01-034-25
3-01-034-30
- General
- Reactor Recycle Purge Vent
- Dehydration Column Vent
- Purification Column Vent
- Fugitive Emissions: General*
>s - 2869
- General
- Ammonia Scrubber Vent
- Vacuum Distillation - Jet Vent
- Fugitive Emissions: General!
- Ethylenediamlne
- Hexamethylen*dlainine
- Hexamethylenetetramine
- Melamlne
*0.2
*0.2
*0.2
*0.0
*0.0
*0.4
*0.4
*0.4
*0.4
Tons Produced
Tons Product
Tons Product
Tons Product
Process Unit-Year
Tons Produced
Tons Product
Tons Product
Process Unit-Year
Tons Produced
Tons Produced
Tons Produced
Tons Produced
13
27
27
13
13
306
6
306
306
*Note that fugitive emissions are reported in units of Ibs/process unit-year rather than Ibs/ton product as in the NEDS Source Classification Codes
and Emission Factor Listing dated October 1985.
Refer to numbered notes in Appendix A or lettered notes in Appendix B; factors without asterisks are from AP-42.
-------
SCC Process
Ethanolamlnes - 2869 (Continued)
3-01-034-35 - Methylamines
3-01-034-99 - Other Not Classified (Specify
In Comments)
Inor«»ni- P'j»—nts - 2816
3-01-035-01 - HO Sulfate Process: Calciner4
3-01-035-02 - T1O Sulfate Process: Digester
3-01-035-03 - TiOJ: Chloride Process: Reactor
3-01-035-06 - Leal Oxide: Barton Pot
3-01-035-07 - Lead Oxide: Calcining Furnace
3-01-035-10 - Red Lead
3-01-035-15 - White Lead
3-01-035-20 - Lead Chromate
3-01-035-50 - Ore Grinding
3-01-035-51 - Ore Dryer
3-01-035-52 - Pigment Milling
3-01-035-53 - Pigment Dryer
3-01-035-54 - Conveying/Storage/Packing
3-01-035-99 - Other Not Classified (Specify
in Comments)
Sodium Bicarbonate - 2812
3-01-038-01 - General
Hydrogen Cyanide - 2819
3-01-039-01 - General
3-01-039-02 - Ammonia Absorber
3-01-039-03 - HCN Absorber
Urea Production - 2873
3-01-040-01 - General: Specify in Comments
3-01-040-02 - Solution Concentration
(Controlled)
3-01-040-03 - Prilling
3-01-040-04 - Drum Granulation
3-01-040-05 - Solid Product: Coating
3-01-040-06 - Solid Product: Bagging
3-01-040-07 - Bulk Loading
3-01-040-08 - Non-Fluldized Bed Prilling
(Agricultural Grade)
3-01-040-09 - Non-Fluidized Bed Prilling
3-01-040-10 -'Fluldlzed Bed Prilling
(Agricultural Grade)
PART
Lbs/Unit
230.0
0.64
15.0
1.0
0.69
0.2
8.0
0.0214
3.8
241.0
4.0
0.19
0.02
3.8
3.6
6.2
SO NO VOC
Lbs/9nit Lbs/flnit Lbs/Unit
*0.4
8.0 *0.0
*3.6 *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
•14.0
•NEC
•NEC
•0.0
*0.0
•0.0
•0.009
•0.0
•0.0
•0.0
*0.0
•0.0
•0.02
CO
Lbs/Unit Units
Tons Produced
Tons Produced
Tons Produced
Tons Produced
220.0 Tons Produced
Tons Produced
Tons Produced
Tons Produced
Tons Produced
Tons Produced
0.0 Tons Produced
0.0 Tons Produced
0.0 Tons Produced
0.0 Tons Produced
0.0 Tons Produced
Tons Produced
Tons Product
Tons Product
Tons Product
Tons Product
Tons Product
Tons Produced
Tons Produced
Tons Produced
Tons Produced
Tons Produced
Tons Produced
Tons Produced
Tons Produced
Tons Produced
Notes
306
70
70, 128
70
70
70
70
70
70
14
285
285
15
15
15
15
15
15
15
15
15
15
Refer to numbered notes in Appendix A or lettered notes in Appendix Bi factors without asterisks are from AP-42.
-------
PART SO NO
SCC Process Lbs/Unit Lbs/Unit Lbs/unit
Urea Production - 2873 (Continued)
3-01-040-11 - Fluldized Bed Prilling (Feed 3.6
Grade)
3-01-040-12 - Rotary Drum Cooler 7.45
3-01-040-13 - Solids Screening
Nitrocellulose - 2892
3-01-041-01 - Nitration Reactors 0.0 1.4 14.0
3-01-041-02 - Sulfurlc Acid Concentrator 0.0 68.0 0.0
3-01-041-03 - Boiling Tubs 0.0 0.0 2.0
3-01-041-04 - Nitric Acid Concentrator 0.0 0.0 14.0
Lead Alkyl Manufacture - (Sodium/Lead Alloy Process) - 2869
3-01-042-01 - Recovery Furnace 63. S *0.0 *2.67
3-01-042-02 - Process Vents (Tetraethyl Lead) 6.25
3-01-042-03 - Process Vents (Tetramethyl Lead) 193.5 *0.0 *0.0
3-01-042-04 - Sludge Pits 1.9
3-01-043-01 - General 1.4 *0.0
Organic Fertiliser - 2873
3-01-045-01 - General: Mixing/Handling *0.0 *0.0
Pharmaceutical Preoaratlons - 2834
3-01-060-01 - Vacuum Dryers
3-01-060-02 - Reactors
3-01-060-03 - Distillation Units
3-01-060-04 - Filters
3-01-060-05 - Extractors
3-01-060-06 - Centrifuges
3-01-060-07 - Crystallicers
3-01-060-08 - Exhaust Systems
3-01-060-09 - Air Dryers
3-01-060-10 - Storage /Transfer
3-01-060-11 - Coating Process
3-01-060-12 - Granulation Process
3-01-060-99 - Other Not Classified (Specify
in Comments)
Industrial Inornanic Chemical Production - General Processes - 2812-2819
3-01-070-01 - Fugitive Leaks
3-01-070-02 - Storage/Transfer
VOC
Lbs/Unit
*0.04
*0.0
*0.0
0.0
0.0
0.0
0.0
*0.0
*0.0
*0.0
•0.0
*0.0
*0.47
*NEG
*11.8
*0.09
•0.006
*0.006
*0.006
*0.006
*1.7
*0.07
200
200
*0.0
•0.0
CO
Lbs/Unit Units
Tons Produced
Tons Produced
Tons Produced
0.0 Tons Produced
0.0 Tons Produced
0.0 Tons Produced
0.0 Tons Produced
Tons Produced
Tons Produced
Tons Produced
Tons Produced
Tons Produced
Tons Processed
Hundreds of Lbs.
Hundreds of Lbs.
Hundreds of Lbs.
Hundreds of Lbs.
Hundreds of Lbs.
Hundreds of Lbs.
Hundreds of Lbs.
Hundreds of Lbs .
Hundreds of Lbs.
Hundreds of Lbs.
Tons Solvent in
Tons Solvent Cor
Hundreds of Lbs.
Tons Product
Tons Product
of Product
of Product
of Product
of Product
of Product
of Product
of Product
of Product
of Product
of Product
Coating
isumed
of Product
Notes
15
15
15
168
168
168
168
169
77
286
77
78
78
286
286
286
143
77
286
286
3
7
*Refer to numbered notes in Appendix A or lettered notes In Appendix Bs factors without asterisks are from AP-42.
-------
CO
SCC Process
Ketone Production - 2869
3-01-091-05 - Methyl Ethyl Ketone (MEK)
3-01-091-10 - Methyl Isobutyl Ketone (MIBK)
Acetone - 2869
3-01-091-01 - Acetone: General
3-01-091-51 - Cumene Oxidation
3-01-091-52 - CHP Concentrator
3-01-091-53 - Light-ends Distillation Vent
3-01-091-54 - Acetone Finishing Column
3-01-091-80 - Fugitive Emissions: General*
Ketone Production - 2869
3-01-091-99 - Other Not Classified (Specify
In Comments)
Malelc Anhydride - 2865
3-01-100-02 - Product Recovery Absorber
3-01-100-03 - Vacuum System Vent
3-01-100-04 - Brlquettlng
3-01-100-05 - Secondary Sources (Dehydration
Column, Vacuum System,
Fractlonatlon Column)
3-01-100-99 - Other Not Classified (Specify
In Comments)
Elemental Phosphorous - 2819
3-01-112-01 - Calclner
3-01-112-02 - Furnace
3-01-112-99 - Other Not Classified
Aldehydes Production - 2869
Formaldehyde - 2869
3-01-120-01 - Formaldehyde: Sliver Catalyst
3-01-120-02 - Formaldehyde: Mixed Oxide
Catalyst
3-01-120-05 - Absorber Vent
3-01-120-06 - Fractlonator Vent
3-01-120-07 - Fugitive Emissions: General*
PART SO NO VOC CO
Lbs/Unlt Lbs/Unlt Lbs/Unlt Lbs/Unlt Lbs/Unlt
*11.6
*0.0 *7.6
*4.2
*0.0 *0.6
*0.0 *1.3
•450,000
*0.1 174.0 1,360.0
*0.0 *0.0 *0.2
*0.0
*0.0 *0.0 *0.2
*HEG
*NEC
•0.0 *0.0 *13.0
*16.0
*2.2
•0.1
*36,000
Units
Tons Produced
Tons Produced
Tons Produced
Tons Product
Tons Product
Tons Product
Tons Product
Process Unit-Year
Tons Produced
Tons Produced
Tons Produced
Tons Produced
Tons Produced
Tons Produced
Tons Processed
Tons Processed
Tons Product
Tons Produced
Tons Produced
Tons Product
Tons Product
Process Unit-Year
Notes
105
108
108
108
108
If 2
165
125
16
125
89
89
14, 156
14
16
16
1, 2
'Note that fugitive emissions are reported In units of Ibs/process unit-year rather than Ibs/ton product as In the NEDS Source Classification Codes
and Emission Factor Listing dated October 1985.
*Refer to numbered notes In Appendix A or lettered notes In Appendix B; factors without asterisks are from AP-42.
-------
SCC Process
Acetaldehyde - 2869
3-01-120-11 - Acetaldchyde from Ethylene
3-01-120-12 - Acetaldehyde from Ethanol
3-01-120-13 - Off -Air Absorb. r Vent
3-01-120-14 - Off-Gas Absorber V«nt
3-01-120-17 - Fugitive Emissions: General*
Butvraldehydc - 2869
3-01-120-21 - General
Acrolein - 2869
3-01-120-31 - CO Stripping Tower
3-01-120-32 - Aqueous Acrolein Receiver
3-01-120-33 - Distillation System
3-01-120-34 - Refrigeration Unit
3-01-120-37 - Fugitive Emissions: Generalf
3-01-120-99 - Other Not Classified (Specify
in Comments)
** Oraanlc Ores /Pigments - 2865
10 3-01-121-99 - Other Not Classified (Specify
in Comments)
Chloroprene - 2869
3-01-124-01 - General
3-01-124-02 - Butadiene Dryer
3-01-124-03 - Chlorination Reactor
3-01-124-04 - Dlchlorobutene Still
3-01-124-05 - Isomerlratlon and 3,4-DCB
Recovery Vent
3-01-124-06 - Chloroprene Stripper
3-01-124-07 - Brine Stripper
3-01-124-80 - Fugitive Emissions: General*
Or«anohalo«ens Production - 2869
Ethvlene Dichlortde - 2869
3-01-125-01 - Ethylene Dichlorlde via
Oxychlorinatlon
3-01-125-02 - Ethylene Dichloride via Direct
Chlorination
3-01-125-04 - Caustic Scrubber
PART SO NO VOC
Lbs/Unit Lbs/flnlt Lbs/finlt Lbs/Unit
•0.0 *0.0 *2.8
*NEG *0.0 *0.04
*4.5
•5.6
*16S,000
*240.0
*120.0
*6.0
*54.0
*54.0
*2.4
*0.47
•7.8
•0.3
*0.3
•0.3
•0.0 *0.0 *24.1
•1.3
*0.0
CO
Lbs/Unit Units
Tons Produced
Tons Produced
Tons Product
Tons Product
Process Unit-Year
Tons Produced
Tons Product
Tons Product
Tons Product
Tons • Product
Process Unit-Year
Tons Product
Tons Produced
Tons Product
Tons Product
Tons Product
Tons Product
Tons Product
Tons Product
Tons Product
Process Unit-Year
Tons Produced
Tons Produced
Tons Product
Notes
14, 82
14, 82
17
17
1, 2
13
18
18
18
18
19
19
19
19
19
19
83, 156
83
13
*Note that fugitive emissions are reported in units of Ibs/process unit-year rather than Ibs/ton product as in the NEDS Source Classification Codes
and Emission Factor Listing dated October 1985.
*Refer to numbered notes in Appendix A or lettered notes In Appendix B; factors without asterisks are from AP-42.
-------
CJl
o
PART SO
SCC Process Lbs/Unlt Lbs/Bnit
Ethylene Di.chlori.de - 2869 (Continued)
3-01-125-05 - Reactor Vessel
3-01-125-06 - Distillation Unit
3-01-125-09 - Fugitive Emissions: General*
Chloromethanes - 2869
3-01-125-10 - General *NEG
3-01-125-11 - Recycled Methane Inert-Purge *NEG
3-01-125-12 - Drying Bed Regeneration Vent *NEG
3-01-125-14 - Fugitive Emission*: Generalf *NEG
Ethyl Chloride - 2869
3-01-125-15 - Ethyl Chloride: General
Perchloroethylene - 2869
3-01-125-20 - General *0.0
3-01-125-21 - Distillation Vent *0.0
3-01-125-22 - Caustic Scrubber *0.0
3-01-125-24 - Fugitive Emissions: Generalf *0.0
1.1.1-Trichloroethane (Methyl Chloroform) - 2869
3-01-125-25 - General
3-01-125-26 - HC1 Absorber Vent
3-01-125-27 - Drying Column Vent
3-01-125-28 - Distillation Column Vent
3-01-125-29 - Fugitive Emissions: General*
Trichloroethylene - 2869
3-01-125-30 - General
3-01-125-31 - Distillation Unit
3-01-125-32 - Neutral Izer
3-01-125-33 - Product Recovery Column
3-01-125-3* - Fugitive Emissions: General*
Chlorobenzene - 2869°*
3-01-125-35 - General
Vinyl Chloride - 2869
3-01-125-40 - General
3-01-125-41 - Cracking Furnace
3-01-125-42 - HC1 Recovery
3-01-125-43 - Light-ends Recovery Vent
HO VOC
Lbs/Snit Lbs/Unlt
•0.0
*0.0
*180,000
•0.0 *12.3
*0.0 *4.2
*0.0 *0.1
*0.0 *482,000
•0.0
*0.0 *3.5
*0.0 *0.09
•0.0 *0.005
*0.0 *730,000
*0.2
*2.0
*0.16
*77,000
•1.3
*0.03
*15.2
*0.8
•730,000
*0.8
•6.5
*0.0
*0.2
*2.0
CO
Lbs/Unit Units
Tons Product
Tons Product
Process Unit-Year
Tons Produced
Tons Product
Tons Product
Process Unit-Year
Tons Produced
Tons Produced
Tons Product
Tons Product
Process Unit-Year
Tons Produced
Tons Product
Tons Product
Tons Product
Process Unit-Year
Tons Produced
Tons Product
Tons Product
Tons Product
Process Unit-Year
Tons Produced
Tons Produced
Tons Product
Tons Product
Tons Product
Notes
13
13
1, 2
269
269
269
1, 2, 269
13
20, 267
20, 267
20, 267
1, 2, 267
284
284
104
1. 2
21
21
104
104
1, 2
13
22
22
22
22
* f . . . UU1UJJ 1.
and Emission Factor Listing dated October 1985.
Refer to numbered notes in Appendix A or lettered notes in Appendix B; factors without asterisks are from AP-42.
-------
sec
Process
PART SO NO VOC CO
Lbs/Unit Lbs/8nit Lbs/Unit Lbs/Unit Lbs/Unit
Units
Notes
Vinyl Chloride - 2869 (Continued)
3-01-125-44
3-01-125-45
3-01-125-46
3-01-125-47
3-01-125-50
- Drying Colunn/Dichloroethane
- Drying Column/Vinyl
Monomer
Chloride
- Product Recovery Still
- Cracking Furnace Decoking
- Fugitive Emissions:
General*
*2
*2
*1
*0
•275,000
.0
.0
.4
.0
Tons
Tons
Tons
Tons
Product
Product
Product
Product
Process Unit-Year
22
22
368
368
1,
2
Vinyl tdene Chloride - 2869
3-01-125-51
3-01-125-52
3-01-125-53
3-01-125-55
Chlorinated
- General
- Dehydrochlorination
Purge Vent
- Distillation Column
Reactor
Vents
- Fugitive Emissions: General*
Orcanics - Other Not Classified - 2869
*15
•0.0 *0.0 *12
•0.0 *0.0 *1
•19,000
.7
.4
.4
Tons
Tons
Tons
Product
Product
Product
Process Unit-Year
25
25,
25,
346
318
318
3-01-125-99 - Chlorine Organlcs: Specify In
Comments
Bromlnated Organic* - 2869
Tons Produced
3-01-126-99 - Bromine Organlcs
FLuoroc*rl>ons/Clilorof luorocarbons ~ 2869
3-01-127-01 - General
3-01-127-02 - Distillation Column
3-01-127-03 - HC1 Recovery Column
3-01-127-20 - Chlorofluorocarbon 12/11
3-01-127-30 - Chlorofluorocarbon 23/22
3-01-127-40 - Chlorofluorocarbon 113/114
3-01-127-80 - Fugitive Emissions: General*
Amnonl1-" Sulfate - 2873
3-01-130-04 - Rotary Dryer
3-01-130-05 - Fluid Bed Dryer
Organic Acids Production - 2869
Acetic Acid - 2869
3-01-132-01 - Acetic Acid via Methanol
3-01-132-05 - Acetic Acid via Butane
3-01-132-10 - Acetic Acid via Acetaldehyde
*0.0 *0.0 *17.1
•0.0 *0.0 *16.6
*0.0 *0.0 *0.0
•6.2
•38
•13
46.0 1.48
218.0 1.48
•0.0 *0.06 *4
•0.0 *0.08 *14
•0.0 *0.0 *22
Tons Produced
Tons Produced
Tons Product
Tons Product
Tons Produced
Tons Produced
Tons Produced
Process Unit-Year
Tons Produced
Tons Produced
Tons Produced
Tons Produced
Tons Produced
268
268
268
49
49
49
105, 82
14, 82
14, 82
Note that fugitive emissions are reported in units of Ibs/process unit-year rather than Ibs/ton product as in the NEDS Source Classification Codes
and Emission Factor Listing dated October 1985.
Refer to numbered notes in Appendix A or lettered notes in Appendix B; factors without asterisks are from AP-42.
-------
sec
Acrylic Acid
3-01-132-21 -
3-01-132-22 -
3-01-132-23 -
3-01-132-24 -
- 2869
General
Process
Quench Absorber
Extraction
Vacuum Sysl
Column
PART SO NO VOC
Lbs/Unlt Lbs/Unlt Lbs/Unit Lbs/Unlt
*240
•239
*1.6
•10.5
CO
Lbs/Unit
Tons
Tons
Tons
Tons
Units
Product
Product
Product
Product
Notes
14
23
23
23
3-01-132-27 - Fugitive Emissions: General*
Organic Acids Production - 2869
3-01-132-99 - Other Not Classified (Specify
In Comments)
Process Unit-Year
Tons Produced
Acetic Anhydride - 2869
3-01-133-01 - General
3-01-133-02 - Reactor By-Product Gas Vent
3-01-133-03 - Distillation Column Vent
3-01-133-80 - Fugitive Emissions: General*
Esters Production - 2869
3-01-137-01 - Ethyl Acrylate
3-01-137-10 - Butyl Acrylate
tn 3-01-137-99 - Acrylates: Specify in Comments
ro
Acetylene Production - 2813
3-01-140-01 - Raw Material Handling
3-01-140-02 - Grinding /Milling
3-01-140-03 - Mixing
3-01-140-04 - Waste Handling
3-01-140-05 - General
Blsohenoi A - 2869
3-01-152-01 - General
Butadiene - 2869
3-01-153-01 - General
3-01-153-10 - Houdry Process: General
3-01-153-11 - Flue Gas Vent
3-01-153-12 - Dehydrogenation Reactor
3-01-153-20 - N-Butene Process: General
3-01-153-21 - Flue Gas Vent
3-01-153-22 - Hydrocarbon Absorber Column
3-01-153-80 - Fugitive Emissions: General*
*0.0 *0.0 *5.5
•9.0
*1.4
*29.1
*5.4
- *0.6
•NEC
*NEG
*NEC
*13.5 *9.3
*0.0
*23
*0.1
*11.0
*23
•0.1
no.o
*313,000
Tons Produced
Tons Product
Tons Product
Process Unit-Year
Tons Produced
Tons Produced
Tons Produced
Tons Throughput
Tons Throughput
Tons Throughput
Tons Throughput
10 Cubic Feet Produced
Tons Produced
Tons Product
Tons Product
Tons Product
Tons Product
Tons Product
Tons Product
Tons Product
Process Unit-Year
24
26
26
336
335
13
206
206
206
206
13
26
26
14
26
26
26
101
*Note that fugitive emissions are reported in units of Ibs/process unit-year rather than Ibs/ton product as in the NEDS Source Classification Codes
and Emission Factor Listing dated October 1985.
*Refer to numbered notes in Appendix A or lettered notes in Appendix B: factors without asterisks are from AP-42.
-------
PART
SCC Process Lbs/Unit
Curoene Production - 2865
3-01-156-01 - General
3-01-156-02 - Benzene Drying Column
3-01-156-03 - Catalyst Mix Tank Scrubber Vent
3-01-156-04 - Wash-Decant System Vent
3-01-156-05 - Benzene Recovery
3-01-156-06 - Cumene Distillation System Vent
3-01-156-07 - DIPB Stripping Vent
3-01-156-80 - Fugitive Emissions: General*
Cyclohexane - 2865
3-01-157-01 - General
3-01-157-02 - Slowdown Tank Discharge
3-01-157-04 - Catalyst Replacement
3-01-157-80 - Fugitive Emissions: General*
Cvclohexanone/ol - 2869
3-01-158-01 - General
3-01-158-80 - Fugitive Emissions: General*
Cvclohexanone/ol - Cvclohexane Oxidation Process - 2869
3-01-158-02 - High Pressure Scrubber Vent
3-01-158-03 - Low Pressure Scrubber Vent
Cvclohexanone/ol - Phenol Hvdro«enation Process - 2869
3-01-158-21 - Hydrogenation Reactor Vent
3-01-158-22 - Distillation Vent
Vinvl Acetate - 2869
3-01-167-01 - General
3-01-167-02 - Inert-Gas Purge Vent
3-01-167-03 - CO Vent
3-01-167-04 - Inhibitor Mix Tank Discharge
3-01-167-80 - Fugitive Emissions: General*
3-01-167-99 - Specify in Comments
Ethvlbenzene - 2865
3-01-169-01 - General
3-01-169-02 - Alkylatlon Reactor Vent
3-01-169-03 - Benzene Drying
3-01-169-04 - Benzene Recovery/Recycle
3-01-169-05 - Ethylbenzene Recovery
SO NO VOC
Lbs/finit Lbs/Unit Lbs/Unit
•1.1
•0.4
•0.3
•0.02
•0.03
•0.06
•0.002
•150,000
•0.006
•NEC
•0.0
•240,000
•78
•33.5
•5.2
•3.0
•0.12
•8.8
•0.6
•5.6
•360,000
•0.01
•0.0
•0 .0
•0.0
•0.0
CO
Lbs/Unit Units
Tons Produced
Tons Product
Tons Product
Tons Product
Tons Product
Tons Product
Tons Product
Process Unit-Year
Tons Produced
Tons Product
Tons Product
Process Unit-Year
Tons Produced
Process Unit-Year
Tons Product
Tons Product
Tons Product
Tons Product
Tons Produced
Tons Product
Tons Product
Tons Product
Process Unit-Year
Tons Product
Tons Produced
Tons Product
Tons Product
Tons Product
Tons Product
Notes
27
27
27
27
27
27
27
1, 2
30
30
1, 2
29
30
30
30
30
31
31
31
1, 2
13
13
13
13
13
*Note that fugitive emissions are reported in units of Ibs/proces, unit-year rather than lb,/ton product as in the NEDS Source Classification Codes
and Emission Factor Listing dated October 1985.
*Refer to numbered notes in Appendix A or lettered notes in Appendix B; factors without asterisks are from AP-42.
-------
01
PART SO
SCC Process Lbs/Unit Lbs/unit
Ethvlbeniene - 2865 (Continued)
3-01-169-06 - Polyethylbenzene Recovery
3-01-169-80 - Fugitive Emissions: General*
Ethvlene Oxide - 2869
3-01-174-01 - General
3-01-174-02 - Air-Oxidation Process Reactor -
Main Vent
3-01-174-10 - Oxygen-Oxidation Process Reactor -
CO Purge Vent
3-01-174-11 - Oxygen-Oxidation Process Reactor -
Argon Purge Vent
3-01-174-21 - Stripper Purge Vent
3-01-174-80 - Fugitive Emissions: General*
Glycerin (Glvcerol) - 2869
3-01-176-01 - General
3-01-176-10 - Chlorination Process: General *0.0
3-01-176-11 - CO Absorber Vent
3-01-176-12 - Evaporator
3-01-176-13 - Concentrator
3-01-176-14 - Stripping Column
3-01-176-15 - Light-ends Stripping Column
3-01-176-16 - Solvent Stripping Column
3-01-176-17 - Product Distillation Column
3-01-176-18 - Cooling Tower
3-01-176-30 - Oxidation Process: General
3-01-176-31 - Light-ends Stripper
3-01-176-32 - Concentrator
3-01-176-33 - Glycerin Flasher Column
3-01-176-34 - Product Distillation Column
3-01-176-80 - Fugitive Emissions: General*
Toluene Diisocvanate - 2865
3-01-181-01 - General
3-01-181-02 - Sulfurlc Acid Concentrator
3-01-181-03 - Nitration Reactor
3-01-181-04 - Catalyst Filtration
3-01-181-05 - IDA Vacuum Distillation Unit
3-01-181-06 - Dlchlorobenzene Solvent Recovery
3-01-181-07 - TDI Flash Distillation
3-01-181-08 - TDI Purification
NO VOC
Lbs/Bnit Lbs/Unit
•0.0
•329,000
•7.8
•2.8
•8.0
•21.8
•0.004
•168,000
•130
•0.0
•0.8
•0.0
•0.0
•0.0
•0.0
•0.2
•0.0
•5.6
•30.0
•0.3
•0.3
•0.3
•10.0
•0.05
•0.001
•0.007
•3
•3
•3
CO
Lbs/Unit Units
Tons Product
Process Unit-Year
Tons Produced
Tons Product
Tons Product
Tons Product
Tons Product
Process Unit-Year
Tons Produced
Tons Product
Tons Product
Tons Product
Tons Product
Tons Product
Tons Product
Tons Product
Tons Product
Tons Product
Tons Product
Tons Product
Tons Product
Tons Product
Tons Product
Process Unit-Year
Tons Produced
Tons Product
Tons Product
Tons Product
Tons Product
Tons Product
Tons Product
Tons Product
Notes
13
106
13
13
31
31
32
31
34
156
33
33
33
33
33
33
33
33
33
33
33
33
35
35
35
35
35
35
35
*Note that fugitive emissions are reported in units of Ibs/process unit-year rather than Ibs/ton product as in the NEDS Source Classification Codes
and Emission Factor Listing dated October 1985.
*Refer to numbered notes In Appendix A or lettered notes In Appendix B; factors without asterisks are from AP-42.
-------
cn
en
SCC Process
Toluene Diisocyanate - 2865 (Continued)
3-01-181-09 - Residue Vacuum Distillation Unit
3-01-181-10 - HC1 Absorber
3-01-181-80 - Fugitive Emissions: Generall
Methyl Methacrylate - 2869
3-01-190-01 - General
3-01-190-02 - Acetone Cyanohydrln Reactor
Off-Gas
3-01-190-03 - Recovery Columns
3-01-190-04 - Acetone Evaporation Vacuum Vent
3-01-190-10 - Hydrolysis Reactor
3-01-190-11 - Distillation Unit
3-01-190-12 - MMA and Light-ends Distillation
Unit
3-01-190-13 - Acid Distillation
3-01-190-1* - MMA Purification
3-01-190-80 - Fugitive Emissions: General!
Nitrobenzene - 2865
3-01-195-01 - General
3-01-195-02 - Reactor and Separator Vent
3-01-195-03 - Acid Stripper Vent
3-01*195-04 - Hasher and Neutralizer Vent
3-01-195-05 - Nitrobenzene Stripper Vent
3-01-195-06 - Waste Acid Storage
3-01-195-80 - Fugitive Emissions: General*
01 « fins Production - 2869
Ethvlene - 2869
3-01-197-01 - General
3-01-197-41 - Flue Gas Vent
3-01-197-42 - Pyrolysis Furnace Decoking
3-01-197-43 - Acid Gas Removal
3-01-197-44 - Catalyst Regeneration
3-01-197-45 - Compressor Lube Oil Vent
3-01-197-49 - Fugitive Emissions: General*
ProoTlene - 2869
3-01-197-05 - General
3-01-197-06 - Reactor
PART SO NO VOC
Lbs/Unit Lbs/Unit Lbs/Unit Lbs/Unit
*0.0
*0.0
*0.08
*2.3
*0.008
*13.2
*1.9
*16.5
*1.1
*14.1
•27,000
*2.7
*1.9
*0.34
*0.02
*0.34
*0.005
*138,000
*0.86
*0.0
*0.02
•NEC
*14.6
*69S,000
*1.0
*0.0
CO
Lbs/Unit Units
Tons Product
Tons Product
Process Unit-Year
Tons Product
Tons Product
Tons Product
Tons Product
Tons Product
Tons Product
Tons Product
Tons Product
Tons Product
Process Unit-Year
Tons Produced
Tons Product
Tons Product
Tons Product
Tons Product
Tons Product
Process Unit-Year
Tons Produced
Tons Product
Tons Product
Tons Product
Tons Product
Tons Product
Process Unit-Year
Tons Produced
Tons Product
Notes
35
35
36
36
36
36
36
36
36
36
1, 2
13
37
37
37
37
37
1, 2
38
44
38
44
44
1, 2
207
13
*Note that fugitive emissions are reported in units of Ibs/process unit-year rather than Ibs/ton product as in the NEDS Source Classification Codes
and Emission Factor Listing dated October 1985.
*Refer to numbered notes in Appendix A or lettered notes In Appendix Bi factors without asterisks are from AP-42.
-------
SCC Process
Propylene - 2869 (Continued)
3-01-197-07 - Drying Tower
3-01-197-08 - Light-end* Stripper
3-01-197-09 - Fugitive Emissions: General*
ButYlene - 2869
3-01-197-10 - General
3-01-197-99 - Other Not Classified (Specify
in Comments)
Phenol - 2865
3-01-202-01 - General
3-01-202-02 - Cumene Oxidation
3-01-202-03 - CHP Concentrator
3-01-202-0* - Light-ends Distillation Vent
3-01-202-05 - Acetone Finishing Column
3-01-202-06 - Phenol Distillation Column
3-01-202-10 - Oxidate Wash/ Separation
3-01-202-11 - CHP Cleavage Vent
3-01-202-80 - Fugitive Emissions: General*
cn
cn
Proovlene Oxide - 2869
3-01-205-01 - General
3-01-205-02 - Chlorohydronatton Process:
General
3-01-205-03 - Vent Gas Scrubber Vent
3-01-205-0* - Saponlficatlon Column Vent
3-01-205-05 - PO Stripping Column Vent
3-01-205-06 - Light-ends Stripping Column Vent
3-01-205-07 - PO Final Distillation Column Vent
3-01-205-08 - DCP Distillation Column Vent
3-01-205-09 - DCIPE Distillation Column Vent
3-01-205-20 - Isobutane Bydroperoxide Process:
General
3-01-205-21 - Oxidation Reactor Scrubber Vent
3-01-205-22 - TBA Stripping Column Vent
3-01-205-23 - Catalyst Mix Tank Vent
3-01-205-2* - PO Stripping Column Vent
3-01-205-25 - Crude TBA Recovery Column Vent
3-01-205-26 - TBA Wash-Decant System Vent
3-01-205-27 - Wastewater Stripping Column Vent
3-01-205-28 - Solvent Scrubber Vent
*Hote that fugitive emissions are reported in units
and Emission Factor Listing dated October 1985.
*Refer to numbered notes in Appendix A or lettered
PART SO NO VOC CO
Lbs/Unit Lbs/Unit Lbs/finlt Lbs/Unit Lbs/Unit
*0.02
*0.01
*20
•0.0 *0.0 *7.6
**.2
*0 . 0 *0 . 6
•0.0 *1.3
•0.0 *7.6
•0.0 *0.16
*0.0 *0.95
•731,000
•20.5
•0.09
•0.01
•0.01
•0.01
*0 . 0002
•0.0
•3.5
•0.008
•0.0
•0.04
•0.03
•0.01
•1.9
•1.3
Units
Tons Product
Tons Product
Process Unit-Year
Tons Produced
Tons Produced
Tons Produced
Tons Product
Tons Product
Tons Product
Tons Product
Tons Product
Tons Product
Tons Product
Process Unit-Year
Tons Produced
Tons Product
Tons Product
Tons Product
Tons Product
Tons Product
Tons Product
Tons Product
Tons Product
Tons Product
Tons Product
Tons Product
Tons Product
Tons Product
Tons Product
Tons Product
Tons Product
Tons Product
of Ibs/process unit-year rather than Ibs/ton product as in the NEDS Source Classification
notes in Appendix B; factors without asterisks are from AP-42.
Notes
368
368
39
39, 156
39
108
108
39
108
108
1, 2
40
40
40
40
40
40
40
40
40
40
40
40
40
40
40
40
Codes
-------
PART
SCC Process Lbs/Unlt
Propylene Oxide - 2869 (Continued)
3-01-205-29 - Solvent Recovery Column Vent
3-01-205-30 - Water Stripping Column Vent
3-01-205-31 - Propylene Glycol and Dipropylene
Glycol Combined Column Vent
3-01-205-32 - Flue Gas Vent
3-01-205-40 - Ethylbencene Hydroperoxlde
Process : General
3-01-205-41 - Oxidation Reactor Scrubber Vent
3-01-205-42 - Falling Film Evaporator Vent
3-01-205-43 - Catalyst Mix Tank Vent
3-01-205-44 - Separation Column Vent
3-01-205-45 - Light-ends Stripping Column Vent
3-01-205-46 - Propylene Recovery Column Vent
3-01-205-47 - Product Wash-Decant System Vent
3-01-205-48 - Mixed Hydrocarbon Wash-Decant
System Vent
3-01-205-49 - Ethylbencene Wash-Decant System
Vent
3-01-205-50 - Ethylbencene Stripping Column Vent
3-01-205-51 - Light Hydrocarbon Stripping Column
i£ Vent
3-01-3D5-52 - MBA-AP Stripping Column Vent
3-01-205-53 - Dehydration Reactor System Vent
3-01-205-54 - Light Impurities Stripping Column
Vent
3-01-205-55 - Styrene Finishing Column Vent
3-01-205-80 - Fugitive Emissions: General*
Styrene - 2865
3-01-206-01 - General
3-01-206-02 - Bencene Recycle
3-01-206-03 - Styrene Purification
3-01-206-80 - Fugitive Emissions: General*
« 1 — —*••—) _ Ofl£Q
3-01-210-01 - General
3-01-210-02 - Cyclohexanone Purification Vent
3-01-210-03 - Dehydrogenation Reactor Vent
3-01-210-04 - Oleum Reactor
3-01-210-05 - Neutralization Reactor Vent
3-01-210-06 - Solvent Separation/Recovery
SO NO VOC CO
Lbs/finit Lbs/flnlt Lbs/Unit Lbs/Unlt
•0.0009
•0.003
•0.1
•0.08
•1.0
•0.01
•0.0
•0.3
•0.3
•0.3
•0.01
•0.003
•0.003
•0.003
•0.003
•0.02
•0.02
•2.5
•1.7
•0.0 *0.04 *33
•0.6
•12
•248,000
•6.2
•0.02
•NEC
•0.08
•4.0
Units
Tons Product
Tons Product
Tons Product
Tons Product
Tons Product
Tons Product
Tons Product
Tons Product
Tons Product
Tons Product
Tons Product
Tons Product
Tons Product
Tons Product
Tons Product
Tons Product
Tons Product
Tons Product
Tons Product
Tons Product
Process Unit-Year
Tons Produced
Tons Product
Tons Product
Process Unit-Year
Tons Product
Tons Product
Tons Product
Tons Product
Tons Product
Tons Product
Notes
40
40
40
40
40
40
40
40
40
40
40
40
40
40
40
40
40
40
40
40
41, 155
42
13
1, 2
42
292
42
42
42
*Note that fugitive emissions are reported in units of Ibs/process unit-year rather than Ibs/ton product as In the NEDS Source Classification Codes
and Emission Factor Listing dated October 1985.
*Refer to numbered notes in Appendix A or lettered notes in Appendix B: factors without asterisks are from AP-42.
-------
tn
Co
SCC Process
Caorolaetam - 2869 (Continued)
3-01-210-07 - Oximation Reactor and Separator
3-01-210-08 - Caprolactan Purification
3-01-210-09 - Ammonium Sulfate Drying
3-01-210-10 - Ammonium Sulfate Cooling/
Screening/Storage
3-01-210-80 - Fugitive Emissions: General*
Linear Alkvlbengene - 2B69
3-01-211-01 - Olefln Process: General
3-01-211-02 - Benrene Drying
3-01-211-03 - Hydrogen Fluoride Scrubber Vent
3-01-211-04 - Vacuum Refining
3-01-211-21 - Chlor last ion Process: General
3-01-211-22 - Parrafin Drying Column Vent
3-01-211-23 - HC1 Absorber Vent
3-01-211-24 - Atmospheric Hash-Decant Vent
3-01-211-25 - Benzene Stripping Column Vent
3-01-211-80 - Fugitive Emissions: General*
Alcohols Production - 2869
Methanol - 2869
3-01-250-01 - General
3-01-250-02 - Purge Gas Vent
3-01-250-03 - Distillation Vent
3-01-250-04 - Fugitive Emissions: General*
Alcohols Production - 2869
3-01-250-05 - Ethanol from Ethylene
3-01-250-10 - Ethanol by Fermentation
3-01-250-15 - Isopropanol
3-01-250-21 - Alcohols by Oxo Process
3-01-250-25 - Fatty Alcohols by Hydrogenation
3-01-250-99 - Other Not Classified (Specify
in Comments)
Ethylene Glvcol - 2869
3-01-251-01 - General
3-01-251-02 - Evaporator Purge Vent
3-01-251-03 Water Sasoval Stss= Jet Ejsctcr
3-01-251-04 - Distillation Column Vent
3-01-251-80 - Fugitive Emissions: General*
PART SO HO VOC
Lbs/Unlt Lbs/unit Lbs/fintt Lbs/Unlt
*0.05
*0.3
•1.2
*0.1
*0.008
•22
*0.2
•5.6
*0.1
*25
*7.4
*2.2
*0.8
•575,000
*0.9
*1.9
*NEG
•4.0
*3.0
*0.95
*i 2
*0.0
*24,000
CO
Lbs/Unit Units
Tons Product
Tons Product
Tons Product
Tons Product
Process Unit-Year
Tons Product
Tons Product
Tons Product
Tons Product
Tons Product
Tons Product
Tons Product
Tons Product
Tons Product
Process Unit-Year
Tons Produced
Tons Product
Tons Product
Process Unit-Year
Tons Produced
Tons Produced
Tons Produced
Tons Produced
Tons Produced
Tons Produced
Tons Produced
Tons Product
Tons Product
Tons Product
Process Unit-Year
Hotes
42
42
42
42
13
43
43
43
43
43
43
44
44
44
372
143
372
372
372
13
13
13
1, 2
*Note that fugitive emissions are reported in units of Ibs/process unit-year rather than Us/ton product as in the NEDS Source Classification Codes
and Emission Factor Listing dated October 1985.
*R*fer to numbered notes in Appendix A or lettered notes In Appendix B; factors without asterisks are from AP-42.
-------
cn
vo
PART
SCC Process Lbs/Unlt
Ethers Production - 2869
3-01-252-01 - General
Glycol Ethers - 2869
3-01-253-01 - General
3-01-253-02 - Vacuum System Vent
3-01-253-05 - Catalyat-Methanol Mix Tank
3-01-253-06 - Methanol Recovery Column Vent
3-01-253-15 - Catalyst -Ethanol Mix Tank
3-01-253-16 - Ethanol Recovery Column Vent
3-01-253-25 - Catalyst-Butanol Mix Tank
3-01-253-26 - Butanol Recovery Column Vent
3-01-253-80 - Fugitive Emissions: General*
Httriles Production - 2869
3-01-254-01 - Acetonitrile
Acrylonitrile - 2869
3-01-254-05 - General
3-01-254-06 - Absorber Vent: Normal
3-01-254-07 - Absorber Vent: Startup
3-01-254-08 - Recovery/Purification Column Vent
3-01-254-09 - Fugitive Emissions: General*
Adiponitrile - 2869
3-01-254-10 - via Adipic Acid: General
3-01-254-11 - Ammonia Recovery Still
3-01-254-12 - Product Fractionator
3-01-254-13 - Product Recovery Vent
3-01-254-15 - via Butadiene: General
3-01-254-16 - Chlorlnation Reactor
3-01-254-17 - Cyanide Synthesis
3-01-254-18 - Cyanation/Isomerization
3-01-254-20 - Fugitive Emissions: General*
Hitriles Production - 2869
3-01-254-99 - Other Not Classified (Specify
in Comments)
SO NO VOC
Lbs/flnit Lbs/unit Lbs/Unit
*0.0 *0.0 *0.16
•0.03
*0.02
*0.03
*0.01
•0.19
*0.002
*0.03
*20,100
*200
*220
•200
*0.5
*20.0
*22,000
*1.6
*NEG
•20
•20
*51
•36
*0.0
•15.5
CO
Lbs/Unit Units
Tons Produced
Tons Produced
Tons Product
Tons Product
Tons Product
Tons Product
Tons Product
Tons Product
Tons Product
Process Unit-Year
Tons Produced
Tons Produced
Tons Product
Tons Product
Tons Product
Process Unit-Year
Tons Produced
Tons Product
Tons Product
Tons Product
Tons Product
Tons Product
Tons Product
Tons Product
Process Unit-Year
Tons Produced
Notes
168
45
45
45
45
45
45
45
45
136
14
46
46
46
1. 2
13
285
52
52
47
47
47
47
*Not. that fugitive emission, are reported in unit, of Ibs/proc.s, unit-year rather than lb,/ton product a, in the NEDS Source Classification Codes
and Emission Factor Listing dated October 1985.
*Refer to numbered notes in Appendix A or lettered notes in Appendix B; factors without asterisks are from AP-42.
-------
SCC Process
Aromatics Production - 2869
Benzene Production - 2869
3-01-258-01 - General
3-01-258-02 - Reactor
3-01-258-03 - Distillation Vent
Toluene Production - 2869
3-01-258-05 - General
3-01-258-06 - Reactor
3-01-258-07 - Distillation Vent
Aromatics Production - 2869
3-01-258-10 - p-Xylene
Mixed Xvlenes - 2869
3-01-258-15 - General
3-01-258-16 - Reactor
3-01-258-17 - Distillation Unit
Aromatics Production - 2869
3-01-258-80 - Fugitive Emissions: Ceneralf
3-01-258-99 - Other Hot Classified (Specify
in Comment a)
Chlorobenzene - 2865
3-01-301-35 - General
3-01-301-01 - Tall Gas Scrubber
3-01-301-02 - Benzene Drying: Distillation
3-01-301-03 - Benzene Recovery
3-01-301-04 - Heavy-ends Processing
3-01-301-05 - MCB Distillation
3-01-301-06 - Vacuum System Vent
3-01-301-07 - DCBz Crystallization
3-01-301-08 - DCBz Crystal Handling/Loading
3-01-301-10 - Catalyst Incineration
3-01-301-80 - Fugitive Emissions: General*
Carbon Tetrachlorlde - 2869
3-01-302-01 - General
^_ni_4no_ ni - ni _* « i i »*• i «. u_«%«-
3-01-302-03 - Caustic Scrubber
3-01-302-80 - Fugitive Emissions: General*
PART SO NO VOC
Lbs/Unlt Lbs/Bnit Lbs/finit Lbs/Unit
*0.3
•0.8
*0.3
*0.8
•0.3
*0.8
*379,000
*1.2
*0.8
*0.0 *0.0 *0.002
*0.0 *0.0 *0.2
*0.0 *0.0 *0.8
*0.0 *0.0 *0.9
*0.0 *0.0 *0.03
*0.0 *0.0 *0.04
*NEG
•418,000
J,n n4
•0.3
*166,000
CO
Lbs/Unit Units
Tons Produced
Tons Product
Tons Product
Tons Produced
Tons Product
Tons Product
Tons Produced
Tons Produced
Tons Produced
Tons Produced
Process Unit-Year
Tons Produced
Tons Product
Tons Product
Tons Product
Tons Product
Tons Product
Tons Product
Tons Product
Tons Product
Tons Product
Process Unit-Year
Tons Product
— .. .
i ons f r oouc c
Tons Product
Process Unit-Year
Notes
13
368
368
368
368
368
238
48
48
13
48
48
48
48
48
285
48
-
ty
49
100
Note that fugitive emissions are reported in units of Ibs/process unit-year rather than Ibs/ton product as in the NEDS Source Classification Codes
and Emission Factor Listing dated October 1985.
*
Refer to numbered notes in Appendix A or lettered notes in Appendix B; factors without asterisks are from AP-42.
-------
CTl
PART SO
scc Process Lbj/Onit Lbs/Unit
Allyl Chloride - 2869
3-01-303-01 - Chlorlnation Process: General
3-01-303-02 - BCL Absorber
3-01-303-03 - Light-ends Distillation Column
3-01-303-04 - Allyl Chloride Distillation Column
3-01-303-05 - Dichloropropene Distillation
Column
3-01-303-80 - Fugitive Emissions: General!
Allyl Alcohol - 2869
3-01-304-01 - General
3-01-304-02 - Catalyst Preparation
3-01-304-03 - Filtration System
3-01-304-04 - Light-ends Stripper
3-01-304-05 - Distillation System Condenser
3-01-304-80 - Fugitive Emissions: General!
Epichlorohydrln - 2869
3-01-305-01 - General
3-01-305-02 - Epoxldation Reactor
3-01-305-03 - Azeotrope Column
3-01-305-04 - Light-ends Stripper
3-01-305-05 - Finishing Column
3-01-305-80 - Fugitive Emissions: General!
NO VOC
Lbs/8nlt Lbs/Unit
*0.3
*130.0
*130.0
*2.0
*450
•6.4
*22
*23
*208
*208
*0.003
*0.7
CO
Lbs/Unit Units
Tons Product
Tons Product
Tons Product
Tons Product
Tons Product
Process Unit-Year
Tons Product
Tons Product
Tons Product
Tons Product
Tons Product
Process Unit-Year
Tons Product
Tons Product
Tons Product
Tons Product
Tons Product
Process Unit-Year
Notes
51
51
51
51
51
51
51
51
13
13
13
13
General Processes - 2865. 2869
3-01-800-01 - Fugitive Leaks!
3-01-810-01 - Air Oxidation Units
3-01-820-01 - Uastewater Separators
3-01-830-01 - Storage/Transfer
3-01-840-01 - Distillation Units
*0.85
Process Unit-Year
Tons Product
Tons Product
Tons Product
Tons Product
53
Inorganic Chemical Storage
Fixed Roof Tanks
3-01-870-01 - Hydrochloric Acid: Breathing Loss
*0.0
*0.0
*0.0
10 Gallons Storage
Capacity
70, 263
3-01-870-02
3-01-870-03
3-01-870-04
3-01-870-05
- Hydrochloric
- Hydrofluoric
- Hydrofluoric
- Nitric Acid:
Acid:
Acid:
Acid:
Working Loss
Breathing Loss
Working Loss
Breathing Loss
*0
*0
*0
*0,
.0
.0
.0
.0
*0.0
*0.0
*0.0
*0
*0
*0
*0,
.0
.0
.0
.0
10 Gallons
10 Gallons
Capacity
10* Gallons
10 Gallons
Capacity
Throughput
Storage
Throughput
Storage
70, 263
70, 263
70, 263
70
Note that fugitive emissions are reported in units of Ibs/process unit-year rather than Ibs/ton product as in the NEDS Source Classification Codes
and Emission Factor Listing dated October 1985.
*
Refer to numbered notes in Appendix A or lettered notes in Appendix B; factors without asterisks are from AP-42.
-------
cn
PART SO NO
SCC Process Lbs/Unlt Lbs/unit Lbs/unit
Fixed Roof Tanks (Continued)
3-01-870-06 - Nitric Acid: Working Loss *0.0
3-01-870-07 - Phosphoric Acid: Breathing Loss *0.0 *0.0
3-01-870-08 - Phosphoric Acid: Working Loss *0.0 *0.0
3-01-870-09 - Sulfuric Acid: Breathing Loss *0.0
3-01-870-10 - Sulfuric Acid: Working Loss *0.0
3-01-870-97 - Specify Liquid: Breathing Loss
3-01-870-98 - Specify Liquid: Working Loss
Floating Roof Tanks
3-01-875-01 - Carbon Disulflde: Breathing Loss *0.0
3-01-875-02 - Carbon Disulflde: Working Loss *0.0
3-01-875-97 - Specify Liquid: Breathing Loss
3-01-875-98 - Specify Liquid: Working Loss
Pressure Tanks
3-01-885-01 - Ammonia: Withdrawal Loss
3-01-885-02 - Carbon Monoxide: Withdrawal Loss *0.0 *0.0
3-01-885-03 - Chlorine: Withdrawal Loss *0.0 *0.0
3-01-885-04 - Hydrogen Cyanide: Withdrawal Loss *0.0 *0.0
3-01-885-05 - Sulfur Dioxide: Withdrawal Loss *°-°
3-01-885-99 - Specify Gas: Withdrawal Loss
f
Chemical Manufacturing - Fugitive Emissions
3-01-888-01 - Specify in Comments Field
3-01-888-02 - Specify In Comments Field
3-01-888-03 - Specify In Comments Field
3-01-888-04 - Specify in Comments Field
3-01-888-05 - Specify in Cooments Field
Chemical Manufacturing - Fuel Fired Equipment
Process Heaters
3-01-900-01 - Distillate Oil (No. 2) *144.0 S *20.0
3-01-900-02 - Residual Oil *159.0 S *50.0
3-01-900-03 - Natural Gas *°-6 *140.0
3-01-900-04 - Process Gas *«0.0 S *1*Q-Q
Incinerators
3-01-900-11 - Distillate Oil (No. 2)
3-01-900-12 - Residual Oil
VOC
Lbs/Unit
*0.0
•0.0
•0.0
*0.0
*0.0
*0.0
*0.0
*0.0
•0.0
*0.0
*0.0
*0.0
•0.20
*0.2B
*2.8
*2 8
*n &
"U.I
*0.56
CO
Lbs/Unlt Units
3
10 Gallons Throughput
10 Gallons Storage
Capacity
10 Gallons Throughput
10 Gallons Storage
Capacity
10 Gallons Throughput
10 Gallons Storage
Capacity
10 Gallons Throughput
3
10 Gallons Storage
Capacity
10 Gallons Throughput
10 Gallons Storage
Capacity
10 Gallons Throughput
3
10 Gallons Throughput
10, Gallons Throughput
10, Gallons Throughput
10 Gallons Throughput
10 Gallons Throughput
10 Gallons Throughput
Process Unit-Year
Process Unit-Year
Process Unit-Year
Process Unit-Year
Process Unit-Year
10 Gallons Burned
10 Gallons Burned
10 Cubic Feet Burned
i o Cubic Feet Burned
10 Gallons Burned
10 Gallons Burned
Notes
70
70, 263
70, 263
70, 263
70, 263
70, 263
70, 263
70
70, 263
70, 263
70, 263
70, 263
129
129
129
129
130
130
*Refer to numbered notes In Appendix A or lettered notes In Appendix B: factors without asterisks are from AP-42.
-------
SCO Process
Incinerators (Continued)
3-01-900-13 - Natural Gas
3-01-900-14 - Process Gas
PART SO
Lbs/Unit Lbs/3nit
NO
Lbs/Unlt
VOC
Lbs/Untt
*5.6
•5.6
CO
Lbs/Unlt Units
10 Cubic Feet Burned
10 Cubic Feet Burned
Notes
130
130
Waste Gas Flares
3-01-900-99 - General
Chemical Manufacturing - Other Hot Classified
3-01-999-98 - Specify in Comment*
3-01-999-99 - Specify in Comments
FOOD AND AGRICULTURE - MAJOR GROUPS 01. 02. 07. 20. 21. 42. 44 AND 51°
*5.6
Alfalfa Dehydrating - 2048
3-02-001-02 - Primary Cyclone and Dryer 10.0
3-02-001-03 - Meal Collector Cyclone 2.6
3-02-001-04 - Pellet Cooler Cyclone 3.0
Coffee Roasting - 2095
3-02-002-01 - Direct Fired Roaster 7.6
^ 3-02-002-02 - Indirect Fired Roaster 4.2
CO 3-02-002-03 - Stoner/Cooler 1.4
3-02-002-99 - Other Not Classified (Specify
in Comments)
Instant Coffee Products - 2095
3-02-003-01 - Spray Dryer 1.4
Cotton Ginning - 0724
3-02-004-01 - Unloading Fan 5.0
3-02-004-02 - Seed Cotton Cleaning System 0.3
3-02-004-03 - Stick/Burr Machine 0.2
3-02-004-04 - Miscellaneous (Lint Cleaner/ 1.5
Battery Condensers/Master Trash/
Overflow/Mote Fans)
3-02-004-10 - General (Entire Process, 7.0
Alternative to Above)
0.0
0.0
0.0
*0.4
*0.4
*NEC
0.0
0.0
0.0
0.0
0.0
0.0
0.0
0.0
0.1
0.1
0.0
0.0
0.0
0.0
0.0
0.0
0.0
0.0
0.0
*2.6
*2.6
•HEG
*HEG
0.0
0.0
0.0
0.0
0.0
10 Cubic Feet Burned
10 Gallons Produced
Tons Produced
314
0.0 Tons Product
0.0 Tons Product
0.0 Tons Product
Tons Green Beans
Tons Green Beans
Tons Green Beans
Tons Product
Tons Green Beans
0.0 Bales of Cotton
0.0 Bales of Cotton
0.0 Bales of Cotton
0.0 Bales of Cotton
0.0 Bales of Cotton
240
240
319
285
Feed and Grain Terminal Elevators - 5153. 4221. 4463
3-02-005-03
3-02-005-04
3-02-005-05
3-02-005-06
3-02-005-07
3-02-005-08
- Cleaning
- Drying
- Unloading (Receiving)
- Loading (Shipping)
- Removal from Bins (Tunnel Belt)
- Elevator Legs (Beadhouse)
3.
1.
1.
0.
1.
1.
0
1
0
3
4
5
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
Tons
Tons
Tons
Tons
Tons
Tons
Grain
Grain
Grain
Grain
Grain
Grain
Processed
Processed
Processed
Processed
Processed
Processed
*Refer to numbered notes in Appendix A or lettered notes in Appendix B; factors without asterisks are from AP-42.
-------
sec
Process
PART
Lbs/Unlt
SO
Lbs/Unit
HO
Lbs/Unlt
VOC
Lbs/Unlt
CO
Lbs/Unic
Units
Notes
Feed and Grain Terminal Elevators - 5153. 4221. 4463 (Continued)
3-02-005-09 - Tripper (Gallery Belt) 1.0
3-02-005-10 - Removal from Bins (Tunnel Belt) 2.8
3-02-005-11 - Elevator Legs (Beadhouse)
3-02-005-12 - Country Elevators: General
4.5
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 Tons Grain Processed
0.0 Tons Grain Shipped
or Received
0.0 Tons Grain Shipped
or Received
0.0 Tons Grain Shipped
or Received
Feed and Grain Country Elevators - 5153. 4221
3-02-006-03
3-02-006-04
3-02-006-05
3-02-006-06
3-02-006-07
3-02-006-08
3-02-006-09
Cleaning
Drying
Unloading
Loading
Removal from Bins
Elevator Legs
Removal from Bins
CT>
3-02-006-10 - Elevator Legs
3-02-006-11 - Country Elevators: General
3,
0,
0.
0,
1.
1.
2.
4.
.0
.7
.6
.3
,0
,5
1
7
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
.0
.0
.0
.0
.0
.0
0
0
0
0
0
0
0
0
0
.0
.0
.0
.0
.0
.0
.0
.0
.0
Tons Grain Processed
Tons Grain Processed
Tons Grain Processed
Tons Grain Processed
Tons Grain Processed
Tons Grain Processed
Tons Grain Shipped
or Received
Tons Grain Shipped
or Received
Tons Grain Shipped
or Received
BarleT Milling - 2041
3-02-007-03 - Barley Cleaning
3-02-007-05 - Barley Flour Hill
Milo Milling - 2041
3-02-007-04 - Milo Cleaning
Drum Mills - 2041
3-02-007-11 - Grain Receiving
3-02-007-12 - Precleanlng/Bandllng
3-02-007-13 - Cleaning Bouae
3-02-007-14 - Millhouse
0.2
3.0
0.4
1.0
5.0
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 Tons Grain Processed
0.0 Tons Grain Processed
0.0 Tons Grain Processed
0.0 Tons Grain Processed
0.0 Tons Grain Processed
0.0 Tons Grain Processed
0.0 Tons Grain Processed
Rye Milling - 2041
3-02-007-21
3-02-007-22
3-02-007-23
3-02-007-24
Grain Receiving
Precleanlng/Bandllng
Cleaning Bouae
Millhouse
1.0
5.0
70.0 P
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 Tons Grain Processed
0.0 Tons Grain Processed
0.0 Tons Grain Processed
0.0 Tons Grain Processed
Wheat Mills - 2041
3-02-007-31
3-02-007-32
Grain Receiving
Precleaning/Bandling
1.0
5.0
0.0
0.0
0.0
0.0
0.0
0.0
0.0
0.0
Tons Grain Processed
Tons Grain Processed
-------
sec
Wheat Mills -
3-02-007-33 -
3-02-007-34 -
Process
2041 (Continued)
Cleaning House
Millhouse
PART
Lbs/Unit
70
.0 P
SO
Lbs/Unit
0.
0.
0
0
NO
Lbs/Unit
0.0
0.0
voc
Lbs/Unit
0.
0.
0
0
CO
Lbs/Unit
0.0
0.0
Tons
Tons
Units Notes
Grain Processed
Grain Processed
Dry Corn Milling - 2041
3-02-007-41 -
3-02-007-42 -
3-02-007-43 -
3-02-007-44 -
3-02-007-45 -
Grain Receiving
Grain Drying
Precl caning /Handl Ing
Cleaning House
Degcralng and Milling
1
0
5
6
.0
.5
.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
Tons
Tons
Tons
Tons
Tons
Grain Received
Grain Received
Grain Received
Grain Received
Grain Received
Corn Wet Mill Ins - 2046
3-02-007-51 -
3-02-007-52 -
3-02-007-53 -
3-02-007-54 -
3-02-007-55 -
3-02-007-56 -
Oat Mil Una -
3-02-007-60 -
CT>
Ul
Rice Mi 11 In*
3-02-007-71 -
3-02-007-72 -
3-02-007-73 -
3-02-007-74 -
Soybean Mills
3-02-007-81 -
3-02-007-82 -
3-02-007-83 -
3-02-007-84 -
3-02-007-85 -
3-02-007-86 -
3-02-007-87 -
3-02-007-88 -
3-02-007-89 -
3-02-007-90 -
3-02-007-91 -
Grain Receiving
Grain Handling
Grain Cleaning
Dryers
Bulk Loading
Milling
2041
General
'
- 2044
Grain Receiving
Precleaning/Handl ing
Drying
Cleaning and Millhouse
- 2075. 2041
Grain Receiving
Grain Handling
Grain Cleaning
Drying
Cracking and Dehulllng
Hull Grinding
Bean Conditioning
Flaking
Meal Dryer
Meal Cooler
Bulk Loading
1
5
6
0
5
0
1
5
7
3
2
0
0
1
1
0
.0
.0
.0
.64
.0
.3
.6
.0
.2
.3
.0
.1
.57
.5
.8
.27
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
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.
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
Feed Manufacture - 2082
3-02-008-02 -
3-02-008-03 -
3-02-008-04 -
Grain Receiving
Shipping
Handling
1
0
3
.3
.5
.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
0.0
0.0
0.0
0.0
0.0
0.0
0.0
0.0
0.0
0.0
0.0
Tons
Tons
Tons
Tons
Tons
Tons
Tons
Tons
Tons
Tons
Tons
Tons
Tons
Tons
Tons
Tons
Tons
Tons
Tons
Tons
Tons
Tons
Tons
Tons
Tons
Grain Received
Grain Received
Grain Received
Grain Received
Grain Received
Grain Received
Grain Received
Grain Received
Grain Received
Grain Received 298
Grain Received
Grain Received
Grain Received
Grain Received
Grain Received
Grain Received
Grain Received
Grain Received
Grain Received
Grain Received
Grain Received
Grain Received
Grain Received
Grain Received
Grain Received
-------
SCC Process
Feed Manufacture - 2082 (Continued)
3-02-008-05 - Grinding
3-02-008-06 - Pellet Coolers
Beer Production - 2082
3-02-009-01 - Grain Handling
3-02-009-02 - Drying Spent Grains
3-02-009-03 - Brewing
3-02-009-04 - Aging
3-02-009-05 - Malt Dryer
Whiskey Fermentation - 2085
3-02-010-01 - Grain Handling
3-02-010-02 - Drying Spent Grains
3-02-010-03 - Aging
3-02-010-04 - Fermentation Tank
Wines. Brandy, and Brandy Soirits - 2084
3-02-011-03 - Aging
3-02-011-04 - Fermentation: Tank
3-02-011-05 - Fermentation at 52 F
3-02-011-06 - Fermentation at 80 F
3-02-011-99 - Other Not Classified (Specify
in Comments)
Fish Processing - 2077. 2091
3-02-012-01 - Cooker-Fresh Fish Scrap
3-02-012-02 - Cookers-Stale Fish Scrap
3-02-012-04 - Canning Cookers
3-02-012-05 - Steam Tube Dry«r
3-02-012-06 - Direct Fire Dryer
Meat Smokehouses - 2012. 2013
3-02-013-01 - Combined Operations
Starch Manufacturing - 2036
3-02-014-01 - Combined Operations
Sugar Cane Processing - 2061. 2062
PART
Lbs/Unit
3.0
5.0
0.0
0.045
3.0
5.0
0.0
0.0
0.0
0.0
0.0
0.0
5.0
8.0
0.3
8.0
SO HO VOC
Lbs/Unit Lbs/Unit Lbs/Unlt
0.0 0.0 0.0
0.0 0.0 0.0
0.0 0.0 0.0
2.6
0.0
0.0 0.0 0.0
0.0
0.0 0.0 0.0
•2.6
10.0
*3
0.0 0.0 *0.0
*3
1.06
4.79
0.3
3.5
*1.5
*3.5
*6.5
*1.0 *0.7 0.07
*120 *250
CO
Lbs/Unit Units
0.0 Tons Grain Received
0.0 Tons Grain Received
0.0 Tons Grain Processed
Tons Grain Processed
10 Gallons
0.0 Barrel-Year of Stored
Product
Tons Grain Dried
0.0 Tons Grain Processed
Tons Grain Processed
Barrels (50 Gallon)
10 Gallons Produced
0.0 Barrel-Year of Stored
Product
10 Gallons Produced
10 Gallons Produced
10 Gallons Produced
Gallons Produced
Tons Fish Processed
Tons Fish Processed
Tons Fish Processed
Tons Fish Scrap
Tons Fish Scrap
0.6 Tons Meat Smoked
Tons Starch Produced
Notes
202
202
202
202
163
126
126
122, 141
141, 143
3-02-015-99 - Other Not Classified (Specify
in Comments)
Tons Sugar Produced
*Refer to numbered notes in Appendix A or lettered notes in Appendix B; factors without asterisks are from AP-42.
-------
sec
Process
PART
Lbs/Unlt
SO
Lbs/Onlt
NO
Lbs/finlt
VOC
Lbs/Unlt
CO
Lbs/Unit
Units
Notes
Sugar Beet Processing - 2063
3-02-016-01 - Dryer *0.41 *0.06
3-02-016-99 - Other Not Classified (Specify
in Commenti)
Peanut Processing - 2076. 2079. 2099
3-02-017-99 - Other Not Classified (Specify *0.06
in Comments)
Candy Manufacturing - 2065. 2066
3-02-018-99 - Other Not Classified (Specify
in Comments)
Vegetable Oil Processing - Specific Products/General - 2046. 2074. 2076. 2079
3-02-019-04 - Coconut Oil: General (2076)
3-02-019-06 - Corn Oil: General (2046)
3-02-019-07 - Cottonseed Oil: General (2074)
3-02-019-08 - Soybean Oil: General (2075)
3-02-019-09 - Peanut Oil: General (2076)
Vegetable Oil Processing - General Processes for All Products - 2046. 2074. 2076. 2079
3-02-019-16 - Oil Extraction *NEG *NEG
3-02-019-17 - Meal Preparation
3-02-019-18 - Oil Refining
3-02-019-19 - Fugitive Leaks
3-02-019-20 - Solvent Storage
*0.2
Beef Cattle Feed Lots - 0211
3-02-020-01 - Feed Lots - General
3-02-020-02 - Feed Lots - General
Poultry and E»» Production
3-02-021-01 - Manure Handling: Dry
3-02-021-02 - Manure Handling: Dry
3-02-021-05 - Manure Handling: Net
3-02-021-06 - Manure Handling: Wet
102.2
54.0
*19.0
*18.0
*16.0
*21.0
*17.0
*1.6
*0.7
*1.7
•0.15
*NEG
*NEG
*NEG
*NEG
Tons Raw Beets 264, 329
Tons Raw Beets
Tons Processed 149
Tons Product
Tons Refined Oil Produced
Ton Extractor Feed Cake SS
Ton Extractor Feed Cake 55
Ton Extractor Feed Cake 55
Ton Extractor Feed Cake 55
Ton Extractor Feed Cake 56, 316
Ton Extractor Feed Cake 56
Ton Extractor Feed Cake 56
Ton Extractor Feed Cake 56
Ton Raw Seed Processed 56
Head of Cattle Capacity
Head of Cattle Throughput
Number of Chickens 61
Capacity
Number of Chickens 61
Throughput
Number of Chickens 61
Capacity
Nixnber of Chickens 61
Throughput
Cotton Seed Delint Ing - 0723
3-02-022-01 - Acid Delinting of Cotton Seeds
Seed Production and Processing - 0180. 3191
3-02-026-01 - Seed Handling - General
*NEG
*NEG
*NEG
Tons Cotton Seed Dellnted
Tons Processed 308
Refer to numbered notes in Appendix A or lettered notes in Appendix B; factors without asterisks are from AP-42.
-------
CT>
CO
SCC Process
Mushroom Growing
3-02-028-01 - General
Dairy Products - 2021. 2022. 2023. 2024. 2026
3-02-030-01 - Milk Spray-Dryer
3-02-030-99 - Other Hot Classified (Specify
In Comments)
Export Grain Elevators - 4463. 4221°
3-02-031-03 - Cleaning
3-02-031-04 - Drying
3-02-031-05 - Unloading
3-02-031-06 - Loading
3-02-031-07 - Removal from Bins (Tunnel Belt)
3-02-031-08 - Elevator Legs
3-02-031-09 - Tripper (Gallery Belt)
3-02-031-10 - Removal from Bins (Tunnel Belt)
3-02-031-11 - Elevator Legs
PART
Lbs/Unlt
3.0
1.1
1.0
1.0
1.4
1.5
1.0
1.7
3.3
SO
Lbs/unit
0.0
0.0
0.0
0.0
0.0
0.0
0.0
0.0
0.0
0.0
NO
Lbs/unit
0.0
0.0
0.0
0.0
0.0
0.0
0.0
0.0
0.0
voc
Lbs/Unlt
0.0
0.0
0.0
0.0
0.0
0.0
0.0
0.0
0.0
CO
Lbs/Unlt
0.0
0.0
0.0
0.0
0.0
0.0
0.0
0.0
0.0
Units Notes
Tons Produced
Tons Product
Tons Product
Tons Grain Processed
Tons Grain Processed
Tons Grain Processed
Tons Grain Processed
Tons Grain Processed
Tons Grain Processed
Tons Grain Processed
Tons Grain Shipped or
Received
Tons Grain Shipped or
Received
Bakeries - 2051. 2052
3-02-032-01 - Bread Baking: Sponge-Dough
Process
3-02-032-02 - Bread Baking: Straight-Dough
Process
3-02-032-99 - Other Not Classified (Specify
in Comments)
Tobacco Processing - 2111. 2121. 2131. 2141
3-02-033-99 - Other Not Classified (Specify
in Comments)
Deep Fat Frying - 2099. 2017. 2051. 2092
3-02-036-01 - Cooking Vats: General
Animal/Poultry Rendering
3-02-038-01 - General
Food and Agriculture - Fugitive Emissions
3-G2-855-G1 - Specify in Comments Field*
3-02-888-02 - Specify in Comments Field!
0.0
0.0
0.0
0.0
0.0
0.0
*0.48
*NEG
*NEG
13.0
1.0
*0.34
*18.5
0.0 Tons of Bread Baked
0.0 Tons of Bread Baked
Tons Product
Tons Product
Tons Processed
Tons Processed
rrocess unit-Year
Process Unit-Year
120
142, 316
Note that fugitive emissions are reported in units of Ibs/process unit-year rather than Ibs/ton product as in the NEDS Source Classification Codes
and Emission Factor Listing dated October 1985.
it
Refer to numbered notes in Appendix A or lettered notes in Appendix B; factors without asterisks are from AP-42.
-------
cn
PART SO NO
SCC Process Lbs/Unit Lbs/finlt Lbs/finit
Food and Agriculture - Fugitive Emissions (Continued)
3-02-888-03 - Specify in Comments Field*
3-02-888-04 - Specify in Comments Field*
3-02-888-05 - Specify in Comments Field*
Food and Agriculture - Fuel Fired Eauinnent
Process Heaters
3-02-900-01 - Distillate Oil (No. 2) *144.0 S *20 . 0
3-02-900-02 - Residual Oil "159.0 S *55.0
3-02-900-03 - Natural Gas *0.6 *140.0
Food and Agriculture - Other Not Classified
3-02-999-98 - Specify in Comments
3-02-999-99 - Specify in Comments
PRIMARY METAL PRODUCTION - MAJOR GROUPS 10 AHD 33
Aluminum Ore - Bauxite - 1051
3-03-000-01 - Crushing/Handling 6.0 0.0 0.0
3-03-000-02 - Drying Oven 1.2 *1.4
Aluminum Ore: Electro-Reduction - 3334
3-03-001-01 - Prebaked Reduction Cell 94.0 *57.3 *0.003
3-03-001-02 - Horizontal Stud Soderberg Cell 98.0 "10.0
3-03-001-03 - Vertical Stud Soderberg 78.0 *17.Qd
3-03-001-04 - Materials Handling 10.0 *0.0 *0.0
3-03-001-05 - Anode Baking Furnace 3.0 "2.7
3-03-001-06 - Degassing 0.0 0.0
3-03-001-07 - Roof Vents
3-03-001-08 - Prebake: Fugitive Emissions 5.0
3-03-001-09 - H.S.S.: Fugitive Emissions 10.0
VOC
Lbs/Unit
*0.20
*0.28
*2.8
0.0
*0.004
*0.1
*1.0
*1.0
*0.0
*1.0
0.0
*2.7
*NEG
*NEG
CO
Lbs/Unit Units
Process Unit-Year
Process Unit-Year
Process Unit-Year
10 Gallons Burned
10, Gallons Burned
10 Cubic Feet Burned
Tons Processed (Input)
Tons Produced (Finished)
0.0 Tons of Ore
Tons of Ore
d
*369.0 Tons of Molten Aluminum
Produced
"244.0 Tons of Molten Aluminum
Produced
"349.0 Tons of Molten Aluminum
Produced
Tons of Molten Aluminum
Produced
*66.0 Tons of Molten Aluminum
Produced
0.0 Tons of Molten Aluminum
Produced
Tons of Molten Aluminum
Produced
Tons of Molten Aluminum
Produced
Tons of Molten Aluminum
Produced
Notes
129
129
129
60, 176
274, 298
367
298, 367
298, 367
170
181
54
199
199
Note that fugitive emissions are reported in units of ibs/process unit-year rather than Ibs/ton product as In the NEDS Source Classification Codes
and Emission Factor Listing dated October 1985.
*
Refer to numbered notes in Appendix A or lettered notes in Appendix B; factors without asterisks are from AP-42.
-------
sec
Process
PART
Lbs/Unit
SO
Lbs/finlt
NO
Lbs/Unit
VOC
Lbs/Unit
CO
Lbs/Unit
Units
Notes
Aluminum Ore: Electro-Reduction - 333* (Continued)
3-03-001-10 - V.S.S.: Fugitive Emissions
3-03-001-11 - Anode Baking: Fugitive Emissions
12.0
*NEG
*NEG
Tons of Molten Aluminum 199
Produced
Tons of Molten Aluminum 199
Produced
Aluminum Hydroxide Calcining - 333*
3-03-002-01
By-Product
3-03-003-02
3-03-003-03
3-03-003-04
3-03-003-05
3-03-003-06
3-03-003-07
3-03-003-08
3-03-003-09
3-03-003-10
3-03-003-11
3-03-003-12
3-03-003-13
3-03-003-14
3-03-003-15
3-03-003-16
3-03-004-01
- Overall Process
Coke Manufacturing - 3312
- Oven Charging
- Oven Pushing
- Quenching
- Coal Unloading
- Oven Underfirlng
- Coal Crushing /Handling
- Oven/ Door Leaks
- Coal Conveying
- Coal Crushing
- Coal Screening
- Coke Crushing/Screening/Handling
- Coal Preheater
- Topside Leaks
- Gas By-Product Plant
- Coal Storage Pile
- General
200
0
1
5
0
0
0
0
*0
3
*0
200
.0
.48
.15
.24
.00011
.58
.51
.11
J
.09*
•5 .
.09d
.0
*27.
0.
*3.
*0.
0.
4.
0.
*0.
0.
0.
0.
0.
*0.
0.
0.
8
02
3
4
0
0
0
1
0
0
0
0
1
0
0
*1
0
*0
*0
0
*0
0
0
0
0
0
0
*0
0
0
.5
.03
.03
.6
.0
.04
.0
.01
.0
.0
.0
.0
.01
.0
.0
*0
2
0
*0
0
*2
0
1
0
0
0
0
*0
*1
0
0
8
.02
.5
.2
.02
.0
.0
.0
.5
.0
.0
.0
.0
.3
.5
.0
.0
.0
Primary Coooer Smelters - 3331
3-03-005-02
3-03-005-03
3-03-005-04
3-03-005-05
3-Q3-QQ5-Q£
3-03-005-07
- Multiple Hearth Roaster
- Reverberatory Smelting Furnace
after Roaster
- Converter (All Configurations)
- Fire (Furnace) Refining
- Ore Concentrate Dryer
- Reverberatory Smelting Furnace
with Ore Charging (without
Roasting)
45
50
36
10
10
50
.0
.0
.0
.0
ft
.0
280.
180.
623.
0.
^
320.
0
0
o1
0
ft
0
*3
•5
.6
.8
*NEG
*0
*0
.009
.015
*NEG
*NEG
*10
.3
*3
*0
.004
.03
Tons of Alumina Produced
0.6 Tons Coal Charged
0.07 Tons Coal Charged 135,
Tons Coal Charged
0.0 Tons Coal Charged
Tons Coal Charged
0.0 Tons Coal Charged
0.6 Tons Coal Charged
0.0 Tons Coal Processed
0.0 Tons Coal Processed
0.0 Tons Coal Processed
0.0 Tons Coke Processed
Tons Coal Charged
Tons Coal Charged
10 Cubic Feet Gas
Processed
0.0 Tons Coal Charged
1.0 Tons Coal Charged
Tons Concentrated Ore
Processed
Tons Concentrated Ore
Processed
Tons Concentrated Ore
Processed
Tons Concentrated Ore
Processed
Tons Concentrated Ore
Processed
Tons Concentrated Ore
Processed
208, 250
298, 301
298, 301
102, 298
131, 136
94, 301
298
57, 298
357
228
228, 299
58, 275
58
bU
228
*Refer to numbered notes in Appendix A or lettered notes in Appendix B; iactors without asterisks are from AP-42.
-------
sec
Process
PART SO HO
Lbs/Unit Lbs/unit Lbs/Onlt
voc
Lbs/Unit
CO
Lbs/Unit Units
Notes
Primary Cooper Smelters - 3331 (Continued)
3-03-005-08
3-03-005-09
3-03-005-10
3-03-005-11
3-03-005-12
3-03-005-13
3-03-005-1*
3-03-005-15
3-03-005-16
3-03-005-17
3-03-005-18
3-03-005-21
3-03-005-22
3-03-005-23
3-03-005-24
3-03-005-25
3-03-005-26
3-03-005-27
3-03-005-28
3-03-005-99
- Refined Metal Finishing
Operations
- Fluidized-Bed Roaster
- Electric Sow It ing Furnace
- Electrolytic Refining
- Flash Smelting
- Roasting: Fugitive Emissions
- Reverberatory Furnace: Fugitive
Emissions
- Converter: Fugitive Emissions
- Anode Refining Furnace: Fugitive
Emissions
- Slag Cleaning Furnace: Fugitive
Emissions
- Converter Slag Return: Fugitive
Emissions
- Noranda Reactor
- Slag Cleaning Furnace
- Reverberatory Furnace with
Converter
- Multi-Hearth Roaster with
Reverberatory Furnace and
Converter or Fluid Bed Roaster
with Electric Furnace with
Converter
- Fluid Bed Roaster with
Reverberatory Furnace and
Converter
- Dryer with Electric Furnace and
Cleaning Furnace and Converter
- Dryer with Flash Furnace and
Converter
- Horanda Reactor and Converter
- Other Hot Classified (Specify
in Comments)
*0
360
100.0 240
0
140.0 820
2.6 1
0.4 4
4.4 130
0.5 0
8.0 6
0
10.0 1
36.0 740
36.0 600
36.0 540
36.0 820
240
.0 *0.0
.0
.0
.0 *0.0
.0
.0
.0
.0
.1
.0
.1
.0
.0
.0
.0
.0
.0
*0.0
*HEG
*NEG
*0.0
*NEG
*NEC
*NEG
*NEG
*HEG
*NEG
*NEC
*NEG
*HEG
*NEG
*NEG
*NEG
*NEG
*HEG
*NEG
Tons Concentrated
Processed
Tons Concentrated
Processed
Tons Concentrated
Processed
Tons Concentrated
Processed
Tons Concentrated
Processed
Tons Concentrated
Processed
Tons Concentrated
Processed
Tons Concentrated
Processed
Tons Concentrated
Processed
Tons Concentrated
Processed
Tons Concentrated
Processed
Tons Concentrated
Processed
Tons Concentrated
Processed
Tons Concentrated
Processed
Tons Concentrated
Processed
Tons Concentrated
Processed
Tons Concentrated
Processed
Tons Concentrated
Processed
Tons Concentrated
Processed
Tons Concentrated
Processed
Ore
Ore
Ore
Ore
Ore
Ore
Ore
Ore
Ore
Ore
Ore
Ore
Ore
Ore
Ore
Ore
Ore
Ore
Ore
Ore
353
58
58
182
58
58
58
58
58
58
58
58
58
58
58
58
58
58
58
*Refer to numbered notes In Appendix A or lettered notes In Appendix B; factors without asterisks are from AP-42.
-------
PART SO
SCC Process Lbs/Unit Lbs/Unit
Ferroalloy (Open Furnace) - 3313
3-03-006-01 - SOX FeSl: Electric Smelting 70.0 *0.07
Furnaces
3-03-006-02 - 75X FeSi: Electric Smelting 316.0 *0.07
Furnaces
3-03-006-03 - 90X FeSl: Electric Smelting 564.0 *0.07
Furnaces
3-03-006-04 - Silicon Metal: Electric 872.0 *0.07
Smelting Furnaces
3-03-006-05 - Siliconmanganese: Electric 192.0 0.07
Smelting Furnaces
3-03-006-10 - Ore Screening
3-03-006-11 - Ore Dryer
3-03-006-13 - Raw Materials Storage
3-03-006-14 - Raw Materials Transfer
3-03-006-15 - Ferromanganese: Blast Furnace
3-03-006-16 - Ferrosllicon: Blast Furnace
3-03-006-17 - Cast Bouse
3-03-006-99 - Other Not Classified (Specify
in Comments)
Ferroalloy (Semi-Covered Furnace) - 3313
3-03-007-01 - Ferromanganese: Electric Arc 12.0 0.02
Furnace
3-03-007-02 - Electric Arc Furnace (Other
Alloys Specify in Comments)
3-03-007-03 - Ferrochromium - Electric Arc
3-03-007-04 - Ferrochromium Silicon - Electric
Arc Furnace
Iron Production - 3312
3-03-008-01 - Blast Furnace: Ore Charge *110.0° 0.0
3-03-008-02 - Blast Furnace: Agglomerates *40.0° 0.0
Charge
Blast Furnace Slag
3-03-008-04 - Loader: Hi-Silt *0.026 0.0
3-03-008-05 - Loader: Lo-Silt "0.0088 0.0
3-03-008-08 - Slag Crushing and Sizing *0.0
3-03-008-09 - Slag Removal and Dumping *0.0
Sintering - 3312
3-03-008-11 - Raw Material Stockpiles, Coke
Breeze, Limestone, Ore Fines
3-03-008-12 - Raw Material Transfer/Handling
NO VOC CO
Lbs/unit Lbs/Unit Lbs/Unlt
*0.1 4.5
*0.1 *4.5
*0.1 *4.5
*0.1 72
*0.1 *4.5
*0.0
•0.004
*0.0
*0.0
•16
•16
*2.8
•0.1 1.4
•8.2
•8.2
0.0 0.0 *l,750.0C>t
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
*4.8
*0.0
Units
Tons Produced
Tons Produced
Tons Produced
Tons Produced
Tons Produced
Tons Processed
Tons Processed
Tons Processed
Tons Processed
Tons Produced
Tons Produced
Tons Produced
Tons Produced
Tons Produced
Tons Produced
Tons Produced
Tons Produced
Tons Iron Produced
Tons Iron Produced
Tons Slag Transferred
Tons Slag Transferred
Tons Processed
Tons Processed
Tons Sinter Produced
Tons Sinter Produced
Notes
298, 301
352, 360
298, 352,
354, 360
298, 352,
354, 360
298, 301
352, 360
298, 299,
354, 360
186
60
186
186
59
355
356
298, 299,
301, 360
59
59
191
191
57
195
Refer to numbered notes in Appendix A or lettered notes in Appendix B; factors without asterisks are from AP-42.
-------
sec
Sintering -
3-03-008-13
3-03-008-14
3-03-008-15
3-03-008-16
3-03-008-17
3-03-008-18
3-03-008-19
3-03-008-20
3-03-008-21
3-03-008-22
3-03-008-23
3-03-008-24
3-03-008-25
3-03-008-26
3-03-008-27
CO
Process
3312 (Continued)
- Windbox
- Sinter Discharge End
- Sinter Breaker
- Sinter Hot Screening
- Sinter Cooler
- Sinter Cold Screening
- Sinter Processing (Combined Code
Includes 15, 16, 17, 18)
- Sinter Conveyor: Transfer Station
- Unloading Ore, Pellets, Limestone
Into Blast Furnace
- Blast Furnace Raw Materials
Stockpiles: Ore, Pellets,
Limestone, Coke, Sinter
- Blast Furnace Charge Materials
Transfer/Handling
- Blast Heating Stoves
- Cast House
- Blast Furnace Slips
- Lump Ore Unloading
PART
Lbs/Unit
11
6
*3
*0
*0
*0
0
87
*0
.1
.8
A
.od
J
.8d
j
.026
.0024
.6
•0
.0003
SO
Lbs/unit
*2
.5*
*NEG
*0
*0
*0
0
0
*3
0
.0
.14
.0
.0
.0
.0
.0
NO
Lbs/unit
.0.3d
•NEC
*0.0
*NEG
*0.0
0.0
0.0
*0.03
0.0
VOC
Lbs/Unit
*1
.4d
•0.0
*0
*0
.0
.0
*NEG
*0
*0
0
0
*4
*0
*o
*2
*0
0
.0
.05
.0
.0
.8
.0
.01
.8
.0
.0
CO
Lbs/Unit
44.0 Tons
Tons
Tons
Tons
Tons
Tons
Tons
0 . 0 Tons
0 . 0 Tons
Tons
Tons
Tons
Tons
Units
Sinter Produced
Sinter Produced
Sinter Produced
Sinter Produced
Sinter Produced
Sinter Produced
Sinter Produced
Sinter Transferred
Ore Transferred
Processed
Processed
Processed
Processed
Number of Slips
0 . 0 Tons
Ore Transferred
Notes
254, 307
254
191
97, 309
191
95
198
195
252
343
241
Punitive Emissions : Roads
3-03-008-31
3-03-008-32
3-03-008-33
3-03-008-34
- Unpaved Roads: LDV
- Unpaved Roads: MDV
- Unpaved Roads: HDV
- Paved Roads: All
1
7
14
0
.8
.3
.0
.78
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 Vehicle-Miles Traveled
0.0 Vehicle-Miles Traveled
0.0 Vehicle-Miles Traveled
0.0 Vehicle-Miles Traveled
Steel Production - 3312
3-03-009-01
3-03-009-04
3-03-009-06
3-03-009-07
3-03-009-08
3-03-009-10
3-03-009-11
3-03-009-12
3-03-009-13
3-03-009-14
3-03-009-15
- Open Hearth Furnace: Stack
- Electric Arc Furnace: Stack
(Alloy Steel)
- Charging: EAP
- Tapping: EAF
- Electric Arc Furnace: Stack
(Carbon Steel)
- Pickling
- Soaking Pits
- Grinding
- Basic Oxygen Furnace: Open
Hood-Stack
- Basic Oxygen Furnace: Closed
Hood-Stack
- Hot Metal (Iron) Transfer to
Steelmaklng Furnace
21
11
50
.1
.3
.0
*1
*0
*0
*0
.4
.7
.7
.0
*HEG
28
28
0
.5
.5
.19
*0
.0
•0.1
*0.1
•0.0
•NEC
*0.0
"0.08
*0
*0
*0
*0
*0
*0
*0
*0
•0
*0
*0
.17
.35
.001
.002
.35
.0
.02
.0
.001
.001
.001
Tons
18 . 0 Tons
Tons
Tons
18.0 Tons
Tons
Tons
Tons
139. 0U Tons
139.0U Tons
Tons
Produced
Produced
Produced
Produced
Produced
Produced
Produced
Produced
Produced
Produced
Produced
57, 94
57, 93
188
243
57, 253
183
144, 276
191
57, 96
57
188
*Refer to numbered notes In Appendix A or lettered notes in Appendix Bi factors without asterisks are from AP-42.
-------
sec
Process
PART SO NO
Lbs/Unit Lbs/Dnit Lbs/unit
voc
Lbs/Unit
CO
Lbs/Unit Units
Notes
Steel Production - 3312 (Continued)
3-03-009-16 -
3-03-009-17 -
3-03-009-18 -
3-03-009-19 -
3-03-009-21 -
3-03-009-22 -
3-03-009-23 -
3-03-009-2* -
3-03-009-25 -
3-03-009-31 -
3-03-009-32 -
3-03-009-33 -
3-03-009-3* -
3-03-009-35 -
3-03-009-36 -
3-03-009-98 -
3-03-009-99 -
Lead Smelters
3-03-010-01 -
3-03-010-02 -
3-03-010-03 -
3-03-010-0* -
3-03-010-05 -
3-03-010-06 -
3-03-010-07 -
3-03-010-08 -
3-03-010-09 -
3-03-010-10 -
3-03-010-11 -
3-03-010-12 -
3-03-010-13 -
3-03-010-14 -
3-03-010-15 -
Charging: BOP
Tapping: BOF
Charging: Open Hearth
Tapping: Open Hearth
Teeming (Unleaded Steel)
Continuous Casting
Steel Furnace Slag Tapping and
Dumping
Steel Furnace Slag Processing,
Crushing and Sizing
Teeming (Leaded Steel)
Hot Rolling
Machine Scarfing
Reheat Furnaces
Heat Treating Furnaces, Annealing
Cold Rolling
Coating (Tin, Zinc, etc.)
Other Not Classified (Specify
in Comments)
Other Not Classified (Specify
in Comments)
- 3332
Sintering: Single Stream
Blast Furnace Operation
Dross Reverberatory Furnace
Ore Crushing
Materials Handling (Includes 11,
12, 13, 04, 14)
Sintering: Dual Stream Feed End
Sintering: Dual Stream Discharge
End
Slag Fume Furnace
Lead Dressing
Crushing and Grinding
Raw Material Unloading
Raw Material Storage Piles
Raw Material Transfer
Sintering Charge Mixing
Sinter Crushing /Screening
0.6
0 . 92 *0 . 02
0.07
•0.05
•0.0 *0.0
0.81
0 . 1 *NEG *NEG
•0.8 *0.8
•0.1
•1.9
106. 5V 275. 0V
180. 5V 22. 5V
20.0 NEC
2.0 0.0 0.0
5.0 *0.0 *0.0
213.0 550.0
4.6 *2.9
0.48 *0.01 *12.8
1.0 *0.0 *0.0
•0.4 *0.0 *0.0
•0.3 *0.0 *0.0
0.5 *0.0 *0.0
2.26
1.5 *0.0 *0.0
•0.001
•0.002
•0.001
•0.002
•0.002
•NEC
•0.002
•0.0
•0.002
•0.08
•NEC
•0.01
•0.004
•0.56
•0.07
•NEC
•NEC
•NEC
0.0
•0.0
•NEC
•NEC
•NEC
•0.03
•0.0
•0.0
•0.0
•0.0
•NEC
•0.0
Tons Produced
Tons Produced
Tons Produced
Tons Produced
Tons Produced
Tons Produced
Tons Produced
Tons Produced
Tons Produced
Tons Produced
Tons Produced
Tons Produced
Tons Produced
Tons Produced
Tons Produced
Tons Produced Each
Tons Produced
Tons of Concentrated Ore
Processed
Tons of Concentrated Ore
Processed
Tons of Concentrated Ore
Processed
0.0 Tons of Ore Crushed
Tons of Lead Product
Tons of Concentrated Ore
Processed
Tons of Concentrated Ore
Processed
Tons of Lead Product
Tons of Lead Product
Tons Processed
Tons of Raw Material
Tons of Raw Material
Tons of Raw Material
Tons of Sinter
Tons of Sinter
57
141, 243
188
243
255
141, 235
243
191
255
57
308
12*
141, 221
57
141, 142
58
58
58, 298,
299
298
191
58, 298,
299
58
58, 189
229
191, 298
191
191
191
58
191
*Refer to numbered notes in Appendix A or lettered notes in Appendix B; factors without asterisks are from AP-42.
-------
in
SCC Process
Lead Smelters - 3332 (Continued)
3-03-010-16 - Sinter Transfer
3-03-010-17 - Sinter Fines Return Handling
3-03-010-18 - Blast Furnace Charging
3-03-010-19 - Blast Furnace Tapping (Metal
and Slag)
3-03-010-20 - Blast Furnace Lead Pouring
3-03-010-21 - Blast Furnace Slag Pouring
3-03-010-22 - Lead Refining/ Silver Retort
Building
3-03-010-23 - Lead Casting
3-03-010-24 - Reverberatory or Kettle Softening
3-03-010-25 - Sinter Machine Leakage
3-03-010-26 - Sinter Dump Area
Molybedenum Ore Mining - 1061
3-03-011-01 - Mining: General
3-03-011-02 - Milling: General
3-03-011-99 - Processing (Specify in Comments)
Titanium Processing - 3339. 3369. 3356
3-03-012-01 - Chlorinatlon
3-03-012-02 - Drying Titanium Sand Ore (Cyclone
Exit)
3-03-012-99 - Other Not Classified (Specify
in Comments)
Gold Processing - 1041. 3341. 3339
3-03-013-01 - Mining/Processing
Barium Ore Processing - 3295
3-03-014-01 - Ore Grinding
3-03-014-02 - Reduction Kiln
3-03-014-03 - Dryers/Calclners
3-03-014-99 - Others Not Classified (Specify
in Comments)
Taconite Iron Ore Processing - 1011
3-03-023-01 - Primary Crushing
3-03-023-02 - Fines Crushing
3-03-023-03 - Ore Screening
3-03-023-04 - Ore Transfer
3-03-023-05 - Ore Storage
3-03-023-06 - Dry Grinding/Milling
3-03-023-07 - Bentonlte Storage
PART SO
Lbs/Unit Lbs/unit
0.2 *0.0
9.0
0.16
0.93
0.47
1.8 *0.0
0.87
3-0
*0 . 68"
*0.01
0.0
0.0
0.5
0.0
*0.0
*0.0
0.2 *0.0
79.8 *0.0
*0.0
0.1 *0.0
*0.0
*0.0
0.04 *0.0
NO
Lbs/unit
*0.0
•0.0
0.0
0.0
0.0
0.0
0.0
*0.42
*0.0
*0.0
*0.0
*0.0
*0.0
•0.0
*0.0
voc
Lbs/Unit
*0.0
*0.0
*0.0
*0.0
*NEC
*NEG
*0.0
*NEG
*NEG
*NEG
*NEG
0.0
0.0
0.0
*0.004
0.0
*0.0
*0.04
*0.004
*0.0
*0.0
*0.0
•0.0
*0.0
*0.0
*0.0
CO
Lbs/Unit Units
Tons of Sinter
Tons of Sinter
Tons of Lead Product
Tons of Lead Product
Tons of Lead Product
Tons of Lead Product
Tons of Lead Product
Tons of Lead Product
Tons of Lead Product
Tons of Sinter
Tons of Sinter
0.0 Hundreds of Tons Mined
0.0 Hundreds of Tons Mined
Hundreds of Tons Mined
0.0 Tons Product
Tons Processed
Tons Processed
0.0 Tons of Ore
Tons Processed
Tons Processed
Tons Processed
Tons Processed
Tons Pellets Produced
Tons Pellets Produced
Tons Pellets Produced
Tons Pellets Produced
Ton* Pellets Produced
Tons Pellets Produced
Tons Pellets Produced
Notes
191
195
195
195
58
58
190
58
58
58
58
60
191
358
60
191
191
191
191
191
191
191
*Refer to numbered notes in Appendix A or lettered notes in Appendix Bi factors without asterisks are from AP-42.
-------
en
sec
Taconite Iron
3-03-023-08 -
3-03-023-09 -
3-03-023-10 -
3-03-023-11 -
3-03-023-12 -
3-03-023-13 -
3-03-023-15 -
3-03-023-16 -
3-03-023-21 -
3-03-023-22 -
Metal Mining
3-03-024-01 -
3-03-024-02 -
3-03-024-03 -
3-03-024-04 -
3-03-024-05 -
3-03-024-06 -
3-03-024-07 -
3-03-024-08 -
3-03-024-09 -
3-03-024-10 -
3-03-024-11 -
Zinc Smelting
3-03-030-02 -
3-03-030-03 -
3-03-030-05 -
3-03-030-06 -
3-03-030-07 -
3-03-030-08 -
3-03-030-09 -
3-03-030-10 -
Process
Ore Processing - 1011 (Continued)
Bentonlte Blending
Traveling Grate Feed
Traveling Grate Discharge
Chip Regrindlng
Indurating Furnace: Gas Fired
Indurating Furnace: Oil Fired
Indurating Furnace: Coal Fired
Pellet Cooler
Pellet Transfer
Haul Road: Rock
Haul Road: Taconite
- General Processes - 1011-1099
Primary Crushing (low moisture
ore)
Secondary Crushing (low moisture
ore)
Tertiary Crushing (low moisture
ore)
Material Handling (low moisture
ore)
Primary Crushing (high moisture
ore)
Secondary Crushing (high moisture
ore)
Tertiary Crushing (high moisture
ore)
Material Handling (high moisture
ore)
Dry Grinding with Air Conveying
Dry Grinding without Air
Conveying, etc.
Ore Drying
- 3333
Multiple Hearth Roaster
Sinter Strand
Vertical Retort/Electrothermal
Furnace
Electrolytic Processor
Flash Roaster
Fluid Bed Roaster
Raw Material Handling and Transfer
Sinter Breaking and Cooling
PART
Lbs/Unit
0.22
0.64
1.32
29.2
29.2
29. 2
3.4
11.0
9.3
0.5
1.2
2.7
0.12*
0.02
0.05
0.06
0.01
28.8
2.4
19. 7y
227.0
90.0
100.0
3.0
2,000.0
2,167.0.
G
*1.5d
SO
Lbs/unlt
*0
*0
*0
•0
0
0
*0
*0
0
0
*0.
*0
*0,
*0.
*0.
*0.
*0.
*0.
*0.
*0.
*0.
1,100.
*0.
*1.
*404.
*223.
0.
0.
.0
.0
.0
.0
.06
.13
f E
. O J
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
0
0
0
0
002
0
65
13
4
5
0
0
NO
Lbs/unlt
*0.
•0.
*0.
*0.
*1.
*0.
*0.
*0.
0.
0.
*0.
*0.
*0.
*0.
*0.
*0.
*0.
*0.
*0.
*0.
*1.
0
0
0
0
6
2
0
0
0
0
0
0
0
0
0
0
0
0
0
0
6
roc
Lbs/Unit
*0
*0
*0
*0
*0
*0
*n
™u
*0
*0
0
0
*0
*0
*0
*0
*0
*0
*0
*0
*0
• 0
*0
0
.0
.0
.0
.0
.004
.003
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.004
.0
*NEG
•NEC
*0.
0.
0.
0
0
0
*0
*0
*0
0
0
.0
.0
.0
.0
.0
CO
Lbs/Unit
Tons
Tons
Tons
Tons
Tons
Tons
Tons
Tons
Tons
Units
Pellets Produced
Pellets Produced
Pellets Produced
Pellets Produced
Pellets Produced
Pellets Produced
Pellets Produced
Pellets Produced
Notes
191
191
191
191
237
237
9^7
^ J /
358
191
0.0 Vehicle-Miles Traveled
0.0 Vehicle-Miles Traveled
Tons
Tons
Tons
Tons
Tons
Tons
Tons
Tons
Tons
Tons
Tons
Tons
Tons
Tons
Tons
Tons
Tons
0 . 0 Tons
0 . 0 Tons
Ore Processed
Ore Processed
Ore Processed
Ore Processed
Ore Processed
Ore Processed
Ore Processed
Ore Processed
Ore Processed
Ore Processed
Ore Processed
Processed
Processed
Processed
Processed
Processed
Processed
Processed
Processed
191
191
191
191
191
191
191
191
191
191
220
298
58, 217
58, 218
222
219, 298
219, 298
*Re£er to numbered notes in Appendix A or lettered notes In Appendix B; factors without asterisks are from AP-42.
-------
sec
Zinc Smelting
3-03-030-11 -
3-03-030-12 -
3-03-030-1* -
3-03-030-15 -
3-03-030-16 -
Primary Metal
PART SO NO
Process Lbs/Unit Lbs/flnit Lbs/Unlt
- 3333 (Continued) .
Zinc Casting *2'5d °'° °'°
Raw Material Unloading *0.* 0.0 0.0
Crushing / Screening 0.0 0.0
Zinc Melting 0.0 0.0
Alloying 0.0 0.0
Industries - Fuel Fired Eou intent
VOC
Lbs/Unit
0.0
0.0
0.0
0.0
0.0
Process Heaters
3-03-900-01 -
3-03-900-02 -
3-03-900-03 -
3-03-900-04 -
Incinerators
3-03-900-11 -
3-03-900-12 -
3-03-900-13 -
3-03-900-1* -
Flares
3-03-900-23 -
3-03-900-2* -
Distillate Oil (Ho. 2) *1*0.0 S *20.0
Residual Oil *159.0 S *55.0
Natural Cas *0.6 * 1*0.0
Process Cas *950.0 S *140.0
Distillate Oil (No. 2)
Residual Oil
Natural Gas
Process Gas
Natural Gas
Process Gas
*0.20
*0.28
*2.8
*2.8
*0.*
*0.56
*5.6
*5.6
*5.6
*5.6
CO
Lbs/Unit Units
0.0 Tons Processed
0.0 Tons Processed
0.0 Tons Processed
0.0 Tons Processed
0.0 Tons Processed
3
10 Gallons Burned
10 Gallons Burned
10 Cubic Feet Burned
10 Cubic Feet Burned
3
10 Gallons Burned
10 Gallons Burned
10 Cubic Feet Burned
10 Cubic Feet Burned
5
10 Cubic Feet Burned
10 Cubic Feet Burned
Notes
129
129
129
129
130
130
130
130
130
130
3-03-888-01 - Specify in Comments Field*
3-03-888-02 - Specify in Comments Field*
3-03-888-03 - Specify In Comments Fieldf
3-03-888-0* - Specify in Comments Fieldf
3-03-888-05 - Specify in Comments Fieldf
Process Unit-Year
Process Unit-Year
Process Unit-Year
Process Unit-Year
3-03-999-99 - Other Not Classified (Specify
in Comments)
SECONDARY METAL PRODUCTION - MAJOR GROUPS 33 AND 34
Secondary Aluminum - 33*1. 3353. 3354. 3355. 3361. 3411, 3497
3-04-001-01
3-04-001-02
3-04-001-03
- Sweating Furnace 14.5 *3.5 *0.6 *2.4
- Smelting Furnace/Crucible 1.9 *2.5 *1.7 *2.5
- Smelting Furnace /Reverberatory 4.3 *0.9 *0.76 *0.2
Tons Produced
Tons Produced 1*9, 150, 197
Tons Metal Produced 344
Tons Metal Produced 122, 144, 145
*Note that fugitive emissions are reported in units of Ibs/process unit-year rather than Ibs/ton product as in the NEDS Source Classification Codes
and Emission Factor Listing dated October 1985.
*Refer to numbered notes In Appendix A or lettered notes in Appendix B; factors without asterisks are from AP-42.
-------
CO
SCC Process
Secondary Aluminum - 3341. 3353. 3354. 3355. 3361,
3-04-001-04 - Fluxing (Chlorination)
3-04-001-05 - Fluxing (Fluoridatlon)
3-04-001-06 - Degassing
3-04-001-07 - Hot Dross Processing
3-04-001-08 - Crushing /Screening
3-04-001-09 - Burning/Drying
3-04-001-10 - Foil Rolling
3-04-001-11 - Foil Converting
3-04-001-12 - Annealing Furnace
3-04-001-13 - Slab Furnace
3-04-001-14 - Pouring/Casting
3-04-001-20 - Can Manufacture
3-04-001-50 - Rolling/Drawing/Extruding
PART
Lbs/Unit
. 3411. 3497
1,000.0
0.22
Secondary CoDDer Smeltinc. and Alloviiut (Brass/Bronze Melt) -
3-04-002-07 - Scrap Dryer (Rotary)
3-04-002-08 - Wire Burning (Incinerator)
3-04-002-09 - Sweating Furnace
Cupolas
3-04-002-10 - Charge with Scrap Copper
3-04-002-11 - Charge with Insulated Copper Wire
3-04-002-12 - Charge with Scrap Copper and Brass
Reverberatory Furnace
3-04-002-14 - Charge with Copper
3-04-002-15 - Charge with Brass and Bronze
Rotary Furnace
3-04-002-17 - Charge with Brass and Bronze
Crucible and Pot Furnaces
3-04-002-19 - Charge with Braas and Bronze
Electric Arc Furnace
3-04-002-20 - Charge with Copper
3-04-002-21 - Charge with Brass and Bronze
Electric Induction Furnace
3-04-002-23 - Charge with Copper
3-04-002-24 - Charge with Brass and Bronze
Fugitive Emissions
3-04-002-30 - Scrap Metal Pretreatment
3-04-002-31 - Scrao Dryer
275.0
275.0*
15.0*
0.0003
230.0
70.0
5.1
36.0
300.0
21.0
5.0
11.0
7.0
20.0
13.75
SO
Lbs/flnit
(Continued)
0.0
*0.0
0.0
0.0
0.0
*3.0
•0 . 002
*0 . 002
*0.02
3341. 3362
*1.5
*12.8
*0.5
*0.03
*0.03
•0.03
*0.0
*0.0
NO
Lbs/flnit
0.0
*0.0
0.0
0.0
0.0
*0.5
•1.5
*1.5
*0.01
•0.7
•0.7
•18
•1.7
•0.08
*0.6
•NEC
•NEC
•0.0
•0.0
VOC
Lbs/Unit
0.0
•0.0
0.0
0.0
0.0
•32
•1.3
•2.4
•0.004
•0.004
•0.14
•300
•0.09
•0.004
•0.6
•0.12
•0.18
•447.0
•0.18
•5.2
•5.2
•2.4
•6.7
•3.9
•NEC
•NEC
•MEG
•0.0
•0.0
CO
Lbs/Unit
0.0
0.0
0.0
0.0
0.0
0.0
0.0
0.0
33.5
Units
Tons of Chlorine Used
Tons Metal Produced
Tons Metal Produced
Tons Metal Produced
Tons Metal Produced
Tons Metal Produced 143,
Tons Produced
Tons Produced
Tons Metal Produced
Tons Metal Produced
Tons Metal Charged
Tons Produced
Tons Produced
Tons of Charge 60,
Tons of Charge
Tons of Charge
Tons of Charge
Tons of Coke-free Charge
Tons of Charge
Tons of Charge
Tons of Charge
Tons of Charge
Tons of Charge
Tons of Charge
Tons of Charge
Tons of Charge
Ions of Charge
Tons of Charge
Tons of Charge
Notes
187
147, 328
143
245
242
242
196
143, 359
143, 145
122, 141
277
207
249
84
249
248
141, 248
147, 247
140
239
193, 361
127
1.Y3, juy
199
199
*Refer to numbered notes in Appendix A or lettered notes in Appendix B; factors without asterisks are from AP-42.
-------
UD
sec
Process
PART
Lbs/Unit
so
Lbs/Unit
NO
Lbs/Unit
VOC
Lbs/Unit
CO
Lbs/Unit
Units
Notes
Fugitive Emissions (Continued)
3-04-002-32 -
3-04-002-33 -
3-04-002-34 -
3-04-002-35 -
3-04-002-36 -
3-04-002-37 -
3-04-002-38 -
3-04-002-39 -
3-04-002-99 -
Gray Iron Fout
3-04-003-01 -
3-04-003-02 -
3-04-003-03 -
3-04-003-04 -
3-04-003-05 -
3-04-003-10 -
3-04-003-15 -
3-04-003-20 -
3-04-003-25 -
3-04-003-31 -
3-04-003-32 -
3-04-003-33 -
3-04-003-40 -
3-04-003-41 -
3-04-003-42 -
3-04-003-50 -
3-04-003-51 -
3-04-003-52 -
3-04-003-53 -
3-04-003-54 -
3-04-003-55 -
3-04-003-56 -
3-04-003-57 -
3-04-003-58 -
3-04-003-60 -
3-04-003-70 -
3-04-003-71 -
3-04-003-98 -
3-04-003-99 -
Wire Incinerator
Sweating Furnace
Cupola Furnace
Reverberatory Furnace
Rotary Furnace
Crucible Furnace
Electric Induction Furnace
Casting Operations
Other Not Classified (Specify
in Comment a)
idries - 3321
Cupola
Reverberatory Furnace
Electric Induction Furnace
Electric Arc Furnace
Annealing Operation
Inoculation
Charge Handling
Pouring /Cast ing
Castings Cooling
Casting Shakeout
Casting Knockout
Shakeout Machine
Castings Grinding/Cleaning
Casting Cleaning/Tumblers
Casting Cleaning /Chippers
Sand Grinding/Handling
Core Ovens
Sand Grinding/Handling
Core Ovens
Core Ovens
Sand Dryer
Sand Silo
Conveyors /Elevators
Sand Screens
Castings Finishing
Shell Core Machine
Core Machines /Other
Other Not Classified (Specify
in Comments)
Other Not Classified (Specify
in Comments)
13.
0.
3.
5.
4.
0.
0.
0.
13.
2.
0.
12.
4.
0.
5.
10.
32.
17.
•0.
•2.
40.
1.
0.
75
75
66
27
43
49
14
015
8
1
9
7
0
6
0
0
0
0
0
1
oid
•0.0
•0.0
•0.0
•0.0
•0.0
•0.0
•0.0
•0.0
1.2 S
•180.0
NEC
•0.25
•NEC
•0.02
•NEC
•0.0
•0.0
•0.0
0.0
•0.0
•0.0
•0.0
•0.32
•0.0
•0.32
•0.33
•0.002
•0.0
•0 . 0
•0.0
•0.32
•0.32
•0.0
•0.0
•0.0
•0.0
•0.0
•0.0
•0.0
•0.0
A
•0.1
•5.8
•NEC
0.32
•1.0
•NEC
•0.01
•NEC
•0.0
•0.0
•0.0
0.0
•0.0
•0.0
•0.0
•0.5
•0.0
•0.5
•0.5
•1.6
•0 .0
•0.0
*0 0
•0.0
•0.5
•0.5
•0.0
•0.0
•0.0
•0.0
•0.0
•0.0
•0.0
•0.0
•0.18
•0.015
•NEC
0.18
•0.10
•0.005
•NEC
•0.14
•NEC
•1.2
•1.2
•1.2
0.0
•0.0
•0.0
•0.0
•0.0008
•0.0
•0.0008
•0.0008
•0.004
•0.0
•0.0
•0.0
•0.0
•o.oooa
•0.0008
Tons
Tons
Tons
Tons
Tons
Tons
Tons
Tons
Tons
145.0 Tons
0 . 0 Tons
0 . 0 Tons
19.0 Tons
Tons
Tons
of Charge
of Charge
of Charge
of Charge
of Charge
of Charge
of Charge
of Castings Produced
Produced
Metal Charged 57,
Metal Charged
Metal Charged 127,
Metal Charged
Processed
Inoculated
Tons Metal Charged
Tons Metal Charged 57,
Tons Metal Charged
Tons Metal Charged
Tons Sand Handled
Tons Sand Handled
0.0 Tons Metal Charged
Tons Castings Cleaned
Tons Castings Cleaned
Tons Sand Handled
Tons Sand Handled
Tons Metal Charged
Tons Metal Charged
Gallons Core Oil Used
Tons Sand Handled
Tons Sand Handled
Tons
Tons
Tons
Tons
Tons
Gal It
Tons
Sand Handled
Sand Bandied
Metal Charged
Cores Produced
Cores Produced
sns
Metal Charged
199
199
199
199
199
199
199
199
298, 299
298, 362
298, 299
298, 305
149, 185
57
311
122, 141
311
57, 280
57, 280
57, 280
246
246
191
194
191
194
194
220
246
246
246
246
281
281
*Refer to numbered notes in Appendix A or lettered notes in Appendix B: factors without asterisks are from AP-42.
-------
SCC Process
Secondary Lead Smelting - 3341. 3369
3-04-004-01 - Pot Furnace
3-04-004-02 - Reverberatory Furnace
3-04-004-03 - Blast Furnace (Cupola)
3-04-004-04 - Rotary Sweating Furnace
3-04-004-05 - Reverberatory Sweating Furnace
3-04-004-06 - Pot Furnace Heater: Distillate
Oil
3-04-004-07 - Pot Furnace Heater: Natural Gas
3-04-004-08 - Barton Process Reactor (Oxidation
Kettle)
3-04-004-09 - Casting
3-04-004-10 - Battery Breaking
3-04-004-11 - Scrap Crushing
3-04-004-12 - Sweating Furnace: Fugitive
3-04-004-13 - Smelting Furnace: Fugitive
3-04-004-14 - Kettle Refining: Fugitive
3-04-004-99 - Other Not Classified (Specify
in Comments)
Lead Battery Manufacture - 3691
3-04-005-05 - Overall Process
3-04-005-06 - Grid Casting
3-04-005-07 - Paste Mixing
3-04-005-08 - Lead Oxide Mill (Baghouse Outlet)
3-04-005-09 - Three Process Operation
3-04-005-10 - Lead Reclaiming Furnace
3-04-005-11 - Small Parts Casting
3-04-005-12 - Formation
3-04-005-13 - Barton Process: Oxidation Kettle
3-04-005-21 - Overall Process
3-04-005-22 - Grid Casting
3-04-005-23 - Paste Mixing
3-04-005-24 - Lead Oxide Mill (Baghouse Outlet)
3-04-005-25 - Stacking/PB Burn Battery Assembly
3-04-005-26 - Lead Reclaiming Furnace
3-04-005-27 - Small Parts Casting
3-04-005-28 - Formation
3-04-005-99 - Other Not Classified (Specify
in Comments)
Magnesium - 3341
3-04-006-01 - Pot Furnace
3-04-006-99 - Other Not Classified (Specify
in Comments)
PART
Lbs/Unit
0.8
323
307
70.0
51.0
40.0
0.87
2.55
16.5
0.002
139.0
2.84
3.92
0.11
84
6.68
0.19
32.4
4.0
SO
Lbs/flnit
0.0
80.0
53.0
M44.0 S
*0.6
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
NO
Lbs/dnit
0.0
*0.3
*0.1
*20.0
*140.0
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
*2.5
voc
Lbs/Unit
0.0
*NEG
*NEG
*NEG
•NEG
*0.20
*2.8
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
*2.4
CO
Lbs/Unit Units
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
Tons Metal Charged
Tons Metal Charged
Tons Metal Charged
Tons Metal Charged
Tons Metal Charged
10 Gallons Burned
6
10 Cubic Feet Burned
Tons Lead Oxide Produced
Tons of Lead Cast
Tons Metal Charged
Tons Metal Charged
Tons Metal Charged
Tons Metal Charged
Tons Metal Charged
Tons Processed
10 Batteries Produced
10 Batteries Produced
10 Batteries Produced
10 Batteries Produced
10 Batteries Produced
10. Batteries Produced
3
10 Batteries Produced
3
10 Batteries Produced
Tons Processed
Tons Processed
Tons Processed
Tons Processed
Tons Processed
Tons Processed
Tons Processed
Tons Processed
Tons Processed
10 Batteries Produced
Tons Processed
Tons Processed
Notes
58, 209, 298
58, 184, 298
58
58
129
129
199
199, 298
199, 298
298
298
298
333
333
333
333
333
333
333
333
333
149, 247
Refer to numbered notes in Appendix A or lettered notes in Appendix B; factors without asterisks are from AP-42.
-------
oo
SCC Process
Steel Foundry - 3324. 3325
3-04-007-01 - Electric Arc Furnace
3-04-007-02 - Open Hearth Furnace
3-04-007-03 - Open Hearth Furnace with Oxygen
Lance
3-04-007-04 - Heat-Treating Furnace
3-04-007-05 - Electric Induction Furnace
3-04-007-06 - Sand Grinding/Handling in Mold
and Core Making
3-04-007-07 - Core Ovens
3-04-007-08 - Pouring and Casting
3-04-007-09 - Casting Shakeout
3-04-007-10 - Casting Knockout
3-04-007-11 - Castings Cleaning
3-04-007-12 - Charge Handling
3-04-007-13 - Castings Cooling
3-04-007-14 - Shakeout Machine
3-04-007-15 - Finishing: Specify in Comments
3-04-007-16 - Sand Grinding and Handling
3-04-007-17 - Core Ovens
3-04-007-18 - Core Ovens
3-04-007-20 - Sand Dryer
3-04-007-21 - Sand Silo
3-04-007-22 - Muller
3-04-007-23 - Conveyors /Elevators
3-04-007-24 - Sand Screens
3-04-007-25 - Casting Cleaning /Tumblers
3-04-007-26 - Casting Cleaning/Chlppers
3-04-007-30 - Shell Core Machine
3-04-007-31 - Core Machines /Other
3-04-007-99 - Other Mot Classified (Specify
in Comments)
Secondary Zinc Production - 3341
3-04-008-01 - Retort Furnace
3-04-008-02 - Horizontal Muffle Furnace
3-04-008-03 - Pot Furnace
3-04-008-05 - Galvanizing Kettle
3-04-008-06 - Calcining Kiln
3-04-008-07 - Concentrate Dryer
3-04-008-09 - Rotary Sweat Furnace
3-04-008-10 - Muffle Sweat Furnace
3-04-008-11 - Electric Resistance Sweat Furnace
3-04-008-12 - Crushing/Screening of Zinc
Residues
PART
Lbs/Unit
13.0
11.0
10.0
0.1
0.65
2.71
*5.0C
*32.0°
*17.0C
*0.6C
*io.oc
J
*0.01
*40.0C
1.1
47.0
45.0
0.1
5.0
89.0
18.0
21.4
10.0
4.25
SO
Lbs/9nlt
*0.25
*470
0.0
*0.0
*0.32
*0.02
*0.0
*NEG
*0.0
*0.4
*0.0
*0.32
*0.33
*0.002
*0.0
*0.0
•0.0
*0.0
•0.0
*0.0
*0.32
•0.32
*0 . 002
*0 . 002
*18.3
*0.0
NO
Lbs/8nit
0.2
0.01
0.0
•80
0.0
*0.0
*0.05
*0.01
*2.4
*0.0
•NEC
•0.0
*87
*0.0
*0.05
*0.05
M.6
*0.0
*0.0
•0.0
*0.0
•0.0
*0.0
*0.5
*0.5
*1.9
*0.4
*0.2
•0.0
VOC CO
Lbs/Unlt Lbs/Unit
*0.35
*0.17
*0.17
*0.02
0.0 0.0
*0.0
•0.0008
*0.14
*1.2
•1.2
*0.0
*0.0
*NEG
•1.2
•1.1
*0.0
•0.0008
•0.0008
•0 . 004
*0.0
*0.0
•0.0
*0.0
•0.0
*0.0
•0.0008
•0.0008
*0.0
*2.4
•2.4
•0.0
•0.06
*0.004
*2.4
*2.4
*2.4
*0.0
Units
Tons Processed
Tons Processed
Tons Processed
Tons Processed
Tons Processed
Tons Processed
Tons Processed
Tons Metal Processed
Tons Metal Processed
Tons Sand Handled
Tons Metal Processed
Tons Metal Processed
Tons Metal Processed
Tons Sand Handled
Tons Metal Processed
Tons Metal Processed
Tons Metal Processed
Gallons Core Oil Used
Tons Sand Handled
Tons Sand Handled
Tons Sand Handled
Tons Sand Handled
Tons Sand Handled
Tons Castings Cleaned
Tons Castings Cleaned
Tons Cores Produced
Tons Cores Produced
Tons Processed
Tons Produced
Tons Produced
Tons Produced
Tons Produced
Ions Produced
Tons Produced
Tons Produced
Tons Produced
Tons Produced
Tons Residue
Notes
252, 305
252
252
148
191
194
196
196
196
246
356
353
196
345
191
194
194
220
246
358
246
246
246
246
281
281
323
321
145, 251, 327
141, 251, 325
122, 250
60
149, 327
327
327
191
*Refer to numbered notes in Appendix A or lettered notes in Appendix B; factors without asterisks are from AP-42.
-------
sec
Process
PART SO NO
Lbs/Unit Lbs/finit Lbs/ffnit
VOC
Lbs/Unit
CO
Lbs/Unit Units
Notes
Secondary Zinc Production - 3341 (Continued)
3-04-008-1*
3-04-008-18
3-04-008-24
3-04-008-28
3-04-008-34
3-04-008-38
3-04-008-40
3-04-008-41
3-04-008-42
3-04-008-43
00 3-04-008-51
ro
3-04-008-52
3-04-008-53
3-04-008-54
3-04-008-55
3-04-008-61
3-04-008-62
3-04-008-63
3-04-008-64
3-04-008-65
3-04-008-66
3-04-008-67
3-04-008-68
3-04-008-69
3-04-008-70
3-04-008-71
3-04-008-72
3-04-008-73
?-ni-nn«-7i
3-04-008-75
3-04-008-76
3-04-008-77
3-04-008-99
- Kettle-Sweat Furnace (Clean
Metallic Scrap)
- Reverberator? Sweat Furnace
(Clean Metallic Scrap)
- Kettle-Sweat Furnace (General
Metallic Scrap)
- Reverberatory Sweat Furnace
(General Metallic Scrap)
- Kettle-Sweat Furnace (Residual
Scrap)
- Reverberatory Sweat Furnace
(Residual Scrap)
- Alloying
- Scrap Melting: Crucible
- Scrap Melting: Reverberatory
Furnace
- Scrap Melting: Electric Induction
Furnace
- Retort and Muffle Distillation:
Pouring
- Retort and Muffle Distillation:
Casting
- Graphite Rod Distillation
- Retort Distillation/Oxidation
- Muffle Distillation/Oxidation
- Reverberatory Sweating
- Rotary Sweating
- Muffle Sweating
- Kettle (Pot) Sweating
- Electric Resistance Sweating
- Sodium Carbonate Leaching
- Kettle (Pot) Melting Furnace
- Crucible Melting Furnace
- Reverberatory Melting Furnace
- Electric Induction Melting
- Alloying Retort Distillation
- Retort and Muffle Distillation
- Casting
- Graphite Rod Distillation
- Retort Distillation/Oxidation
- Muffle Distillation/Oxidation
- Retort Reduction
- Other Not Classified (Specify
in Comments)
0.0
0.0
11.0
13.0
25.0
32.0
0.6
0.3
30.0 *20 *7.9
30.0 *40 *110
1.3
0.9
1.07
0.56
0.5
*NEG *NEG
0.005
0.005
0.005
0.005
2.36
0.015
*0.0
*0.0
*2.4
•2.4
*2.4
*2.4
*0.0
*2.5
*5.2
*0.18
*NEG
*NEG
*NEG
*0.0
*0.0
•2.4
*2.4
•2.4
*2.4
*2.4
*NEG
*2.4
•2.5
•5.2
*0.18
*0.0
•NEC
*NEG
*NEG
*0.0
*NEG
*NEC
Tons Produced
Tons Produced
Tons Produced
Tons Produced
Tons Produced
Tons Produced
Tons Produced
Tons Produced
Tons Produced
Tons Produced
Tons Produced
Tons Produced
Tons Produced
Tons Zinc Oxide
Produced
Tons Zinc Oxide
Produced
Tons Produced
Tons Produced
Tons Produced
Tons Produced
Tons Scrap Processed
Tons Produced
Tons Produced
Tons Produced
Tons Produced
Tons Produced
Tons Produced
Tons Produced
Tons Produced
Tons Produced
Tons Produced
Tons Produced
Tons Produced
Tons Produced
323
323
321
321
321
321
325
248
248
249
322
322
326
146, 149, 323
146, 149, 323
321
327
327
321
327
324
321
248
248
249
323
322
322
326
323
326
247
*Refer to numbered notes in Appendix A or lettered notes in Appendix Bj factors without asterisks are from AP-42.
-------
CO
CO
PART
SCC Process Lbs/Unlt
Malleable Iron - 3322
3-04-009-01 - Annealing
3-04-009-99 - Other Not Classified (Specify
In Comnents)
Nickel - 3341
3-04-010-01 - Flux Furnace
3-04-010-02 - Mlxlng/Blendlng/Grlndlng/Screening
3-04-010-04 - Heat Treat Furnace
3-04-010-05 - Induction Furnace (Inlet Air)
3-04-010-06 - Induction Furnace (Under Vacuum)
3-04-010-07 - EAF with Carbon Electrode
3-04-010-08 - EAF
3-04-010-10 - Finishing: Pickling/Neutralizing
3-04-010-11 - Finishing: Grinding
3-04-010-99 - Other Not Classified (Specify
in Conments)
Furnace Electrode Hanufacture - 3624
3-04-020-01 - Calcination
3-04-020-02 - Mixing
3-04-020-03 - Pitch Treating
3-04-020-04 - Bake Furnaces
3-04-020-99 - Other Not Classified (Specify
in Comments)
Metal Heat Treating - 3398
3-04-022-01 - Furnace: General
3-04-022-10 - Quench Bath
Lead Cable Coatiiut - 3357. 3315
3-04-040-01 - General 0.6
Miscellaneous CastiM and Fabricating - 3300-3399
SO
Lbs/Snit
*0.002
*0.0
•0.002
•0.03
*0.03
*57.3
•0.25
*0.0
•0.0
0.0
0.0
*1.6
*0.002
*NEG
NO
Lbs/finit
•0.6
*1.5
*0.0
*1.5
*0.003
•0.32
*0.0
*0.0
0.0
0.0
•4.0
*NEG
VOC
Lbs/Unlt
*0.1
*0.004
*0.0
*0.004
*NEG
*NEG
*0.1
*0.18
*0.0
*0.0
*0.06
0.0
*NEG
*1.0
*0.1
*280
CO
Lbs/Unlt Units
Tons Metal Charged
Tons Metal Charged
Tons Processed
Tons Processed
Tons Processed
Tons Processed
Tons Processed
Tons Processed
Tons Processed
Tons Processed
Tons Processed
Tons Processed
Tons Processed
0.0 Tons Processed
Tons Processed
Tons Processed
Tons Processed
Tons Metal Processed
Tons Metal Processed
Tons Lead Processed
Notes
142, 149
363
191
363
364
364
365
353
365
353
207
285
210, 248
145, 224, 251
143, 307
7A
3-04-049-01 - Wax Burnout Oven
3-04-050-01 - Other Not Classified (Specify
in Comments)
3-04-050-99 - Other Not Classified (Specify
in Comments)
Secondary Metal Production - Fugitive Emissions
3-04-888-01 - Specify in Comments Field
3-04-888-02 - Specify in Comments Field
3-04-888-03 - Specify in Comments Field
3-04-888-04 - Specify in Comments Field
3-04-888-05 - Specify In Comments Field
Tons Produced
Each
Tons Product
Tons Product
Tons Product
Tons Product
Tons Product
*Refer to numbered notes In Appendix A or lettered notes In Appendix B: factors without asterisks are from AP-42.
-------
CO
PART
scc Process Lbs/Unlt
Secondary Metal Production - Fuel Fired Equipment
Process Heaters
3-04-900-01 - Distillate Oil (No. 2)
3-04-900-02 - Residual Oil
3-04-900-03 - Natural Gas
3-04-900-04 - Process Gas
Incinerators
3-04-900-11 - Distillate Oil (No. 2)
3-04-900-12 - Residual Oil
3-04-900-13 - Natural Gas
3-04-900-14 - Process Gas
Flares
3-04-900-023 - Natural Gas
3-04-900-024 - Process Gas
Secondary Metal Production - Other Not Classified
3-04-999-99 - Other Not Classified (Specify in
Comments)
MINERAL PRODUCTS - MAJOR GROUPS 11. 12, 14. 28. 29. 32. 44
Asphalt Roofing Manufacture - 2952
3-05-001-01 - Asphalt Blowing: Saturant 7.2
3-05-001-02 - Asphalt Bloving: Coating 26.7
3-05-001-03 - Felt Saturation: Dipping Only 0.5
3-05-001-04 - Felt Saturation: Dipping/Spraying 3.14
3-05-001-10 - Bloving
3-05-001-11 - Dipping Only
3-05-001-12 - Spraying Only
3-05-001-13 - Dipping/Spraying
3-05-001-98 - Not Classified (Specify in
Comments)
Asphaltic Concrete - 2951
3-05-002-01 - Rotary Dryer, Conventional Plant 45.0
3-05-002-02 - Hot Elevators, Screens, Bins and 0.2
Mixer
3-05-002-03 - Stnrage Pl].« *0.33CC
3-05-002-04 - Cold Aggregate Handling 0.1
3-05-002-05 - Drum, Dryer Hot Asphalt Plants 4.9
3-05-002-06 - Asphalt Heater (Natural Gas)
3-05-002-07 - Asphalt Heater (Residual Oil)
3-05-002-08 - Asphalt Heater (Distillate Oil)
SO
Lbs/Unit
*144.0 S
•159.0 S
*0.6
*950.0 S
0.0
0 . 0
0.0
0.0
*0 . 0
*0.0
*0.0
*0.0
*0.073bb
*0.09
*0.12
0.0
*0.6
*159 0 S
*144.0 S
NO
Lbs/finit
*20.0
*55.0
M40.0
*140.0
0.0
0 . 0
0.0
0.0
*0 . 0
*0.0
*0.0
*0.0
0.036
*0.03
*0.0
0.0
*140.0
*55.0
*20.0
voc
Lbs/Unit
*0.20
*0.28
*2.8
*2.8
*0.4
*0.56
*5.6
*5.6
*5.6
*5.6
1.46
1.86
0.02
0.03
*Q ,09
*0.02
*0.01
•0.03
0.028
*0.0
•NEC
*0.13
0.0
*2.8
*0.28
*0.20
CO
Lbs/Unit Units
10 Gallons Burned
10 Gallons Burned
10 Cubic Feet Burned
10 Cubic Feet Burned
10 Gallons Burned
10 Gallons Burned
10 Cubic Feet Burned
10 Cubic Feet Burned
6
10 Cubic Feet Burned
10 Cubic Feet Burned
Tons Processed
0.27 Tons Asphalt Processed
0.02 Tons Asphalt Shingle
0.25 Tons Asphalt Shingle
Tons Saturated Felt
Tons Saturated Felt
Tons Saturated Felt
Gallons
0.038 Tons Produced
Tons Produced
Tons Produced
Tons Produced
0.0 Tops of Asphalt
10 Cubic Feet Burned
10 Gallons Burned
10 Gallons Burned
Notes
129
129
129
129
130
130
130
130
130
130
ry -t £
£.±0
216
216
216
301
134
972
169
129
129
129
Refer to numbered notes in Appendix A or lettered notes in Appendix B; factors without asterisks are from AP-42.
-------
sec
Process
PART
Lbs/Unlt
SO
Lbs/Unit
NO
Lbs/unit
VOC
Lbs/Unit
CO
Lbs/Unit
Units
Notes
Brick Manufacturing - 3251
3-05-003-01
3-05-003-02
3-05-003-03
3-05-003-07
3-05-003-08
3-05-003-09
3-05-003-11
3-05-003-12
3-05-003-13
3-05-003-14
3-05-003-15
3-05-003-16
00 3-05-003-98
cn
- Raw Material Drying
- Raw Material Grinding
- Storage of Raw Materials
- Process Calcining
- Screening
- Proceas Blending and Mixing
- Curing and Firing: Gas-Fired
Tunnel Kilns
- Curing and Firing: 011-Fired
Tunnel Kilns
- Curing and Firing: Coal -Fired
Tunnel Kilns
- Curing and Firing: Gas-Fired
Periodic Kilns
- Curing and Firing: 011-Fired
Periodic Kilns
- Curing and Firing: Coal -Fired
Periodic Kilns
- Other Not Classified (Specify
in Comments)
70.
76.
34.
20
0.
0.
0.
0.
0.
18.
0
0
0
02
6
67 A
065
88
84
*0
0
0
0
0
.002
.0
.0
.0
.0
NEC
4
7
.0 S
.31 S
NEC
5
12
.9 S
.13 S
0
0
0
0
0
0
1
1
0
1
2
.0
.0
.0
.0
.0
.18
.1
.45
.5
.62
.35
*0.004
0.0
0.0
*0.02
0.0
0.0
0.03
0.07
0.01
0.01
0.01
0.02
Tons
0 . 0 Tons
0 . 0 Tons
Tons
0 . 0 Tons
0 . 0 Tons
0.06 Tons
0 . 12 Tons
1.43 Tons
0 . 15 Tons
0.19 Tons
2.39 Tons
Raw Material
Raw Material
Material Stored
Raw Material
Raw Material
Raw Material
Produced
Brick Produced
Produced
Produced
Produced
Produced
220
223
298
298-302
301, 302
298-302
298-302
298, 300-302
298-302
Gallons
Calcium Carbide - 2819
3-05-004-01
3-05-004-02
3-05-004-03
3-05-004-04
3-05-004-05
3-05-004-06
- Electric Furnace (Hoods and
Main Stack)
- Coke Dryer
- Furnace Room Vents
- Tap Fume Vents
- Primary Secondary/Crushing
- Circular Charging: Conveyor
24.
2.
26.
0
0
0
3
3
0
0
0
0
.0
.0
.0
.0
.0
.0
*0
*0
.2
.0
*NEG
*0.0
*NEG
*NEG
*0.0
*NEG
Tons
Tons
Tons
Tons
Tons
Tons
Produced
Produced
Produced
Produced
Produced
Produced
285
141
285
285
191
285
Caatable Refractory - 3255
3-05-005-01
3-05-005-02
3-05-005-03
3-05-005-04
3-05-005-05
3-05-005-98
3-05-005-99
- Raw Material Dryer
- Raw Material Crushing/Processing
- Electric Arc Melt
- Curing Oven
- Molding and Shakeout
- Other Hot Classified (Specify in
Comments)
- Other Not Classified (Specify in
Comments)
30.
120.
50.
0.
25.
0
0
0
2
0
*0
0
*0
*0
.002
.0
.0
.0
*1
0
*0
*0
.6
.0
.16
.0
*0.004
0.0
*NEG
*1.0
•0.0005
Tons
0 . 0 Tons
Tons
Tons
Tons
Feed Material
Feed Material
Feed Material
Feed Material
Feed Material
220
119
119, 338
170
Gallons
Tons
Cement Manufacturing - Dry Process - 3241
3-05-006-06 - Kilns""
3-05-006-07
- Raw Material Unloading
256
*0.
J
2d
10
0
.2
.0
2
0
.8
.0
*0.02
0.0
Tons
0 . 0 Tons
Feed Material
Cement Produced
Material Unloaded
107, 298, 300
*Refer to numbered notes in Appendix A or lettered notes in Appendix B; factors without asterisks are from AP-42.
-------
CO
sec
Process
PART
Lbs/Unit
SO
Lbs/Unit
NO
Lbs/Unit
voc
Lbs/Unit
CO
Lbs/Unit
Units
Notes
Cement Manufacturing - Dry Process - 3241 (Continued)
3-05-006-08
3-05-006-09
3-05-006-10
3-05-006-11
3-05-006-12
3-05-006-13
3-05-006-14
3-05-006-15
3-05-006-16
3-05-006-17
3-05-006-18
3-05-006-19
Wet Process
3-05-007-06
3-05-007-07
3-05-007-08
3-05-007-09
3-05-007-10
3-05-007-11
3-05-007-12
3-05-007-14
3-05-007-15
3-05-007-16
3-05-007-17
3-05-007-18
3-05-007-19
Ceramic Clay
3-05-008-01
3-05-008-02
3-05-008-03
3-05-008-99
Clay and Fly
3-05-009-01
3-05-009-02
3-05-009-03
3-05-009-04
3-05-005-05
3-05-009-06
3-05-009-07
- Raw Material Piles
- Primary Crushing
- Secondary Crushing
- Screening
- Raw Material Transfer
- Raw Material Grinding and Drying
- Clinker Cooler
- Clinker Piles
- Clinker Transfer
- Clinker Grinding
- Cement Silos
- Cement Load Out
- 3241
- Kilns
- Raw Material Unloading
- Raw Material Piles
- Primary Crushing
- Secondary Crushing
- Screening
- Raw Material Transfer
- Clinker Cooler
- Clinker Piles
- Clinker Transfer
- Clinker Grinding
- Cement Silo
- Cement Loadout
Manufacturing - 3261
- Drying
- Grinding
- Storage
- Other Not Classified (Specify
in Comments)
Ash Sinterinc (Low Density Aggregate
- Fly Ash Sintering
- Clay/Coke Sintering
- Natural Clay/Shale Sintering
- Raw Clay/Shale Crushing/Screening
- Raw Clay/ Shale Tc*uaf»/CcuV*,iii*
- Raw Clay /Shale Storage Piles
- Sintered Clay/Coke Product
Crushing and Screening
*4.0Q
*0.5C
*1.5C
J
*0.3d
64.0
9.2
96.0
J
*0.24
228.0.
*0.2d
*4.0d
*0.5°
*1.5C
J
*0.3d
32.0
J
•0.24
70.0
76.0
34.0
Manufacture )
110.0
40.0
12.0.
*°'5d
O
15.0
0.0
0.0
0.0
0.0
0.0
0.0
0.0
0.0
0.0
0.0
0.0
0.0
10.2
0.0
0.0
0.0
0.0
0.0
0.0
0.0
0.0
0.0
0.0
0.0
0.0
*2.4
•7.4
- 3295
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
2.8
0.0
0.0
0.0
0.0
0.0
0.0
0.0
0.0
0.0
0.0
0.0
0.0
n.6
*2.3
•0.0
0.0
a.o
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
«o
*0
*0
*1
*1
*1
0
n
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
.004
.0
.0
.4
.4
.4
.0
_ n
.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
n
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
Tons
Tons
Tons
Tons
Tons
Tons
Tons
Tons
Tons
Tons
Tons
Tons
Tons
Tons
Tons
Tons
Tons
Tons
Tons
Tons
Tons
Tons
Tons
Tons
Tons
Tons
Tons
Tons
Tons
Tons
Tons
Tons
Tons
Tons
Tons
in Piles
Processed
Processed
Processed
Handled
Cement Produced
Cement Produced
Cement Produced
Cement Produced
Cement Produced
Cement Produced
Cement Produced
Cement Produced
of Material Unloaded
in Piles
Processed
Processed
Processed
Handled
Cement Produced
Cement Produced
Cement Produced
Cement Produced
Cement Produced
Cement Produced
Input to Process
Input to Process 122,
Input to Process
Produced
Finished Product
Finished Product
Finished Product
Raw Material
P-v M-tsrial
Raw Material
Finished Product
298
298
300
211, 220
141, 160
160
81
81
81
*Refer to numbered notes in Appendix A or lettered notes in Appendix B; factors without asterisks are from AP-42.
-------
CO
sec
Process
PART
Lbs/Unit
Clay and Fly Ash Sintering (Low Density Aggregate Manufacture)
3-05-009-08 -
3-05-009-09 -
3-05-009-10 -
3-05-009-99 -
Coal Cleaning
Thermal Dryer
3-05-010-01 -
3-05-010-02 -
3-05-010-03 -
3-05-010-04 -
3-05-010-05 -
3-05-010-06 -
3-05-010-07 -
Sintered Clay/Shale Product
Crushing and Screening
Expanded Shale Clinker Cooling
Expanded Shale Storage
Other Not Classified (Specify
in Comments)
- 1111. 1211*"
- 1111. 1211**
Fluldized Bed
Flash or Suspension
Multilouvered
Rotary
Cascade
Continuous Carrier
Screen
12
20
16
25
Material Handling - 1111. 121l"
3-05-010-08 -
3-05-010-09 -
3-05-010-10 -
3-05-010-11 -
3-05-010-12 -
3-05-010-13 -
3-05-010-1* -
3-05-010-15 -
3-05-010-16 -
3-05-010-17 -
Unloading
Raw Coal Storage
Crushing
Coal Transfer
Screening
Air Tables
Cleaned Coal Storage
Loading
Loading: Clean Coal
Secondary Crushing
*0
*0
*0
*0
*0
.0
.0
.0
.0
.02d
V
*\
.16d
J
.ld
SO
Lbs/finit
NO
Lbs/Snlt
voc
Lbs/Unit
CO
Lbs/Unit
Units
Notes
- 3295 (Continued)
0
0
0
0
*0
0
0
0
0
0
0
0
0
0
0
.0
.0
.0
.A3
.42
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
0.0
0.0
0.0
0.17
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
.1
.1
.1
.1
.1
.1
.1
.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
Tons Finished Product
Tons Finished Product
Tons Finished Product
Tons Finished Product
Tons Coal Dried
Tons Coal Dried
Tons Coal Dried
Tons Coal Dried
Tons Coal Dried
Tons Coal Dried
Tons Coal Dried
Tons Shipped
Tons Shipped
Tons Shipped
Tons Shipped
Tons Shipped
Tons Shipped
Tons Shipped
Tons Shipped
Tons Shipped
Tons Shipped
133, 225
225
225
225
225
225
Surface Mining Operations - 1111. 1211*"
3-05-010-21 -
3-05-010-22 -
3-05-010-23 -
3-05-010-2* -
3-05-010-30 -
3-05-010-31 -
3-05-010-32 -
3-05-010-33 -
3-05-010-3* -
3-05-010-35 -
3-05-010-36 -
3-05-010-37 -
Overburden Removal
Drilling/Blasting
Loading
Hauling
Topsoll Removal
Scrapers: Travel Mode
Topsoil Unloading
Overburden: Drilling
Coal Sean: Drilling
Blasting: Coal Overburden
Dragline: Overburden Removal
Truck Loading: Overburden
0
0
0
17
0
1*.
0
1.
0
32
0.
0.
.45
.0001
.1
.2
.05
.6
.0*
.3
.22
.7
.05
.03
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
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
Tons Coal Mined
Tons Coal Mined
Tons Coal Mined
Vehicle-Miles Traveled
Tons of Topsoll Removed
Vehicle-Miles by Scrapers
Tons of Topsoll
Holes Drilled
Holes Drilled
Blasts
Cubic Yards Overburden
Tons Overburden Loaded
*Refer to numbered notes in Appendix A or lettered notes in Appendix B; factors without asterisks are from AP-42.
-------
sec
Process
PART
Lbs/Unit
SO
Lbs/finit
NO
Lbs/$nit
voc
Lbs/Unit
CO
Lbs/Unit
Units
Notes
Surface Mining Operations - 1111. 1211 (Continued)
3-05-010-38
3-05-010-39
3-05-010-40
3-05-010-41
3-05-010-42
3-05-010-43
3-05-010-44
3-05-010-45
3-05-010-46
3-05-010-47
3-05-010-48
3-05-010-49
3-05-010-50
3-05-010-90
CO 3-05-010-99
- Truck Loading: Coal
- Hauling: Haul Trucks
- Truck Unloading: End Dump-Coal
- Truck Unloading: Bottom
Dump-Coal
- Truck Unloading: Bottom
Dump-Overburden
- Open Storage Pile: Coal
- Train Loading: Coal
- Bulldozing: Overburden
- Bulldozing : Coal
- Grading
- Overburden Replacement
- Wind Erosion: Exposed Areas
- Vehicle Traffic: Light/Medium
Vehicles
- Haul Roads: General
- Other Not Classified (Specify
in Comments)
Concrete Batching - 3271. 3272. 3273. 3275. 1771,
3-05-011-01
3-05-011-12
3-05-011-13
3-05-011-14
3-05-011-15
- General (Non-fugitive)
- Mixing: Wet
- Mixing: Dry
- Transferring: Conveyors/Elevators
- Storage: Bins /Hoppers
0
17
0
0
0
47,400
0
3
49
5
0
760
2
, 3292
0
.03
.2
.007
.066
.002
.0
.028
.94
.4
.37
.012
.0
.79
.2
Concrete Batching - Fugitive Emissions - 3271. 3272. 3273. 3275,
3-05-011-06
3-05-011-07
3-05-011-08
3-05-011-09
- Transfer of Sand and Aggregate
to Elevated Bins
- Cement Unloading to Storage Bins
- Weight Hopper Loading of Cement,
Sand and Aggregate
- Mixer Loading of Cement, Sand
and Aggregate
0
0
0
0
.04
.24
.02
.04
0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
*0.
*0.
*0.
*0.
*0.
1771
0.
0.
0.
0.
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
. 3292
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
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
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
Tons Coal Loaded
Vehicle-Miles by Haul
Trucks
Tons Coal
Tons Coal
Tons Overburden
Acres of Coal Storage Area
Tons of Coal Loaded
Bulldozer-Hours of
Operation
Bulldozer-Hours of
Operation
Vehicle-Miles by Graders
Tons Overburden
Acres of Exposed Area
Vehicle-Miles by Light/
Medium Vehicles
Tons Coal
Tons Shipped
Cubic Yards Concrete
Produced
Cubic Yards Concrete
Produced
Cubic Yards Concrete
Produced
Cubic Yards Concrete
Produced
Cubic Yards Concrete
Produced
Tons Produced
Tons Produced
Tons Produced
Tons Produced
170
278
278
278
278
*Refer to numbered notes in Appendix A or lettered notes in Appendix B; factors without asterisks are from AP-42.
-------
CO
10
SCC Process
Concrete Batching - Fugitive Emissions - 3271. 3272,
3-05-011-10 - Loading of Transit Mix Truck
3-05-011-11 - Loading of Dry-Batch Truck
3-05-011-20 - Asbestos/Cement Products
3-05-011-99 - Other Not Classified (Specify
in Comments)
Fiberglass Manufacturing - 3229. 3296
Uool-Type Class Fiber - 3296
3-05-012-01 - Regenerative Furnace
3-05-012-02 - Recuperative Furnace
3-05-012-03 - Electric Furnace
3-05-012-04 - Forming (Rotary Spun)
3-05-012-05 - Curing Oven (Rotary Spun)
3-05-012-06 - Cooling
3-05-012-07 - Unit Melter Furnace
3-05-012-08 - Forming (Flame Attenuation)
3-05-012-09 - Curing (Flame Attenuation)
Textile-Type Glass Fiber - 3229
3-05-012-11 - Regenerative Furnace
3-05-012-12 - Recuperative Furnace
3-05-012-13 - Unit Melter Furnace
3-05-012-14 - Forming Process
3-05-012-15 - Curing Oven
3-05-012-21 - Raw Material Unloading/Conveying
3-05-012-22 - Raw Material Storage Bins
3-05-012-23 - Raw Material Mixing/Weighing
3-05-012-24 - Raw Material Crushing/Charging
3-05-012-99 - Other Not Classified (Specify
in Comments)
Frit Manufacture - 2899
3-05-013-01 - Rotary Furnace
3-05-013-99 - Other Not Classified (Specify
in Comments)
Glass Manufacture - 3211. 3221. 3229
3-05-014-02 - Container Glass: Melting Furnace
3-05-014-03 - Flat Glass: Melting Furnace
PART
Lbs/Unit
. 3273. 3275.
0.02
0.04
0.2
22.0
27.5
0.5
58.0
9.0
1.3
9.0
2.0
6.0
16.0
2.0
6.0
1.0
1.2
3.0
0.2
0.6
16.0
1.4
2.0
SO
Lbs/finit
1771. 3292
0.0
0.0
0.0
10.0
10.0
0.04
0.6
30.0
3.0
0.0
0.0
0.0
0.0
3.4
3.0
NO
Lbs/dnlt
(Continued)
0.0
0.0
0.0
5.0
1.7
0.27
*0.49
1.1
0.3
0.3
2.0
20.0
20.0
20.0
2.6
0.0
0.0
0.0
0.0
6.2
8.0
VOC
Lbs/Unlt
0.0
0.0
0.0
*0.2
*0.2
*0.2
7.0
3.0
0.04
*0.0
0.3
7.0
*0.2
*0.2
0.0
0.0
0.0
0.0
0.0
0.0
0.0
*2.4
0.2
0.1
CO
Lbs/Unit
0.0
0.0
0.0
0.25
0.25
0.05
1.7
0.25
3.5
1.0
0.5
0.9
1.5
0.0
0.0
0.0
0.0
0.2
0.1
Units
Tons Produced
Tons Produced
Tons Produced
Tons Produced
Tons Material Processed
Tons Material Processed
Tons Material Processed
Tons Material Processed
Tons Material Processed
Tons Material Processed
Tons Material Processed
Tons Material Processed
Tons Material Processed
Tons Material Processed
Tons Material Processed
Tons Material Processed
Tons Material Processed
Tons Material Processed
Tons Raw Material
Processed
Tons Raw Material
Processed
Tons Raw Material
Processed
Tons Raw Material
Processed
Tons Material Processed
Tons Charged
Tons Charged
Tons of Glass Produced
Tons of Glass Produced
Notes
162
162
162
131
162
162
162
247
299
Refer to numbered notes in Appendix A or lettered notes in Appendix B; factors without asterisks are from AP-42.
-------
sec
3-05-014-04
3-05-014-06
3-05-014-07
3-05-014-08
3-05-014-10
3-05-014-13
3-05-014-14
3-05-014-15
Process
icture - 3211. 3221. 3229 (Contlnuedl
- Pressed and Blown Class: Melting
Furnace
- Container Class: Forming and
Finishing
- Flat Class: Forming and Finishing
- Pressed and Blown Class: Forming
and Finishing
- Raw Material Handling (All Types
of Class)
- Gullet Crushing/Grinding
- Ground Gullet Beading Furnace
- Glass Etching with Hydrofluoric
Acid Solution
CvDsum Manufacture - 3275
3-05-015-01
3-05-015-02
3-05-015-04
3-05-015-05
3-05-015-06
3-05-015-07
3-05-015-08
3-05-015-09
3-05-015-10
3-05-015-11
3-05-015-12
3-05-015-13
3-05-015-14
3-05-015-15
3-05-015-16
3-05-015-17
3-05-015-18
3-05-015-19
3-05-015-20
3-05-015-21
3-05-015-22
- Rotary Ore Dryer
- Primary Grinder/Roller Mills
- Conveying
- Primary Crushing: Gypsum Ore
- Secondary Crushing: Gypsum Ore
- Screening: Gypsum Ore
- Stockpile: Gypsum Ore
- Storage Bins: Gypsum Ore
- Storage Bins: Landplaster
- Continuous Kettle: Calciner
- Flash Calciner
- Impact Mill
- Storage Bins: Stucco
- Tube/Ball Mills
- Mixers
- Bagging
- Mixers/Conveyor
- Forming Line
- Drying Kiln
- End Sawing (8 ft)
- End Sawing (12 ft)
Lime Manufacture - 327*
3-05-016-01
3-05-016-02
- Primary Crushing
- Secondary Crushing /Screening
PART
Lbs/Unit
17.4
NEC
NEC
NEC
NEC
ft
**°-°ff
*2 6
ff
•0.7
•0.5°
•1.5C
41.0
37.0
100.0
8.0
5.0
•0.5°
•1.5°
SO
Lbs/9nit
5.6
NEC
NEC
NEC
0.0
0.0
•5.6
•NEC
•0.002
•0.0
0.0
0.0
0.0
0.0
0.0
0.0
0.0
•46.2
*8.2
0.0
0.0
0.0
0.0
0.0
0.0
0.0
0.0
0.0
0.0
NO
Lbs/unit
8.5
NEC
NEC
NEC
0.0
0.0
•8.5
•NEC
•1.6
•0.0
0.0
0.0
0.0
0.0
0.0
0.0
0.0
•2.8
•2.8
0.0
0.0
0.0
0.0
0.0
0.0
0.0
0.0
0.0
0.0
voc
Lbs/Unit
0.3
8.7
NEC
9.0
0.0
0.0
•0.3
•NEC
•0.004
•0.0
0.0
0.0
0.0
0.0
0.0
0.0
0.0
•0.02
•0.02
•0.02
0.0
0.0
0.0
0.0
0.0
0.0
•0.02
0.0
0.0
0.0
0.0
CO
Lbs/Unit
0.2
NEC
MEG
NEC
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
Units Notes
Tons of Glass Produced
Tons of Glass Produced 298-300
299
, 302
Tons of Glass Produced 298-302
Tons of Glass Produced 298-300
Tons of Glass Produced
Tons Gullet Processed
Tons Beaded Glass
Gallons Etching Solution
Consumed
Tons Product
Tons Product
Tons Throughput
Tons Crude Gypsum
Processed
Tons Crude Gypsum
Processed
Tons Crude Gypsum
Processed
Tons Crude Gypsum
Processed
Tons Crude Gypsum
Processed
Tons Product
Tons Product 177, 223
Tons Product 223
Tons Product
Tons Product
Tons Product
Tons Product
Tons Product
Tons Product
Tons Product
TODS Product
10^ Sq. Ft. Board Sawed
10" Sq. Ft. Board Sawed
Tons Limestone Processed
Tons Limestone Processed
, 302
298
341
308
220
191
, 267
, 270
223
107
Refer to
numbered notes in Appendix A or lettered notes in Appendix B; factors without asterisks are from AP-42.
-------
sec
Process
PART
Lbs/Unit
SO
Lbs/unit
HO
Lbs/unit
voc
Lbs/Unlt
CO
Lbs/Unit
Units
Notes
Lime Manufacture - 3274 (Continued)
3-05-016-03
3-05-016-0*
3-05-016-05
3-05-016-06
3-05-016-07
3*05-016-08
3-05-016-09
3-05-016-10
3-05-016-11
3-05-016-12
— — — — — — ^^— — — ^^^— — rtrt
- Calcining-Vcrtlcal Kiln
- Calcining-Rotary Kiln
- Calcimatlc Kiln*"
- Fluidiz.d Bed Kiln
- Raw Material Transfer and
Conveying
- Raw Material Unloading
- Hydrator (Atmospheric)
- Raw Material Storage Piles
- Product Cooler
- Pressure Hydrator
8
350
50
*0.
*0.
0.
**.
40.
0.
j
8d
J
2d
-d
od
0
1
*8
*5,
0
0,
0
0
.2
.1
.0
.0
.0
.0
MEG
MEG
*2.8
2.8
0.2
0.0
0.0
0.0
0.0
HEG
NEC
*0
*0
*0
*0
0
0
.02
.06
.02
.02
.0
.0
*HEG
0
0
0
.0
.0
.0
Tons
*2 Tons
Tons
Tons
0 . 0 Tons
0 . 0 Tons
0 . 0 Tons
0 . 0 Tons
HEG Tons
HEG Tons
Lime Produced
Lime Produced
Lime Produced
Lime Produced
Limestone Processed
Limestone Processed
Hydrated Lime
Limestone Processed
Lime Produced
Hydrated Lime
Produced
3-05-016-13
3-05-016-1*
3-05-016-15
3-05-016-16
3-05-016-17
Mineral Wool
3-05-017-01
3-05-017-02
3-05-017-03
3-05-017-04
3-05-017-05
3-05-017-99
- Lime Silos
- Pack ing /Shipping
- Product Transfer and Conveying
- Primary Screening
- Multiple Hearth Calclner
- 3296
- Cupola
- Reverberatory Furnace
- Blow Chamber
- Curing Oven
- Cooler
- Other Hot Classified (Specify
in Comments)
*0.
22.
5.
17.
*.
2.
25d
0
0
0
0
0
0.
0
0
0.
*8
0.
0
0.
0
0
.0
.0
.0
.0
.2
.02
.0
.0
.0
.0
0.0
0.0
0.0
0.0
*2.8
*1.6
•NEC
*HEG
*0.16
*NEG
0
0
0
0
*o
.0
.0
.0
.0
.02
*HEG
*HEG
*0
*1
*0
.9
.0
.0*
0 . 0 Tons
0 . 0 Tons
0 . 0 Tons
0 . 0 Tons
Tons
Tons
Tons
Tons
Tons
Tons
Tons
Lime Produced
Lime Produced
Lime Produced
Limestone Processed
Lime Produced
Charged
Charged
Charged
Charged
Charged
Processed
Perlite Manufacture - 3295
3-05-018-01
3-05-018-99
- Vertical Furnace
- Other Not Classified (Specify
in Comments)
21.
0
*NEG
*NEG
*NEG
Tons
Tons
Phosphate Rock - 1*75
3-05-019-01
3-05-019-02
3-05-019-03
3-05-019-0*
3-05-019-05
3-05-019-99
- Drying
- Grinding
- Transfer/Storage
- Open Storage
- Calcining
- Other Hot Classified (Specify
in Comment 3)
Stone Quarrying/Process inn - 1411. 1422, 1423,
3-05-020-01
3-05-020-02
- Primary Crushing
- Secondary Crush/ Screen
5.
1.
2.
40.
15.
1429, 149
0.
1.
7
5
0
0
*
9
588
588
*0.
0.
0
0
0
0.
0.
.002
0
.0
.0
.0
.0
,0
*1.6
0.0
0.0
0.0
0.0
0.0
0.0
*0
0
0
0
0
0
0
.00*
.0
.0
.0
.0
.0
.0
Tons
0 . 0 Tons
0 . 0 Tons
0 . 0 Tons
0 . 0 Tons
Tons
0 . 0 Tons
0 . 0 Tons
Charged
Processed
Phosphate Rock
Phosphate Rock
Phosphate Rock
Phosphate Rock
Phosphate Rock
Processed
Raw Material
Raw Material
223, 270
132, 226
298, 300
226
226
285
298, 299
300, 302
298, 299
300, 302
226, 270
158
158
158
158
158
159
220
"Refer to numbered notes in Appendix A or lettered notes in Appendix B; factors without asterisks are from AP-42.
-------
ro
sec
PART
Process Lbs/Unit
SO
Lbs/Onit
NO
Lbs/finit
VOC
Lbs/Unit
CO
Lbs/Unit
Units
Notes
Stone Quarry Inn/Process Ion - 1411. 1422. 1423. 1429. 1499 (Continued)
3-05-020-03
3-05-020-04
3-05-020-05
3-05-020-06
3-05-020-07
3-05-020-08
3-05-020-09
3-05-020-10
3-05-020-11
3-05-020-12
3-05-020-13
3-05-020-14
3-05-020-15
3-05-020-16
3-05-020-20
Salt Mint tut
3-05-021-01
3-05-021-02
3-05-021-03
3-05-021-04
3-05-021-05
3-05-021-06
- Tertiary Crush/Screen 6.0BB
- Recrush/ Screening 5.0
- Fines Mill 6.088
- Miscellaneous Operation Screen/ 2.0
Convey /Handling
- Open Storage *0.33
- Cut Stone - General ,
- Blasting - General *0.16
- Drilling
- Hauling 52.0
- Drying *35.0
- Bar Grizzlies
- Shaker Screens
- Vibrating Screens
- Revolving Screens
- Drilling
- 1476
- General
- Granulation: Stack Dryer
- Filtration: Vacuum Filter
- Crushing
- Screening
- Conveying
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
002
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
•1.6
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
.004
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
*NEG
*0.
*0.
*0.
0
0
0
•0.0
*0.0
*0.0
*0
*0
*0
.0
.0
.0
Tons
Tons
Tons
Tons
Tons
Tons
Tons
Tons
Raw Material
Processed
Processed
Raw Material
Product Stored
Processed
Raw Material
Raw Material
Vehicle-Miles
Tons
Tons
Tons
Tons
Tons
Feet
Tons
Tons
Tons
Tons
Tons
Tons
Stone Dried
Processed
Processed
Processed
Processed
Drilled
Mined
Salt Granulated
Salt Produced
Salt Handled
Salt Handled
Salt Handled
220
285
192
192
192
Potash Production - 1474
3-05-022-01
3-05-022-99
- Mine - Grind/Dry
- Other Not Classified (Specify
in Comments)
0.
0
0.0
0
.0
0
.0
Tons
Tons
Ore
Processed
MaEnesium Carbonate - 1459
3-05-024-01
3-05-024-99
Sand/Gravel
3-05-025-02
3-05-025-03
3-05-025-04
3-05-025-05
3-05-025-06
3-05-025-07
3-05-025-08
3-05-025-09
- Mine/Process
- Other Not Classified (Specify
in Comments)
- 1442. 1446
- Aggregate Storage *0.33
- Material Transfer and Conveying 0.029
- Hauling 52.0
- Pile Forming: Stacker 0.13
- Bulk Loading 0.24
- Storage Piles 3,796.0
- Dryer
- Cooler
0.
0.
0.
0.
0.
0.
0.
*0.
0
0
0
0
0
0
0
002
*NEG
0.0
0.0
0.0
0.0
0.0
0.0
0.0
*1.6
*NEG
0
0,
0,
0,
.0
.0
.0
.0
0.0
0.0
0.0
*0.
004
0
0
0
0.
0,
0.
0.
.0
.0
.0
.0
.0
.0
.0
*0.0
Tons
Tons
Tons
Tons
Product
Processed
Product
Product
Vehicle-Miles
Tons
Tons
Acres
Tons
Tons
Product
Product
of Storage Area
Product Produced
Product Produced
220
304
*Refer to numbered notes in Appendix A or lettered notes in Appendix Bj factors without asterisks are from AP-42.
-------
sec
Process
PART
Lbs/Unit
SO
Lbs/finlt
NO
Lbs/finlt
VOC
Lbs/Unit
CO
Lbs/Unit
Units
Notes
Sand/Gravel - 1442, 1446 (Continued)
3-05-025-10 - Crushing
3-05-025-11 - Screening
Diatomaceous Earth - 1499. 3295
3-05-026-01 - Handling
3-05-026-99 - Other Not Classified (Specify
in Comments)
*0.0
*0.0
0.0
*0.0
*0.0
0.0
*0.0
•0.0
0.0
0.0
Tons Product Produced
Tons Product Produced
Tons Product
Tons Processed
192
192
CO
3-05-030-99 -
Other Not Classified (Specify
in Comments)
Tons
Processed
Asbestos Mininc - 1499
3-05-031-01 -
3-05-031-02 -
3-05-031-03 -
3-05-031-04 -
3-05-031-05 -
3-05-031-06 -
3-05-031-07 -
3-05-031-08 -
3-05-031-09 -
3-05-031-10 -
3-05-031-11 -
3-05-031-99 -
Asbestos Mill!
3-05-032-01 -
3-05-032-02 -
3-05-032-03 -
3-05-032-04 -
3-05-032-05 -
3-05-032-06 -
3-05-032-99 -
Vermiculite -
3-05-033-01 -
Surface Blasting
Surface Drilling
Cobbing
Loading
Convey/Haul Asbestos
Convey/Haul Waste
Unloading
Overburden Stripping
Ventilation of Process Operations
Stockpiling
Tailing Piles
Other Not Classified (Specify
in Comments)
n* - 1499
Crushing
Drying
Recrushing
Screening
Flberizing
Bagging
Other Not Classified (Specify
in Comments)
1499
General
Mining and Quarrying of Nonmetalllc Minerals . Except
3-05-040-01 -
3-05-040-02 -
3-05-040-03 -
Open Pit Blasting
Open Pit Drilling
Open Pit Cobbing
0.
0
0
0,
0
0
0
0,
0
0,
0.
0.
0.
0.
0.
0.
0.
*0.
Fuels - Soecifv
0.
0.
0.
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
,0
.0
.0
,0
0
.0
0
47
Material
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
.08
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
0
0
0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
*NEG
Tons
Tons
Tons
Tons
Tons
Tons
Tons
Tons
Tons
Tons
Tons
Tons
Tons
Tons
Tons
Tons
Tons
Tons
Tons
Tons
of Ore
of Ore
of Ore
of Ore
of Ore
of Ore
of Ore
Removed
of Ore
of Ore
of Material
Processed
Processed
Processed
Processed
Processed
Processed
Processed
Processed
Product 213
- 1400-1499
0
0
0
.0
.0
.0
0
0
0
.0
.0
.0
0
0
0
.0
.0
.0
Hundreds of Tons Material
Hundreds of Tons Material
Hundreds of Tons Material
*Refer to numbered notes in Appendix A or lettered notes In Appendix B; factors without asterisks are from AP-42.
-------
UD
sec
Process
PART SO
Lbs/Unit Lbs/8nit
Mining and Quarrying of Nonmetalllc Minerals. Except Fuels - Specify
3-05-0*0-10 -
3-05-0*0-20 -
3-05-0*0-21 -
3-05-0*0-22 -
3-05-0*0-23 -
3-05-0*0-2* -
3-05-0*0-25 -
3-05-0*0-30 -
3-05-0*0-31 -
3-05-040-32 -
3-05-040-33 -
3-05-0*0-3* -
3-05-0*0-36 -
3-05-040-99 -
Bulk Materials
3-05-100-01 -
3-05-100-02 -
3-05-100-03 -
3-05-100-04 -
3-05-100-05 -
3-05-100-06 -
3-05-100-07 -
Bulk Materials
3-05-101-01 -
3-05-101-02 -
3-05-101-03 -
3-05-101-04 -
3-05-101-05 -
3-05-101-06 -
3-05-101-07 -
3-05-101-08 -
3-05-101-96 -
3-05-101-97 -
3-05-101-98 -
3-05-101-99 -
Storage Bins -
3-05-102-01 -
3-05-102-02 -
3-05-102-03 -
Underground Ventilation
Loading
Convey /Haul Material
Convey/Haul Waste
Unloading
Stripping
Stockpile
Primary Crusher
Secondary Crusher
Ore Concentrator
Ore Dryer
Screening
Tailing Piles
Other Not Classified (Specify
in Comments)
Elevators (Specify Material Handled
Unloading
Loading
Removal from Bins
Drying
Cleaning
Elevator Legs (Headhouse)
Tripper (Gallery Belt)
Conveyors - 4463
Ammonium Sulfate
Cement
Coal
Coke
Limestone
Phosphate Rock
Scrap Metal
Sulfur
Chemical: Specify in Comments
Fertilizer: Specify in Comments
Mineral: Specify in Comnents
Other Not Classified (Specify
in Comments)
4*63
Ammonium Sulfate
Cement
Coal
0
0
0
0
0,
0
0
0.
0
0.
0
0,
0.
NO
Lbs/flnlt
voc
Lbs/Unit
CO
Lbs/Unit
Units
Notes
Material - 1*00-1*99 (Continued)
.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
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
Hundreds of Tons
Hundreds of Tons
Hundreds of Tons
Hundreds of Tons
Hundreds of Tons
Hundreds of Tons
Hundreds of Tons
Hundreds of Tons
Hundreds of Tons
Hundreds of Tons
Hundreds of Tons
Hundreds of Tons
Hundreds of Tons
Hundreds of Tons
Material
Material
Material
Material
Material
Material
Material
Material
Material
Material
Material
Material
Material
Material
in Comments) - 4*63
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.
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
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
0
0
0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
Tons Processed
Tons Processed
Tons Processed
Tons Processed
Tons Processed
Tons Processed
Tons Processed
Tons Processed
Tons Processed
Tons Processed
Tons Processed
Tons Processed
Tons Processed
Tons Processed
Tons Processed
Tons Processed
Tons Processed
Tons Processed
Tons Processed
Tons Processed
Tons Processed
Tons Processed
-------
PART SO^
SCC Process Lbs/Unit Lbs/Unit
Storage Bins - 4463 (Continued)
3-05-102-04 - Coke
3-05-102-05 - Limestone
3-05-102-06 - Phosphate Rock
3-05-102-07 - Scrap Metal
3-05-102-08 - Sulfur
3-05-102-96 - Chemical: Specify in Comments
3-05-102-97 - Fertilizer: Specify in Comments
3-05-102-98 - Mineral: Specify in Comments
3-05-102-99 - Other Mot Classified (Specify
in Comments)
Open Stockpiles - 4463
3-05-103-01 - Ammonium Sulfate
3-05-103-02 - Cement
3-05-103-03 - Coal
3-05-103-04 - Coke
3-05-103-05 - Limestone
3-05-103-06 - Phosphate Rock
3-05-103-07 - Scrap Metal
3-05-103-08 - Sulfur
Jn 3-05-103-96 - Chemical: Specify in Comments
3-05-103-97 - Fertilizer: Specify in Conments
3-05-103-98 - Mineral: Specify in Comments
3-05-103-99 - Other Mot Classified (Specify
in Conments)
Unloading Ooeration - 4463
3-05-104-01 - Ammonium Sulfate
3-05-104-02 - Cement
3-05-104-03 - Coal
3-05-104-04 - Coke
3-05-104-05 - Limestone
-05-104-06 - Phosphate Rock
-05-104-07 - Scrap Metal
-05-104-08 - Sulfur
-05-104-96 - Chemical: Specify in Comments
-05-104-97 - Fertilizer: Specify in Comments
-05-104-98 - Mineral: Specify in Comments
3-05-104-99 - Other Mot Classified (Specify
in Comments)
Loading Operation - 4463
3-05-105-01 - Ammonium Sulfate
3-05-105-02 - Cement
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
0.0
0.0
0.0
0.0
0.0
0.0
0.0
0.0
NO
Lbs/flnit
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
0.0
0.0
0.0
0.0
0.0
0.0
0.0
0.0
voc
Lbs/Unit
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
0.0
0.0
0.0
0.0
0.0
0.0
0.0
0.0
CO
Lbs/Unit
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
0.0
0.0
0.0
0.0
0.0
0.0
0.0
0.0
Units Notes
Tons Processed
Tons Processed
Tons Processed
Tons Processed
Tons Processed
Tons Processed
Tons Processed
Tons Processed
Tons Processed
Tons Processed
Tons Processed
Tons Processed
Tons Processed
Tons Processed
Tons Processed
Tons Processed
Tons Processed
Tons Processed
Tons Processed
Tons Processed
Tons Processed
Tons Processed
Tons Processed
Tons Processed
Tons Processed
Tons Processed
Tons Processed
Tons Processed
Tons Processed
Tons Processed
Tons Processed
Tons Processed
Tons Processed
Tons Processed
Tons Processed
-------
sec
PART SO NO VOC
Process Lbs/Unlt Lbs/unit Lbs/8nlt Lbs/Unlt
CO
Lbs/Unlt Units
Notes
Loading Operation - 4463 (Continued)
3-05-105-03
3-05-105-04
3-05-105-05
3-05-105-06
3-05-105-07
3-05-105-08
3-05-105-96
3-05-105-97
3-05-105-98
3-05-105-99
Calcining -
3-05-150-01
3-05-150-02
3-05-150-03
3-05-150-04
3-05-150-05
- Coal
- Coke
- Limestone
- Phosphate Rock
- Scrap Metal
- Sulfur
- Chemical : Specify In Comments
- Fertilizer: Specify In Comments
- Mineral: Specify In Comments
- Other Hot Classified (Specify
In Comments)
4463
- Raw Material Handling
- General
- Grinding /Mil ling
- Finished Product Handling
- Mixing
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
0.0 0.0 0.0
*0.0
•0.0
*0.0
*0.0
*0.0
0.0 Tons Processed
0.0 Tons Processed
0.0 Tons Processed
0.0 Tons Processed
0.0 Tons Processed
0.0 Tons Processed
0.0 Tons Processed
0.0 Tons Processed
0.0 Tons Processed
Tons Processed
Tons Throughput
Tons Throughput
Tons Throughput
Tons Throughput
Tons Throughput
90
90
90
90
90
Mineral Products - Fugitive Emissions
3-05-888-01
(7, 3-05-888-02
3-05-888-03
3-05-888-0*
3-05-888-05
- Specify In Comments Field
- Specify In Comments Field
- Specify In Comments Field
- Specify In Comments Field
- Specify In Comments Field
Tons Product
Tons Product
Tons Product
Tons Product
Tons Product
Mineral Products - Fuel Fired Equipment
Process Heaters
3-05-900-01 - Distillate Oil (No. 2)
3-05-900-02 - Residual Oil
3-05-900-03 - Natural Gas
*144.0 S
*159.0 S
•0.6
*20.0
*55.0
•140.0
*0.20
*0.28
•2.8
10 Gallons Burned
10 Gallons Burned
10 Cubic Feet Burned
129
129
129
Incinerators
3-05-900-11 - Distillate Oil (No. 2)
3-05-900-12 - Residual Oil
3-05-900-13 - Natural Gas
*0.4
*0.56
*5.6
10 Gallons Burned
10 Gallons Burned
10 Cubic Feet Burned
130
130
130
Flares
3-05-900-23 - Natural Gas
*5.6
10 Cubic Feet Burned
130
Mineral Products: Other Not Classified
3-05-999-99 - Specify In Comments
Tons Product
Refer to numbered notes In Appendix A or lettered notes in Appendix B; factors without asterisks are from AP-42.
-------
10
SCC Process
PETROLEUM INDUSTRY - MAJOR GROUP 29t>h
Process Heaters - 2911
3-06-001-03 - Oil Fired
3-06-001-04 - Gas Fired
3-06-001-05 - Natural Gas-Fired
3-06-001-06 - Process Gas-Fired
3-06-001-07 - LPG Fired
3-06-001-08 - Landfill Gas-Fired
3-06-001-99 - Other Not Classified
Fluid Catalytic Cracking Units (FCC) - 2911
3-06-002-01 - Fluid Catalytic Cracking Unit
3-06-002-02 - Catalyst Handling System
3-06-003-01 - Thermal Catalytic Cracking Unit
Slowdown Systems - 2911
3-06-004-01 - Slowdown System with Vapor
Recovery System with Flaring
3-06-004-02 - Slowdown System without Controls
FuKltlve Hydrocarbon Emissions from Petroleum
3-06-005-03 - Process Drains and Haste Hater
Separators
3-06-005-04 - Process Drains and Uaste Hater
Separators
3-06-005-05 - Haste Hater Treatment Plant
Excluding Separator
3-06-005-06 - Uaste Hater Treatment Plant
Excluding Separator
Vacuum Distillate Column Condensers - 2911
3-06-006-02 - Vacuum Distillation Column
Condsnsoir
3-06-006-03 - Vacuum Distillation Column
Condenser
Cooling Towers - 2911
3-06-007-01 - Cooling Towers
3-06-007-02 - Cooling Towers
Fugitive Hydrocarbon En»i««t.>ns from Petroleum
3-06-008-01 - Pipeline Valves and Flanges
3-06-008-02 - Vessel Relief Valves
3-06-008-03 - Pump Seals (Without Controls)
PART
Lbs/Unlt
K
•12.0 S
3.0
3.0
3.0
0.27
242.0
17.0
0.0
0.0
Refinlns, - 2911
0.0
0.0
0.0
0.0
0.0
0.0
0.0
0.0
Reflnln. - 2911
0.0
0.0
0.0
SO
Lbs/Unlt
159.0 S
•950.0 S°
0.6
•950.0 S°
•86.5 S°
493.0
60.0
26.9
0.0
0.0
0.0
0.0
0.0
0.0
0.0
0.0
0.0
0.0
0.0
0.0
NO
Lbs/Unlt
55.0
140.0
140.0
140.0
12.8
71.0
5.0
18.9
0.0
0.0
0.0
0.0
0.0
0.0
0.0
0.0
0.0
0.0
0.0
0.0
voc
Lbs/Unlt
0.3
2.8
2.8
2.8
0.26
•2.8
11
140.8
•NEG
55. 7"
0.8
580.0
5.0
200.0
•0.04
•0.77
50.0
18.0
6.0
10.0
16.3
2.9
4.1
CO
Lbs/Unlt
5.0
35.0
35.0
35.0
3.2
II
13,700.0
it
3,800.0
4.3
0.0
0.0
0.0
0.0
0.0
0.0
0.0
0.0
0.0
0.0
0.0
0.0
Units
3
10 Gallons Oil Burned
10 Cubic Feet Burned
10 Cubic Feet Burned
10 Cubic Feet Burned
10, Gallons Burned
10 Cubic Feet Burned
Gallons Heated
10* BBLs. Fresh Feed
10 BBLs. Fresh Feed
10 BBLs. Fresh Feed
3 _ .
10 BBLs. Refinery Feed
3
10 BBLs. Refinery Feed
103 Gallons Uaste Hater
103 BBLs. Refinery Feed
103 Gallons Uaste Hater
103 BBLs. Refinery Feed
.
10 BBLs. Vacuum Feed
3
10 BBLs. Refinery Feed
10* Gallons Cooling Hater
10 BBLs. Refinery Feed
10 BBLs. Refinery Feed
10 BBLs. Refinery Feed
10 BBLs. Refinery Feed
Notes
129
285
98
99
*Refer to numbered notes In Appendix A or lettered notes In Appendix B; factors without asterisks are from AP-42.
-------
CO
SCC Process
Fugitive Hydrocarbon Emissions from Petroleum
3-06-008-04 - Compressor Seals
3-06-008-05 - Miscellaneous: Sampling/
Non-Asphalt Blowing, Purging, et
3-06-008-06 - Pump Seals (With Controls)
3-06-008-07 - Blind Changing
Pioellne Valves - 2911JJ
3-06-008-11 - Gas Streams
3-06-008-12 - Light Liquid/Gas Stream
3-06-008-13 - Heavy Liquid Streaa
3-06-008-14 - Hydrogen Streams
3-06-008-15 - Open-ended Valves (All Streams)
3-06-008-16 - Flanges (All Streams)
3-06-008-17 - Pump Seals (Liquid/Gas Stream)
3-06-008-18 - Pump Seals (Heavy Liquid Stream)
3-06-008-19 - Compressor Seals (Gas Streams)
3-06-008-20 - Compressor Seals (Heavy Liquid
Stream)
3-06-008-21 - Drains (All Streams)
3-06-008-22 - Vessel Relief Valves (All Streaa
Flares - 2900-2999
3-06-009-03 - Natural Gas
3-06-009-04 - Process Gas
Sludge Converter - 2999
3-06-010-01 - General
Asohalt Bloving - 2911
3-06-011-01 - Asphalt Blowing
Fluid Coking Units - 2911
3-06-012-01 - Fluid Coking Units
Petroleum Coke Calcining - 2911
3-06-014-01 - Coke Calciner
Bauxite Burning
3-06-015-99 - Other Not Classified (Specify
in Comments)
3-06-099-11 - Distillate Oil (No. 2)
3-06-099-12 - Residual Oil
PART
Lbs/Unlt
Refining - 2911
0.0
0.0
c.
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
is) 0.0
d
*523.0
SO
Lbs/Unlt
(Continued)
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
*15
NO
Lbs/Unlt
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
•1.2
voc
Lbs/Unlt
3.7
10.0
4.1
0.3
516.84
210.24
4.38
157.68
43.8
4.9
2,190.0
402.96
12,264.0
963.6
613.2
3,153.6
*5.6
•5.6
*0.2
60.0
*16
*0.8
*0.4
•0.56
CO
Lbs/Unlt
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
Units
3
1(T BBLs. Refinery Feed
10 BBLs. Refinery Feed
10* BBLs. Refinery Feed
10 BBLs. Refinery Feed
Valves In Operation
Valves In Operation
Valves In Operation
Valves In Operation
Valves in Operation
Valves in Operation
Seals In Operation
Seals In Operation
Seals In Operation
Seals in Operation
Drains in Operation
Valves in Operation
£
10£ Cubic Feet Burned
10 Cubic Feet Burned
Tons Processed
Tons of Asphalt
3
10 BBLs . Fresh Feed
Tons Raw Coke
Tons Bauxite Used
10 Gallons Burned
10 Gallons Burned
Notes
130
130
143
1 LI 1 71
LHJ p If*.
1 Ifl
J. JO
130
130
*Refer to numbered notes In Appendix A or lettered note, In Appendix B; factors without asterisks are fro. AP-42.
-------
10
PART SO NO
SCC Process Lbs/Unit Lbs/Unit Lbs/Dnit
Incinerators - 2900-2999 (Continued)
3-06-099-13 - Natural Gas
3-06-099-14 - Process Gas
Lube Oil Refining - 2922
3-06-100-01 - General
Petroleum Industry - Fugitive Emi »«««««
3-06-888-01 - Specify In Comments Field
3-06-888-02 - Specify In Comments Field
3-06-888-03 - Specify In Consents Field
3-06-888-04 - Specify In Cements Field
3-06-888-05 - Specify In Coonents Field
PULP AND PAPER INDUSTRY - MAJOR GROUPS 24, 25. 26. 27
Sulfate (Kraft) Pulping - 2611. 2621. 2631 (For Bark Boilers. See Industrial Boilers)
3-07-001-01 - Digester Relief and Blow Tank 0.0 0.0 *0.0
3-07-001-02 - Washers /Screens 0.0 0.01 *0.0
3-07-001-03 - Multi-Effect Evaporator 0.0 0.01 *0.0
j
3-07-001-04 - Recovery Furnace/Direct Contact 180 7 *1.0
Evaporator
3-07-001-05 - Smelt Dissolving Tank 7 0.2 *2.9
J
3-07-001-06 - Lime Kiln 56 0.3 *1.0
3-07-001-07 - Turpentine Condenser 0.0 0.0 0.0
j
3-07-001-08 - Fluid Bed Calclner *72.0 *0.3 *1.0
3-07-001-09 - Liquor Oxidation Tower *0.02 *0.0
3-07-001-10 - Recovery Furnace /Indirect Contact 230 *1.5 *2.0
Evaporator
3-07-001-99 - Other Not Classified (Specify •
in Comments)
Sulfite Pulping - 2611. 2621. 2631
3-07-002-03 - Digester/Blow Pit/Dump Tank NEC 40.0 *0.0
(All Bases Except Ca)
3-07-002-11 - Digester/Blow Pit/Dump Tank (Ca) NEC 67.0 *0.0
VOC CO
Lbs/Unit Lbs/Unit Units
6
*5.6 10 Cubic Feet Burned
•5.6 10 Cubic Feet Burned
103 BBL. Lube Oil
103 BBL. Refinery Feed
10 BBL. Refinery Feed
10* BBL. Refinery Feed
10* BBL. Refinery Feed
10 BBL. Refinery Feed
*0.0 0.0 Air-Dry Tons Unbleached
Pulp
*0.2 0.0 Air-Dry Tons Unbleached
Pulp
•0.0 0.0 Air-Dry Tons Unbleached
Pulp
*1.95 11 Air-Dry Tons Unbleached
Pulp
*0.16 0.0 Air-Dry Tons Unbleached
Pulp
*0.25 0.1 Air-Dry Tons Unbleached
Pulp
*0.07 0.0 Air-Dry Tons Unbleached
Pulp
*0.25 Air-Dry Tons Unbleached
Pulp
*0.4S Air-Dry Tons Unbleached
Pulp
*0.8 11 Air-Dry Tons Unbleached
Pulp
Air-Dry Tons Unbleached
Pulp
*NEG Air-Dry Tons Unbleached
Pulp
*NEG Air-Dry Tons Unbleached
Pulp
Notes
130
130
-
172
207, 257
172
154, 298,
299, 302
207, 209,
298, 299
153, 298,
302
207
266
115, 152,
257
154, 173,
298, 302
257, 298,
320
257, 298,
320
Refer to numbered notes in Appendix A or lettered notes in Appendix B; factors without asterisks are from AP-42.
-------
SCC Process
Sulfite Pulping - 2611. 2621. 2631 (Continued)
3-07-002-12 - Digester/Blow Pit/Dump Tank
(MgO with Recovery System)
3-07-002-13 - Digester/Blow Pit/Dump Tank (MgO
with Process Change and Scrubber)
3-07-002-14 - Digester/Blow Pit/Dump Tank (NH
with Process Change and Scrubber)
3-07-002-15 - Digester/Blow Pit/Dump Tank (Ma
with Process Change and Scrubber)
3-07-002-21 - Recovery System (MgO)
3-07-002-22 - Recovery System (NH)
3-07-002-23 - Recovery System (Ha)
3-07-002-31 - Acid Plant (NH,)
3
3-07-002-32 - Acid Plant (Ha)
3-07-002-33 - Acid Plant (Ca)
t-»
O 3-07-002-34 - Other Miscellaneous Sources:
Knotters /Washers /Screens, etc.
Neutral Sulfite Semichemlcal Pulping - 2611. 2621.
3-07-003-01 - Digester /Dump Tank/Blow Pit
3-07-003-02 - Evaporator
3-07-003-03 - Fluid Bed Reactor
3-07-003-04 - Sulfur Burner/Absorbers
Pulpboard Manufacture - 2631. 2661
3-07-004-01 - Paperboard: General
3-07-004-02 - Fiberboard: General
3-07-005-01 - Creosote
3-07-005-97 - Other Not Classified (Specify
in Comments)
3-07-005-98 - Other Not Classified (Specify
in Comments)
3-07-005-99 - Other Not Classified (Specify
in Comments)
PART SO NO
Lbs/Unit Lbs/flnit Lbs/8nit
NEC 0.0 »0 . 0
NEC 0.2 *0.0
NEC 0.4 *0.0
NEC 2.0 *0.0
*0.0
*0.0
*0.0
*0.0
*0.0
•0.0
0.0 12.0 *0.0
2531 (For Bark Boilers. See Industrial
*0.2 *0.0
*0.01 *0.0
*1.0
*20.0 *0.0
0.0
0.6
VOC
Lbs/Unit
•NEC
*NEG
*NEG
*NEG
*3.5
*3.5
*3.5
*0.0
*0.0
*0.0
*NEG
Boilers)
*NEG
*NEG
*0.25
*NEG
*0.2
*2.5
*NEG
CO
Lbs/Unit Units
Air-Dry Tons Unbleached
Pulp
Air-Dry Tons Unbleached
Pulp
Air-Dry Tons Unbleached
Pulp
Air-Dry Tons Unbleached
Pulp
Air-Dry Tons Unbleached
Pulp
Air-Dry Tons Unbleached
Pulp
Air-Dry Tons Unbleached
Pulp
Air-Dry Tons Unbleached
Pulp
Air-Dry Tons Unbleached
Pulp
Air-Dry Tons Unbleached
Pulp
Air-Dry Tons Unbleached
Pulp
Air-Dry Tons Unbleached
Pulp
Air-Dry Tons Unbleached
Pulp
Air-Dry Tons Unbleached
Pulp
Air-Dry Tons Unbleached
Pulp
Tons Finished Product
Tons Finished Product
Tons Wood Treated
10 Cubic Feet
3
10 Board Feet
Tons Wood Treated
Notes
257, 298
320
257, 320
257, 320
257, 320
151, 257
151, 257
151, 257
257, 350
257, 350
257, 350
257, 320
116, 259
259
79
116, 259
143
28
265
Refer to numbered notes in Appendix A or lettered notes in Appendix B; factors without asterisks are from AP-42.
-------
sec
Process
PART
Lbs/Unit
SO
Lbs/Unit
NO
Lbs/finit
VOC
Lbs/Unit
Plywood/Part Icleboard Operations - 2435. 2436. 2492
3-07-007-01 -
3-07-007-02 -
3-07-007-03 -
3-07-007-0* -
3-07-007-05 -
3-07-007-06 -
3-07-007-07 -
3-07-007-08 -
3-07-007-09 -
3-07-007-11 -
3-07-007-12 -
3-07-007-13 -
3-07-007-1* -
3-07-007-15 -
3-07-007-98 -
3-07-007-99 -
General: Not Classified
Sanding Operations
Particleboard Drying
Waferboard Dryer
Hardboard: Coe Dryer
Hardboard: Predryer
Hardboard: Pressing
Hardboard: Tempering
Hardboard: Bake Oven
Fir-Sapwood-Steam Fired Dryer
Flr-Sapwood-Gas Fired Dryer
Fir-Heartwood Plywood Veneer Dryer
Larch Plywood Veneer Dryer
Southern Pine Plywood Veneer Dryer
Other Not Classified (Specify
in Comments)
Other Not Classified (Specify
in Comments)
4.25
0.6
*859.0
4.64
2.37
3.18
4.1*
3.7
0.0
0.0
*17
*NEG
*NEG
•0.0
•0.0
•0.0
*0.0
*0.0
•0.0
•0.0
*0.0
0.0
0.0
*114
*0.3
*0.3
*NEG
*NEG
*0.1
Sawmill Operations - 2421. 2426. 2429
3-07-008-01 -
3-07-008-02 -
3-07-008-03 -
3-07-008-0* -
3-07-008-05 -
3-07-008-06 -
3-02-008-07 -
3-07-008-08 -
3-07-008-96 -
3-07-008-97 -
3-07-008-98 -
3-07-008-99 -
3-07-011-99 -
Log Debarking
Log Sawing
Sawdust Pile Handling
Sawing: Cyclone Exhaust
Planning/Trimming: Cyclone
Exhaust
Sanding: Cyclone Exhaust
Sanderdust: Cyclone Exhaust
Other Cyclones: Exhaust
Other Not Classified (Specify
in Comments)
Other Not Classified (Specify
in Comments)
Other Not Classified (Specify
in Comments)
Other Not Classified (Specify
in Comments)
and Glazln* - 2641. 2642. 2643. 2651
Extrusion Coating Line
Applications of Solvent Free
Resin or Wax)
0.02
0.35
1.0
2.25U
4.0U
5.0
2.0
. 2654. 2655.
*0.0
*0.0
•0.0
0.0
0.0
0.0
0.0
0.0
2661
*0.0
*0.0
*0.0
0.0
0.0
0.0
0.0
0.0
1.52
0.0
0.0
*409
*1
*1
*1.45
*NEG
*0.003
0.45
7.53
1.3
0.19
2.9*
*NEG
*NEG
*NEG
0.0
0.0
0.0
0.0
0.0
CO
Lbs/Unit Units
L
10 Sq. Ft. 3/8" Plywood
0.0 Tons Processed
0.0 Tons Processed
10 Lbs. Wafers/Chips
Dried
Tons of Dry Product
Tons of Dry Product
Tons of Dry Product 175,
Tons of Dry Product
Tons of Product
10 Sq. Ft. 3/8" Plywood
10* Sq. Ft. 3/8" Plywood
10 Sq. Ft. 3/8" Plywood
10* Sq. Ft. 3/8" Plywood
10 Sq. Ft. 3/8" Plywood
10 Board Feet
Tons Processed
Tons of Logs Processed
Tons of Logs Processed
Tons of Sawdust
0.0 SCFM Average Airflow
0.0 SCFM Average Airflow
0.0 SCFM Average Airflow
0.0 Hours of Operation
0.0 Hours of Operation
10 Cubic Feet
Gallons
3
10 Board Feet
Tons Processed
Tons Res in/ Wax Consumed
Notes
121, 123
174, 330
330
271, 330
271, 351
271, 330
271
271
271
271
271
260
260
260
*Refer to numbered notes in Appendix A or lettered notes in Appendix B; factors without asterisks are from AP-42.
-------
sec
Process
PART
Lbs/Unlt
SO
Lbs/unlt
NO
Lbs/Unlt
VOC
Lbs/Unlt
CO
Lbs/Unit
Units
Notes
CD
f\J
Miscellaneous Paper Products - 2649
3-07-013-01 - Shredding Newspaper for Insulation
Manufacture
3-07-013-99 - Other Mot Classified (Specify
In Coanents)
Furniture Manufacturing - 2500-2599alB>
3-07-020-98 - Other Not Classified (Specify
In Coanents)
3-07-020-99 - Other Not Classified (Specify
In Cooxnents)
*12.0
Miscellaneous
3-07-030-01 -
3-07-030-02 -
3-07-030-96 -
3-07-030-97 -
3-07-030-98 -
3-07-030-99 -
Wood Products
3-07-888-01 -
3-07-888-02 -
3-07-888-03 -
3-07-888-04 -
3-07-888-05 -
3-07-888-98 -
Woodworking Ooeratlons - 2*21. 2*26. 2*29. 2*31.
Wood Waste Storage Bin Vent 1.0
Wood Waste Storage Bin Loadout 2.0
Sanding /Planning Operations
(Specify In Coanents)
Sanding/Planning Operations
(Specify in Coanents)
Sanding/Planning Operations
(Specify in Coanents)
Sanding/Planning Operations
(Specify in Coanents)
- Fucitive Emissions
Specify in Coanents Field
Specify in Coanents Field
Specify in Coanents Field
Specify in Coanents Field
Specify In Coanents Field
Specify in Coanants Field
243*. 24391
0.0
0.0
0.0
0.0
0.0
0.0
Wood Products - Fuel Fired Equipment
Process Heaters
0.0
0.0
0.0
0.0
0.0
0.0
0.0
0.0
0.0
0.0
0.0
0.0
Tons Newspaper Shredded
Tons Processed
10 Board Feet
Tons Processed
0.0
0.0
0.0
0.0
0.0
0.0
Tons Wood Waste
Tons Wood Waste
10 Square Feet
Each
10 Board Feet
Tons Processed
Tons Product
Tons Product
Tons Product
Tons Product
TODS Product
10 Board Feet
120
3-07-900-01 -
3-07-900-02 -
3-07-900-03 -
Incinerators
3-07-900-12 -
3-07-900-13 -
Flares
3-07-900-23 -
Distillate Oil (No. 2)
Residual Oil
Natural Gas
Residual Oil
Natural Gas
Natural Gas
•144.0 S *20.0 *0.20
•159.0 S *55.0 *0.28
•0.6 M40.0 *2.8
*0.56
*5.6
*5.6
10 Gallons Burned
10 Gallons Burned
10 Cubic Feet Burned
10 Gallons Burned
10 Cubic Feet Burned
6
10 Cubic Feet Burned
129
129
129
130
130
130
Refer to numbered notes In Appendix A or lettered notes In Appendix B; factors without asterisks are from AP-42.
-------
801
30
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-------
sec
Process
PART
Lbs/Unit
SO
Lbs/finit
NO
Lbs/finit
VOC
Lbs/Unit
CO
Lbs/Unit
Units
Notes
Fiberglass Resin Products (Continued)
3-08-007-22 - Gel Coat-Spray On
3-08-007-23 - Resin-General-Roll On
3-08-007-24 - Resin-General-Spray On
Fabricated Plastics Products - 3079
3-08-007-99 - Other Not Classified (Specify
in Comments)
Rubber and Miscellaneous Plastics Products - Fuel Fired Eau
*600
*500
•220
Tons Coating Applied
Tons Coating Applied
Tons Coating Applied
Tons Product
288
288
288
Process Heaters
3-08-900-01 - Distillate Oil (No. 2)
3-08-900-02 - Residual Oil
3-08-900-03 - Natural Gas
Incinerators
3-08-900-11 - Distillate Oil (No. 2)
3-08-900-12 - Residual Oil
3-08-900-13 - Natural Gas
*144.0 S
•159.0 S
•0.6
*20.0
•55.0
*140.0
*0.20
•0.28
*2.8
•0.4
•0.56
•5.6
10 Gallons Burned
10 Gallons Burned
10 Cubic Feet Burned
10 Gallons Burned
10 Gallons Burned
10 Cubic Feet Burned
129
129
129
130
130
130
Flares
3-08-900-23 - Natural Gas
•5.6
10 Cubic Feet Burned
130
Rubber and Plastics: Other Not Classified
3-08-999-99 - Specify in Comments
FABRICATED METAL PRODUCTS - MAJOR GROUP 34 AND 50
Tons Processed
General Processes
3-09-001-98 - Other Not Classified (Specify
in Comments)
Gallons
- utner not 01 as six lea opecny
in Comments)
ions
i
Abrasive Blasting of Metal Parts
3-09-002-01
3-09-002-02
3-09-002-03
3-09-002-04
3-09-002-05
3-09-002-07
3-09-002-08
3-09-002-98
3-09-002-99
- General
- Sand Abrasive
- Slag Abrasive
- Garnet Abrasive
- Steel Grit Abrasive
- Shotblast with Air
- Shotblast without Air
- General
- General
0
0
0
0,
0.
u .
0.
0.
.0
.0
.0
.0
.0
. 0
0
o
0.0
0.0
0.0
0.0
0.0
0 . u
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
Tons
Tons
Tons
Tons
Tons
Tons
Tons
Abrasive
Abrasive
Abrasive
Abrasive
Abrasive
Consumed
Consumed
Consumed
Consumed
Consumed
Shot Consumed
Shot Consumed
Linear Feet
0.
0
0.0
0,
.0
0.
0
Each
Refer to numbered notes in Appendix A or lettered notes in Appendix B; factors without asterisks are from AP-42.
-------
o
en
PART
SCC Process Lbs/Unit
Abrasive Cleaning of Metal Parts
3-09-003-01 - Brush Cleaning
3-09-003-02 - Tumble Cleaning
3-09-003-03 - Polishing
3-09-003-04 - Buffing
Electroplating Operations - 3471
3-09-010-01 - General: Entire Process
3-09-010-97 - Other Hot Classified (Specify
in Comments)
3-09-010-98 - Other Hot Classified (Specify
in Comnents)
Conversion Coat Inn of Metal Products - 3471
3-09-011-01 - Alkaline Cleaning Bath
3-09-011-02 - Acid Cleaning Bath (Pickling)
3-09-011-03 - Anodizing Kettle
3-09-011-04 - Rinsing/Finishing
3-09-011-99 - Other Hot Classified (Specify
in Comnents)
Chemical Mi Ulna of Metal Parts - 3471
3-09-015-01 - Milling Tank
Metal Pine Coatiiu with Asohalt/Coal Tar - 3479
SO
Lbs/finit
•NEC
•NEC
*NEG
•NEG
*0.0
*NEG
*0.6
*NEG
*NEG
NO
Lbs/5nlt
•NEC
•NEC
•NEC
•NEC
•0.009
•0.3
•13
•0.2
•8.0
•160
VOC
Lbs/Unit
•NEC
•NEC
•NEC
•HEG
•0.026
•0.0
•0.0
•0.0
•100
•0.0
CO
Lbs/Unit Units
Tons Abrasive Consumed
Tons Abrasive Consumed
Tons Abrasive Consumed
Tons Abrasive Consumed
Square Feet of Product
Plated
Tons Makeup
Gallons
Tons Processed 149,
Tons Processed 149,
Tons Processed 141,
Tons Processed 143,
Gallons
Tons Processed
Notes
262
262
262
262
122, 230
273, 317
273, 347
273, 317
147, 317
3, 141
3-09-016-04 - Coal Tar/Asphalt Melting Kettle
3-09-016-05 - Asphalt Dipping
3-09-016-06 - Pipe Spinning
3-09-016-07 - Pipe Wrapping
Drum Cleaning/Reclamation - 5085
3-09-025-01 - Drum Burning Furnace
0.035
*0.002
*1.5
*NEG
*13
*13
*13
0.002
Tons Coating Melted
10 Sq. Ft. Pipe Processed
10 * Sq. Ft. Pipe Processed
10 Sq. Ft. Pipe Processed
Drums Burned
370
370
370
371
Machining Operations
3-09-030-05 - Sawing (Specify Material)
3-09-030-06 - Boning (Specify Material)
Tons Processed
Tons Processed
Metal Deposition Processes
3-09-040-01 - Metallizing (Wire Atomizatlon
3-09-040-10
3-09-040-20
and Spraying)
- Thermal Spraying of Powdered Metal
- Plasma Arc Spraying of Powdered
Metal
*0.0 *NEG *340 Tons Sprayed Metal
Consumed
*0.0 *0.0 *0.0 Tons Sprayed Metal
Consumed
*0.0 *0.0 *130 Tons Sprayed Metal
Consumed
143, 283
282
261
*Refer to numbered notes in Appendix A or lettered notes in Appendix B; factors without asterisks are from AP-42.
-------
sec
Process
PART
Lbs/Unit
SO
Lbs/unit
NO
Lbs/finit
VOC
Los/Unit
CO
Lbs/Unit
Units
Notes
Porcelain Enamel and Ceramic Glaze Spraying - 3431
3-09-060-01 - Spray Booth
3-09-060-99 - Spray Booth
Fabricated Metals - Fu»ltl\
Emissions
3-09-888-01 - Specify In Commit* Field
3-09-888-02 - Specify in Coments Field
3-09-888-03 - Specify in Comments Field
3-09-888-04 - Specify in Comments Field
3-09-888-05 - Specify in Comments Field
Fabricated Metal Products - Fuel Fired Equipment
Gallons Wet Slurry
Sprayed
Tons Processed
Tons Product
Tons Product
Tons Product
Tons Product
Tons Product
Process Heaters
3-09-900-01 - Distillate Oil (No. 2)
3-09-900-02 - Residual Oil
3-09-900-03 - Natural Gas
*144.0 S
*159.0 S
*0.6
*20.0
•55.0
•140.0
*0.20
*0.28
*2.8
10 Gallons Burned
10 Gallons Burned
10 Cubic Feet Burned
129
129
129
O
(Ti
Incinerators
3-09-900-11 - Distillate Oil (No. 2)
3-09-900-12 - Residual Oil
3-09-900-13 - Natural Gas
*0.4
*0.56
*5.6
10 Gallons Burned
10, Gallons Burned
10 Cubic Feet Burned
130
130
130
Flares
3-09-900-23 - Natural Gas
Fabricated Metal Products-. Other Hot Classified
3-09-999-97 - Other Not Classified (Specify
in Comments)
3-09-999-98 - Other Not Classified (Specify
in Comments)
3-09-999-99 - Other Hot Classified (Specify
in Comments)
OIL AND GAS PRODUCTION - MAJOR GROUP 13
Crude Oil Production - 1311
3-10-001-01 - Complete Well: Fugitive Emissions
^-10-001-02 - Miscellaneous Uells! General
3-10-001-03 - Wells-Rod Pump*
3-10-001-04 - Crude Oil Sumps
3-10-001-05 - Crude Oil Pits
3-10-001-99 - Processing Operations: Not
Classified (Specify in Comments)
*5.6
*396
*2SC
•455
*9
*9
10 Cubic Feet Burned
10 Pieces Processed
10 Pieces Processed
Tons Processed
Wells/Year In Operation
Wells/Yesr In Operation
Wells/Year in Operation
Sq. Ft. Sump Area/Year
Sq. Ft. Pit Area/Year
10 BBLs. Produced
130
3
62
62
*Refer to numbered notes in Appendix A or lettered notes in Appendix B; factors without asterisks are from AP-42.
-------
O
-O
sec
Natural Gas
3-10-002-01
3-10-002-02
3-10-002-03
3-10-002-04
3-10-002-05
3-10-002-06
3-10-002-07
3-10-002-99
Process
Production - 1311
- Gas Sweeting (Amine Process)
(Smokeless Flares/Tail Gas
Incinerators)
- Gas Stripping Operations
- Compressors
- Wells
- Flares
- Gas Lift
- Valves (Fugitive Emissions)
- Other Not Classified (Specify
PART SO NO VOC
Lbs/Unlt Lbs/Unit Lbs/Unit Lbs/Unit
0.0 1685.0 S°° 0.0 0.0
*310 *6.0
*6.0
*35
*5.6
*6.0
CO
Lbs/Unit Units
g
0.0 10 Cubic Feet of Sour
Processed
g
10 Cubic Feet of Gas
Produced
10 Cubic Feet of Gas
Produced
10 Cubic Feet of Gas
Produced
10 Cubic Feet of Gas
Produced
10 Cubic Feet of Gas
Produced
Lbs/Year
10 Cubic Feet of Gas
Notes
146, 369
63
7
130
369
in Comments)
Oil and Gas Production - Fuel Fired Equipment
Produced
Process Heaters
3-10-004-01
3-10-004-02
3-10-004-03
3-10-004-04
3-10-004-05
- Distillate Oil
- Residual Oil
- Crude Oil
- Natural Gas
- Process Gas
2.
•12.
*12.
3.
3.
0 .
°Sb
o sb
0
0
144.
159.
159.
0.
*950.
0
0
0
6
0
s
s
s
sc
20.0
55.0
55.0
140.0
140.0
0
0
0
2
2
.20
.28
.28
.8
.8
5.0
5.0
5.0
35.0
35.0
Steam Generators
3-10-004-11
3-10-004-12
3-10-004-13
3-10-004-14
3-10-004-15
Oil and Gas
3-10-888-01
3-10-888-02
3-10-888-03
3-10-889-04
3-10-888-05
- Distillate Oil
- Residual Oil
- Crude Oil
- Natural Gas
- Process Gas
f
Production - Fugitive Emissions
- Specify in Comments Field*
- Specify in Comments Field*
- Specify in Comments Field*
- Specify in Comments Field*
- Specify in Comments Field*
2.
•12.
*12.
3.
3.
o .
osh
o sb
0
0
144.
159.
159.
0.
*950.
0
0
0
6
0
s
s
s
sc
20.0
55.0
55.0
140.0
140.0
0
0
0
2
2
.20
.28
.28
.8
.8
5.0
5.0
5.0
35.0
35.0
3
10 Gallons Burned
10 Gallons Burned
10 Gallons Burned
10, Cubic Feet Burned
10 Cubic Feet Burned
10 Gallons Burned
10 Gallons Burned
10 Gallons Burned
10 Cubic Feet Burned
10 Cubic Feet Burned
Process Unit /Year
Process Unit/Year
Process Unit/Year
Process Unit/Year
Process Unit/Year
*Note that fugitive emissions are reported in units of Ibs/process unit-year rather than lbs/10 BB1. feed produced as in the NEDS Source
Classification Codes and Emission Factor Listing dated October 1985.
*Refer to numbered notes in Appendix A or lettered notes in Appendix B; factors without asterisks are from AP-A2.
-------
o
CO
PART :,0 NO VOC
scc Process Lbs/Unlt Lbs/dnlt Lbs/finlt Lbs/Unlt
BUILDING CONSTRUCTION - MAJOR GROUP 15
Construction: Building Contractors
3-11-001-99 - Other Not Classified (Specify
In Comments)
Construction: Special Trade Contract
3-11-002-99 - Other Not Classified (Specify
In Comments)
MACHINERY. MISCELLANEOUS - MAJOR GROUP 25
Miscellaneous Machinery
3-12-999-99 - Other Not Classified (Specify
In Comments)
ELECTRICAL EQUIPMENT - MAJOR GROUP 76
Electrical Windings Reclamation - 7694
3-13-070-01 - Single Chamber Incinerator/Oven *2.5 *950
3-13-070-02 - Multiple Chamber Incinerator/Oven *2.5 *0.1 *190
Electrical Equipment - Fuel Fired Equipment
Process Heaters
3-13-900-01 - Distillate Oil (No. 2) *144.0 S *20.0 *0.20
3-13-900-02 - Residual Oil *159.0 S *55.0 *0.28
3-13-900-03 - Natural Gas *0.6 *140.0 *2.8
Miscellaneous Electrical Equipment
3-13-999-99 - Other Hot Classified (Specify
In Comments)
TRANSPORTATION EQUIPMENT - MAJOR GROUP 37. 50, 75
Automobile/Truck Assembly Operations - 3711. 3713
3-14-009-01 - Solder Joint Grinding 0.0 0.0 0.0
Brake Shoe Debondlng - 7539
3-14-010-01 - Single Chamber Incinerator *2.5 *950
3-14-010-02 - Multiple Chamber Incinerator *2.5 *190
Auto Body Shredding. - 5093
3-14-011-01 - Primary Metal Recovery Line *NEG *NEG *NEG
3-14-011-02 - Secondary Metal Recovery Line *NEG *NEG *NEG
CO
Lbs/Unlt Units
Acres of Construction
Activity
Acres of Construction
Activity
Tons Processed
Tons Charged
Tons Charged
10 Gallons Burned
10 Gallons Burned
10 Cubic Feet Burned
Tons Processed
0.0 Number of Vehicles
Tons Charged
Tons Charged
Tons Scrap Processed
Tons Scrap Processed
Notes
92
141, 143
129
129
129
92
92
262
262
Refer to numbered notes In Appendix A or lettered notes In Appendix B; factors without asterisks are from AP-42.
-------
sec
Process
PART
Lbs/Unit
SO
Lbs/flnlt
NO
Lbs/dnit
VOC
Lbs/Unit
CO
Lbs/Unit
Units
Notes
O
10
Miscellaneous Transportation Equipment
3-14-999-99 - Other Hot Classified (Specify
in Comments)
PHOTOGRAPHIC EQUIPMENT - MAJOR GROUP 38
Photocopying Equipment Manufacture - 3861
3-15-010-01 - Resin Transfer/Storage
3-15-010-02 - Toner Classification
3-15-010-03 - Toner (Carbon Black) Grinding
HEALTH SERVICES - MAJOR GROUP 80
Hospitals - 8062
3-15-020-01 - Sterilization with Ethylene
Oxide
LEATHER AND LEATHER PRODUCTS - MAJOR GROUP 31
Leather and Leather Products - 3111-3199
3-20-999-97 - Other Hot Classified (Specify
in Comments)
3-20-999-98 - Other Not Classified (Specify
in Comments)
3-20-999-99 - Other Not Classified (Specify
in Comments)
TEXTILE PRODUCTS - MAJOR GROUPS 22 AND 30
•NEC
*630
*NEG
*2000
•19
Tons Processed
10, Pounds Resin
10 Pounds Toner
10 Pounds Toner
Tons Ethylene Oxide
Consumed
10 Square Feet
Gallons
Tons Processed
285
143
285
64
123
Miscellaneous General Fabric Operations - 2261. 2262. 2281-2284. 2294. 2297. 2299
3-30-001-01
3-30-001-02
3-30-001-03
3-30-001-04
3-30-001-05
3-30-001-98
3-30-001-99
- Yarn Preparation/Bleaching
- Printing1*1*
- Polyester Thread Production
- Tenter Frames: Heat Setting
- Carding
- Other Not Classified (Specify
in Cooments)
- Other Not Classified (Specify
in Comments)
*NEG Tons Fabric Processed
*284 Tons Fabric Processed
*NEG Tons Fabric Processed
•0.47 Tons Fabric Processed
*NEG Tons Fabric Processed
10 Feet
Tons Fabric Processed
285
117
285
118
285
Rubberized Fabric - 3069. 2241
3-30-002-11
3-30-002-12
3-30-002-13
- Impregnation
- Wet Coating
- Hot Melt Coating
*120 Tons Coating Applied
*1200 Tons Coating Applied
*120 Tons Coating Applied
340
340
340
Refer to numbered notes in Appendix A or lettered notes in Appendix B; factors without asterisks are from AP-42.
-------
PART SO NO VOC
SCC Process Lbs/Unit Lbs/ftnit Lbs/finlt Lbs/Unit
Rubberized Fabric - 3069. 2241 (Continued}
3-30-002-14 - Wet Coating Mixing *133
3-30-002-98 - Other Not Classified (Specify
in Coaments)
3-30-002-99 - Other Not Classified (Specify
in Comments)
Carpet Operations - 2271. 2272, 2279
3-30-003-99 - Other Not Classified (Specify
in Comments)
Fabric Finishing - 2261. 2262. 2269 (Shrink Proofing. Water Proofing. Ant I Wrinkling. Sizing, etc.)
3-30-004-99 - Other Not Classified (Specify
in Comments)
3-30-005-99 - Other Not Classified (Specify
in Comments)
Textile Products - Fugitive Emissions
3-30-888-01 - Specify in Comments Field*
3-30-888-02 - Specify in Coaments Field*
3-30-888-03 - Specify in Comments Field*
3-30-888-04 - Specify in Comments Field*
3-30-888-05 - Specify in Comments Field*
PRINTING AND PUBLISHING - TYPESETTING - MAJOR GROUP 27
Typesetting (Lead Kernel ting} - 2791
3-60-001-01 - Kernel ting (Lead Emissions Only) 0.7
IN-PROCESS FUEL USEq<1
Anthracite Coal
3-90-001-99 - General 0.0 0.0 0.0 0.0qq
Bituminous Coal
3-90-002-01 - Cement Kiln/Dryer 0.0 *26.0 s" 0.0 °qq
3-90-002-03 - Lime Kiln 0.0 *19.0 s" 0.0 ° qq
3-90-002-99 - General 0.0 0.0 0.0 0.0
Lianite
3-90-003-99 - General 0.0 0.0 0.0 0.0*1"*
CO
Lbs/Unit Units Notes
Tons Coating Applied 340
Gallons
Tons Processed
Tons Processed
Tons Fabric Processed
Items Produced
Process Unit -Year
Process Unit-Year
Process Unit-Year
Process Unit-Year
Process Unit-Year
Tons Melted
0 . 0 Tons Burned
0.0 Tons Burned
0.0 Tons Burned
0 . 0 Tons Burned
0.0 Tons Burned
*Note that fugitive emissions are reported in units of Ibs/process unit-year rather than Ibs/ton product as in the NEDS Source Classification Codes
and Emission Factor Listing dated October 1985.
Refer to numbered notes in Appendix A or lettered notes in Appendix B; factors without asterisks are from AP-42.
-------
sec
Residual Oil
3-90-004-02 -
3-90-004-03 -
3-90-004-99 -
Distillate Oil
3-90-005-02 -
3-90-005-03 -
3-90-005-98 -
3-90-005-99 -
Natural Gas
3-90-006-02 -
3-90-006-03 -
3-90-006-99 -
Process Gas
3-90-007-01 -
3-90-007-02 -
3-90-007-97 -
3-90-007-98 -
3-90-007-99 -
Coke
3-90-008-99 -
Wood
3-90-009-99 -
Process
Cement Kiln/Dryer
Lime Kiln
General
Cement Kiln/Dryer
Lime Kiln
Grade 4 Oil: General
General
Cement Kiln/Dryer
Lime Kiln
General
Coke Oven or Blast Furnace
Coke Oven Gas
General: Specify in Comments
General: Specify in Comments
General: Specify in Comments
General
General
PART
Lbs/Unit
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
so
Lbs/finit
*108.
*79
0.
*98.
*72.
0.
0,
0.
0,
0
0
0.
0.
0
0
0
0
,0 S"
5 S"
.0
.0 S"
.0 S"
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
NO
Lbs/finit
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
voc
Lbs/Unit
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
Liquified Petroleum Gas
3-90-010-99 -
Solid Waste
3-90-012-99 -
Liquid Waste
3-90-013-99 -
MISCELLANEOUS
General
Specify in Comments
Specify in Comments
MANUFACTURING INDUSTRIES - MAJOR GROUP
Manufacturing Industries - Fuel Fired
0
0
0
39
.0
.0
.0
0
0
0
.0
.0
.0
0.0
0.0
0.0
0
0
0
.oqq
.oqq
.oqq
.oqq
.oqq
.oqq
.oqq
.oqq
.oqq
.oqq
.oqq
.oqq
.oqq
.oqq
.oqq
.oqq
.oqq
.oqq
.oqq
.oqq
CO
Lbs/Unit
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
Units Notes
10 Gallons Burned
10 Gallons Burned
10 Gallons Burned
3
10 Gallons Burned
10 Gallons Burned
10 Gallons Burned
10 Gallons Burned
£
10 Cubic Feed Burned
10 Cubic Feed Burned
10 Cubic Feed Burned
10 Cubic Feed Burned
10 Cubic Feed Burned
10 Cubic Feed Burned
10 Cubic Feed Burned
10 Cubic Feed Burned
Tons Burned
Tons Burned
3
10 Gallons Burned
Tons Burned
10 Gallons Burned
EouiDment
Process Heaters
3-99-900-01 - Distillate Oil (No. 2)
3-99-900-02 - Residual Oil
*144
*159
.0 S
.0 S
*20.0
*55.0
*0
*0
.20
.28
103 Gallons Burned 129
10 Gallons Burned 129
*Refer to numbered notes in Appendix A or lettered notes in Appendix B; factors without asterisks are from AP-42.
-------
f\J
PART
SCC Process Lbs/Unit
Process Heaters (Continued)
3-99-900-03 - Natural Gas
3-99-900-04 - Process Gas
Incinerators
3-99-900-11 - Distillate Oil (No. 2)
3-99-900-12 - Residual Oil
3-99-900-13 - Natural Gas
3-99-900-14 - Process Gas
Flares
3-99-900-23 - Natural Gas
3-99-900-24 - Process Gas
Miscellaneous Industrial Processes
3-99-999-93 - Other Not Classified (Specify
in Comments)
3-99-999-94 - Other Not Classified (Specify
in Comments)
3-99-999-95 - Other Not Classified (Specify
in Comnents)
3-99-999-96 - Other Not Classified (Specify
in Comments)
3-99-999-98 - Other Not Classified (Specify
in Comments)
3-99-999-99 - Other Not Classified (Specify
in Comments)
ORGANIC SOLVENT EVAPORATION - DRY CLEANING - MAJOR GROUP 72
Dry Cleaning - 7215. 7216. 7218
4-01-001-01 - Perchloroethylene 0.0
4-01-001-02 - Stoddard (Petroleum Solvent) 0.0
4-01-001-03 - Perchloroethylene 0.0
4-01-001-04 - Stoddard (Petroleum Solvent) 0.0
4-01-001-05 - Trlchlorotrlfluoroethane (Freon) 0.0
4-01-001-06 - Trlchlorotrlfluoroethane (Freon) 0.0
4-01-001-98 - Other Not Classified (Specify 0.0
in Comments)
Open-Top Vapor Degreaslng
4-01-002-01 - Stoddard (Petroleum Naphtha) 0.0
4-01-002-02 - l.l.l-Trichloroethane* (Methyl 0.0
Chloroform)
SO NO VOC
Lbs/unIt Los/unit Lbs/Unit
*0.6 M40.0 *2.8
*950.0 S *140.0 *2.8
*0.4
*0.56
*5.6
•5.6
*5.6
*5.6
0.0 0.0 550.0
0.0 0.0 56°'°d
0.0 0.0 *2, 000.0
0.0 0.0 *2, 000.0
0.0 0.0 0.0
0.0 0.0 0.0
0.0 0.0
*~ ,..ss
0.0 0.0 2,000.0
0.0 0.0 0.0
CO
Lbs/Unit Units
6
10 Cubic Feet Burned
10 Cubic Feet Burned
10, Gallons Burned
10 Gallons Burned
10 Cubic Feet Burned
10 Cubic Feet Burned
6
10 Cubic Feet Burned
10 Cubic Feet Burned
Parts Processed
Pounds Processed
Gallons
3
10 Gallons
3
10 Parts Produced
Tons Processed
0.0 Tons Clothes Cleaned
0.0 Tons Clothes Cleaned
0 . 0 Tons Solvent Consumed
0 . 0 Tons Solvent Consumed
0 . 0 Tons Solvent Consumed
0.0 Tons Clothes Cleaned
0 . 0 Tons Solvent Consumed
0.0 Tons Make-Up Solvent Used
0.0 Tons Make-Up Solvent Used
Notes
129
129
130
130
130
130
130
130
Refer to numbered notes In Appendix A or lettered notes In Appendix B; factors without asterisks are from AP-42.
-------
CO
sec
Process
PART
Lbs/Unit
SO
Lbs/flnit
NO VOC
Lbs/finit Lbs/Unit
CO
Lbs/Unit
Units
Motes
Open-Top Vapor Degreasina (Continued)
4-01-002-03
4-01-002-04
(,-01-002-05
4-01-002-06
4-01-002-07
4-01-002-08
4-01-002-15
- Perchloroethylene
- Methylene Chloride"
- Trlchl.oroethyl.ene
- Toluene
- Trichlorotrifluoroettuuie
- Chlorosolve
uu
- Entire Unit
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
2,000.0
0.0
2,000.0
2,000.0
0.0
*2, 000.0
21,000.0
0.0
0.0
0.0
0.0
0.0
*0.0
0.0
Tons
Tons
Tons
Tons
Tons
Tons
Make-Up
Make -Up
Make-Up
Make-Up
Make-Up
Make-Up
Solvent
Solvent
Solvent
Solvent
Solvent
Solvent
Number of Degreasing
Used
Used
Used
Used
Used
Used 332
Units
4-01-002-16 - Entire Unit
till
4-01-002-17 - Entire Unit
4-01-002-97 - Other Not Classified (Specify
in Comments)
4-01-002-99 - Other Not Classified (Specify
in Comments)
Conveyor!zed Vapor Decreasing
0.0
0.0
0.0
0.0
0.0
0.0
in Operation-Year
0.0 180.0 0.0 10 Sq. Ft. Product
Surface Area
0.0 0.15 0.0 Sq. Ft. Surface Area Per
Hours of Operation
0.0 0.0 Gallons Solvent Used
Tons Make-Up Solvent Used
-01-002-21
-01-002-22
-01-002-23
-01-002-24
-01-002-25
-01-002-35
4-01-002-36
4-01-002-96
4-01-002-98
Deceasing
4-01-002-51
4-01-002-52
4-01-002-53
4-01-002-54
4-01-002-55
4-01-002-56
4-01-002-57
4-01-002-95
- Stoddard (Petroleum Naphtha)
- 1,1,1-Trichloroethane
- Perchloroethylene
- Methylene Chloride
- Trichloroethylene
- Entire Unit: with Vaporized
Solvent
uu
- Entire Unit: with Nonboiling
Solvent
- Other Not Classified (Specify
in Comments)
- Other Not Classified (Specify
in Comments)
Units - General
- Stoddard Solvent
- 1,1,1-Trichloroethane
- Perchloroethylene
- Methylene Chloride
- Trichloroethylene
- Toluene
- Trichlorotrifluoroethane
- Other Not Classified (Specify
in Comments)
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
.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
2,000
0
2,000
0
2,000
52,000
104,000
*7
*0
*13
*0
*12
*7
*0
.0
.0
.0
.0
.0
.0
.0
.2
.0
.4
.0
.1
.2
.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
Tons Make-Up Solvent Used
Tons Make-Up Solvent Used
Tons Make-Up Solvent Used
Tons Make-Up Solvent Used
Tons Make-Up Solvent Used
Number of Degreasing Units
in Ope rat ion- Year
Number of Degreasing Units
in Operation-Year
Gallons Solvent Used
Tons Make-Up Solvent Used
Gallons Solvent Consumed
Gallons Solvent Consumed
Gallons Solvent Consumed
Gallons Solvent Consumed
Gallons Solvent Consumed
Gallons Solvent Consumed
Gallons Solvent Consumed
Gallons Solvent Consumed
157
157
157
157
157
157
157
*Refer to numbered notes in Appendix A or lettered notes in Appendix B; factors without asterisks are from AP-42.
-------
sec
Process
PART
Lbs/Unit
SO
Lbs/finit
NO
Lbs/Onlt
VOC
Lbs/Unit
CO
Lbs/Unit
Units Notes
Cold Solvent Cleaning/Stripping
4-01-003-01
4-01-003-02
4-01-003-03
4-01-003-04
4-01-003-05
4-01-003-06
4-01-003-35
- Methanol
- Methylene Chloride
- Stoddard (Petroleum Solvent)
' Perchloroethylene
- 1,1,1-Trlchloroethane (Methyl
Chloroform)
- Trichloroethvlene
- Entire Unit"
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
2,000.
0.
2,000.
2,000.
0.
2,000.
660.
.0
.0
.0
0
.0
.0
0
0.0
0.0
0.0
0.0
0.0
0.0
0.0
Tons
Tons
Tons
Tons
Tons
Solvent
Solvent
Solvent
Solvent
Solvent
Consumed
Consumed
Consumed
Consumed
Consumed
Tons Solvent Consumed
Number of Cold Solvent
4-01-003-36 - Entire Unit
4-01-003-98 - Other Hot Classified (Specify
in Comments)
4-01-003-99 - Other Hot Classified (Specify
in Comments)
0.0
0.0
0.0
96.0
Cleaners in Operation-Year
0.0 10 Sq. Ft. Product
Surface Area
Gallons Solvent Consumed
Tons Solvent Consumed
rin« with Chlorinated Solvent - 2211-2241. 2261-2269. 2281-2284 (Removal of Finish Oils from Fabric)
Knit Fabric !
4-01-004-01 - Perchloroethylene
4-01-004-99 - Other Hot Classified (Specify
in Comments)
0.0
0.0
0.0
2,000.0
0.0 Tons Solvent Consumed
Tons Solvent Consumed
Organic Solvent Evaporation - Fugitive Emissions
4-01-888-01 - Specify in Comments Field
4-01-888-02 - Specify in Cements Field
4-01-888-03 - Specify in Comments Field
4-01-888-04 - Specify in Comments Field
4-01-888-05 - Specify in Comments Field
4-01-888-98 - Specify in Comments Field
vv
SURFACE COATING OPERATIONS
Coating Application - General
4-02-001-01 - Paint: Solvent-Base
4-02-001-10 - Paint: Solvent-Base
4-02-002-01 - Paint: Water-Base
4-02-002-10 - Paint: Water-Base
4-02-003-01 - Varnish/Shellac
4-02-003-10 - Varnish/ Shellac
4-02-004-01 - Lacquer
4-02-004-10 - Lacquer
Tons Product
Tons Product
Tons Product
Tons Product
Tons Product
Gallons
O.o 0.0 1,120.0 0.0 Tons Coating Mix Applied
0.0 0.0 *5.6° 0.0 Gallons of Coating
O.o 0.0 *180.0d 0.0 Tons Coating Mix Applied
0.0 0.0 *1.0d 0.0 Gallons of Coating
O.o 0.0 1,000.0 0.0 Tons Coating Mix Applied
00 0.0 *3.5° 0.0 Gallons of Coating
O.Q 0.0 1,540.0 0.0 Tons Coating Mix Applied
0 o 0.0 *6.5° 0.0 Gallons of Coating
Refer to numbered notes
in Appendix A or lettered notes in Appendix B: factors without asterisks are from AP-42
-------
SCC Process
Coating. ADD! lotion - General. (Continued)
4-02-005-01 - Enamel
4-02-005-10 - Enamel
4-02-006-01 - Primer
4-02-006-10 - Primer
4-02-007-01 - Adhesive Application
4-02-007-06 - Adhesive: Solvent Mining
4-02-007-07 - Adhesive: Solvent Storage
4-02-007-10 - Adhesive
Coat ins Oven
4-02-008-01 - General
4-02-008-10 - General
4-02-008-98 - General
SS XX
Thinning Solvents
4-02-009-01 - General: Specify in Comment »
4-02-009-02 - Acetone
4-02-009-03 - Butyl Acetate
4-02-009-04 - Butyl Alcohol
4-02-009-05 - Carbltol
4-02-009-06 - Cellosolve
4-02-009-07 - Cellosolve Acetate
4-02-009-08 - Dimethyl Fonnamlde
4-02-009-09 - Ethyl Acetate
4-02-009-10 - Ethyl Alcohol
4-02-009-11 - Gasoline
4-02-009-12 - Isopropyl Alcohol
4-02-009-13 - Isopropyl Acetate
4-02-009-14 - Kerosene
4-02-009-15 - Lactol Spirits
4-02-009-16 - Methyl Acetate
4-02-009-17 - Methyl Alcohol
4-02-009-18 - MEK
4-02-009-19 - MIBK
4-02-009-20 - Mineral Spirits
4-02-009-21 - Naphtha
4-02-009-22 - Toluene
4-02-009-23 - Varsol
4-02-009-24 - Xylene
4-02-009-25 - Benzene
4-02-009-26 - Turpentine
4-02-009-27 - Hexylene Clycol
PART
Lbs/Unlt
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
0.0
0.0
0.0
0.0
0.0
*0.0
so
Lbs/Snit
0.0
0.0
0.0
0.0
0.0
0.0
0.0
0.0
*5.0
*1
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
0.0
0.0
•0.0
NO
Lbs/finit
0.0
0.0
0.0
0.0
0.0
0.0
0.0
0.0
*54
*13
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
0.0
0.0
*0.0
voc
Lbs/Unlt
840.0
W
3.8
1,320.0
*6.6°
*900
*200
*NEG
*4.4
•800
*42
2,000.0
2,000.0
2,000.0
2,000.0
2,000.0
2,000.0
2,000.0
2,000.0
2,000.0
2,000.0
2,000.0
2,000.0
2,000.0
2,000.0
2,000.0
2,000.0
2,000.0
2,000.0
2,000.0
2,000.0
2,000.0
2,000.0
2,000.0
2,000.0
2,000.0
2,000.0
*2, 000.0
CO
Lbs/Unit
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
0.0
0.0
0.0
0.0
0.0
0.0
0.0
0.0
0.0
0.0
*0.0
Units
Tons Coating Mix Applied
Gallons of Coating
Tons Coating Mix Applied
Gallons of Coating
Tons Coating Mix Applied
Tons Solvent Mixed
Tons Solvent Stored
Gallons of Coating
Tons Coating
Gallons of Coating
10 Feet
Tons Solvent
Tons Solvent
Tons Solvent
Tons Solvent
Tons Solvent
Tons Solvent
Tons Solvent
Tons Solvent
Tons Solvent
Tons Solvent
Tons Solvent
Tons Solvent
Tons Solvent
Tons Solvent
Tons Solvent
Tons Solvent
Tons Solvent
Tons Solvent
Tons Solvent
Tons Solvent
Tons Solvent
Tons Solvent
Tons Solvent
Tons Solvent
Tons Solvent
Tons Solvent
Tons Solvent
Notes
65
293
293
66
67, 146, 212
132, 296
332
*Refer to numbered notes in Appendix A or lettered notes in Appendix B, factors without asterisks are from AP-42.
-------
PART
SCC Process Lbs/Unlt
Thinning Solvents (Continued) '
4-02-009-28 - Ethylene Oxide *0.0
4-02-009-98 - General: Specify in Comments 0.0
w
Coating Oven Heater
4-02-010-01 - Natural Gas
4-02-010-02 - Distillate Oil
4-02-010-03 - Residual Oil
4-02-010-04 - Liquified Petroleum Gas (LPG)
Fabric Coating - 2295PP
4-02-011-01 - Coating Operation
4-02-011-03 - Coating Mixing
4-02-011-04 - Coating Storage
4-02-011-05 - Equipment Cleanup
Fabric Printing - 2261. 2262. 2269PP
4-02-011-11 - Fabric Printing: Roller
4-02-011-12 - Fabric Printing: Roller
4-02-011-13 - Fabric Printing: Rotary Screen
4-02-011-14 - Fabric Printing: Rotary Screen77
4-02-011-15 - Fabric Printing: Flat Screen
4-02-011-16 - Fabric Printing: Flat Screen77
4-02-011-99 - Other Hot Classified (Specify
in Comments)
Fabric Dyeiru. - 2211-2241. 2261-2269. 2281-2284PP
4-02-012-01 - Dye Application: General
4-02-012-10 - Dye Application: General
ADDllcatlon of Solvent-Borne Coating (Pacer Coating)
4-02-013-01 - Coating Operation
4-02-013-03 - Coating Mixing
4-02-013-04 - Coating Storage
4-02-013-05 - Equipment Cleaning
4-02-013-99 - Other Hot Classified (Specify
in Comments)
Surface Coating of Lame ADD! lances - 363, 365. 343, 358
4-02-014-01 - Prime Coating Operation
4-02-014-02 - Cleaning/Pretreatment
4-02-014-03 - Coating Mixing
4-02-014-04 - Coating Storage
4-02-014-05 - Equipment Cleanup
4-02-014-06 - Topcoat Spray
SO
Lbs/ftnit
*0.0
0.0
*0.6
*144.0 S
*159.0 S
*86.5 S
0.0
0.0
0.0
0.0
0.0
0.0
0.0
0.0
0.0
0.0
0.0
0.0
Of)
. u
Of)
. u
Of)
• U
On
. U
NO
Lbs/Snit
*0.0
0.0
*140.0
*20.0
*55.0
*9.0
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
voc
Lbs/Unlt
*2, 000.0
*2.8
*0.20
*0.28
*0.5
*1,600
*200
*NEG
*200
284.0
278,000.0
46.0
62,000.0
158.0
62,000.0
*196
*1,400
*NEG
*300
*900
*NEG
*200
*NEG
*200
*700
CO
Lbs/Unlt
*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
Units
Tons Solvent
Gallons Solvent
10 Cubic Feet Burned
10 Gallons Burned
10 Gallons Burned
10 Gallons Burned
Tons Solvent in Coating
Tons Solvent in Coating
Tons Solvent in Coating
Tons Solvent in Coating
Tons of Fabric
Huober of Printing Lines-Year
Tons of Fabric
Number of Printing Lines-Year
Tons of Fabric
Number of Printing Lines-Year
Tons Solvent in Coating
Tons Dye Consumed
Gallons Dye Consumed
Tons Solvent in Coating
Tons Solvent in Coating
Tons Solvent in Coating
Tons Solvent in Coating
Tons Solvent in Coating
Tons Solvent in Coating
Tons Solvent in Coating
Tons Solvent in Coating
Tons Solvent in Coating
Tons Solvent in Coating
Tons Solvent in Coating
Notes
332
91, 130
91, 130
91, 130
91, 130
287
287
287
287
117
287
287
287
287
290
290
290
290
290
290
*Refer to numbered notes In Appendix A or Uttered notes in Appendix B; factors without asterisks are from AP-42.
-------
sec
PART
Process Lbs/Unit
SO
Lbs/finlt
NO VOC
Lbs/Unit Lbs/Unit
CO
Lbs/Unit
Units
Notes
Surface Coat Inn of Lame Aoollances - 363. 365. 343. 318 tCanf Inued)"
4-02-014-31
4-02-014-32
4-02-014-33
4-02-014-34
4-02-014-35
4-02-014-36
4-02-014-37
4-02-014-38
4-02-014-99
MaRnet Wire
4-02-015-01
4-02-015-02
4-02-015-03
4-02-015-04
4-02-015-05
4-02-015-31
4-02-015-99
- Coating Line-General
- Prime Air Spray
- Prime Electrostatic Spray
- Prime Flow Coat
- Prime Dip Coat
- Prime Electro-Deposition
- Top Air Spray
- Top Electrostatic Spray
- Other Not Classified (Specify
in Comments )
Surface Coating - 3357. 3351
- Coating/Application/Curing
- Cleaning/Pretreatment
- Coating Mixing
- Coating Storage
- Equipment Cleanup
- Coating Line-General
- Other Not Classified (Specify
in Comments)
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
.0
.0
.0
.0
.0
.0
.0
.0
0.9
3.1
1.75
1.65
1.65
1.5
5.0
2.8
*1,600
*NEG
*200
*NEG
*200
186,000.0
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
Number of Appliances
Produced
10 Sq. Ft.
Surface Area
Product
10 Sq. Ft. Product
Surface Area
10 Sq. Ft. Product
Surface Area
10 Sq. Ft.
Surface Area
10 Sq. Ft.
Surface Area
10 Sq. Ft.
Surface Area
10 Sq. Ft.
Surface Area
Tons Solvent
Tons Solvent
Tons Solvent
Tons Solvent
Tons Solvent
Tons Solvent
Product
Product
Product
Product
in Coating
in Coating
in Coating
in Coating
in Coat ing
in Coating
293
293
293
293
293
Number of Coating Lines
Tons Solvent
in Coating
Surface Coating of Automobiles and Light Trucks - 3771. 3713
4-02-016-01
4-02-016-02
4-02-016-03
4-02-016-04
4-02-016-05
4-02-016-06
4-02-016-19
4-02-016-20
Automobiles
4-02-016-21
4-02-016-22
4-02-016-23
- Prime Application, Electro- 9.68
Deposit ion/Dip/ Spray
- Cleaning/Pretreatment
- Coating Mixing
- Coating Storage
- Equipment Cleanup
- Topcoat Operation
- Prime Surfacing Operation
- Repair Topcoat Application Area
- 3711
- Prime Coating: Solvent-Borne
- Prime Coating: Electro-Deposition
- Guide Coating: Solvent-Borne
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
•500
*NEG
*200
*NEG
*200
*800
*100
*200
14.54
01 f
. 45
4.16
0,
0,
0,
0.
0,
0.
0.
0.
0.
.
0.
.0
.0
.0
.0
.0
.0
.0
.0
,0
,0
Tons Solvent
Tons Solvent
Tons Solvent
Tons Solvent
Tons Solvent
Tons Solvent
Tons Solvent
Tons Solvent
in Coating
in Coating
in Coating
in Coating
in Coat ing
in Coating
in Coating
in Coating
298, 348
348
348
348
348
348
348
348
Number of Autos Produced
Number of Autos Produced
Refer to numbered notes in Appendix A or lettered notes in Appendix B; factors without asterisks are from AP-42.
-------
CO
PART SO
SCC Process Lbs/Unit Lbs/unit
Automobiles - 3711 (Continued)
4-02-016-24 - Guide Coating: Waterbome
4-02-016-25 - Topcoat: Solvent-Borne
4-02-016-26 - Topcoat: Waterbome
LlRht Duty Trucks - 3713
4-02-016-27 - Prime Coating: Solvent-Borne
4-02-016-28 - Prime Coating: Electro-Deposition
4-02-016-29 - Guide Coating: Solvent-Borne
4-02-016-30 - Guide Coating: Waterborne
4-02-016-31 - Topcoat: Solvent-Borne
4-02-016-32 - Topcoat: Waterbome
4-02-016-99 - Other Not Classified (Specify
in Comments)
Surface Coat inn of Metal Cans - 3411
4-02*017-02 - Cleanlng/Pretceatownt
4-02-017-03 - Coating Mixing
4-02-017-04 - Coating Storage
4-02-017-05 ' Equipment Cleanup
4-02-017-21 - Two Piece and Exterior Base
Coating
4-02-017-22 - Interior Spray Coating
4-02-017-23 - Sheet Basecoating (Interior)
4-02-017-24 - Sheet Basecoating (Exterior)
4-02-017-25 - Side Seam Spray Coating
4-02-017-26 - End Sealing Compound
4-02-017-27 - Lithography
4-02-017-28 - Over Varnish
4-02-017-31 - Three-piece Can Sheet Basecoating
4-02-017-32 - Three-piece Can Sheet Lithographic
Coating Line
4-02-017-33 - Three-piece Beverage Can-Side Seam
Spray Coating
4-02-017-34 - Three-piece Beverage Can Interior
Body Spray Coating
4-02-017-35 - Two-piece Can Coating Line
4-02-017-36 - Two-piece Can End Sealing Compound
4-02-017-99 - Other Not Classified (Specify
in Comments)
Surface Coat inn of Metal Colls - 3353. 3354
4-02-018-01 - Prime Coating Application
4-02-018-03 - Solvent Mixing
4-02-018-04 - Solvent Storage
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
0.0
0.0
0.0
0.0
0.0
0.0
0.0
NO VOC
Lbs/unlt Lbs/Unit
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
0.0
0.0
0.0
0.0
0.0
0.0
0.0
1.5
30.8
4.95
42.39
0.58
14.04
5.06
34.0
15.47
•NEC
•200
•NEC
•200
*900
*400
*400
*400
• 100
•100
*2,000
•200
352,000.0
11,000.0
40,000.0
176,000.0
574,000.0
30,000.0
*2, 000.0
•800
•200
•MEG
CO
Lbs/Unit Units
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
0.0
0.0
0.0
0.0
0.0
0.0
0.0
Number of Autos Produced
Number of Autos Produced
Number of Autos Produced
Number of Trucks Produced
Number of Trucks Produced
Number of Trucks Produced
Number of Trucks Produced
Number of Trucks Produced
Number of Trucks Produced
Tons Solvent in Coating
Tons Solvent in Coating
Tons Solvent in Coating
Tons Solvent in Coating
Tons Solvent in Coating
Tons Solvent in Coating
Tons Solvent in Coating
Tons Solvent In Coating
Tons Solvent in Coating
Tons Solvent in Coating
Tons Solvent in Coating
Tons Solvent in Ink
Tons Solvent in Coating
Number of Coating Lines
Number of Coating Lines
Number of Coating Lines
Number of Coating Lines
Number of Coating Lines
Number of Coating Lines
Tons Solvent in Coating
Tons Solvent in Coating
Tons Solvent in Coating
Tons Solvent in Coating
Notes
293
293
293
293
349
349
349
349
349
349
349
293
293
293
Refer to numbered notes in Appendix A or lettered notes in Appendix B: factors without asterisks are from AP-42.
-------
PART
SCC Process Lbs/Unit
Surface Coating of Metal Colls - 3353, 3354 (Continued)
4-02-018-05 - Equipment Cleanup
4-02-018-06 - Finish Coating Application
4-02-018-99 - Other Not Classified (Specify
in Comments)
Wood Furniture Surface Coating - 2511. 2512. 2517. 2521
4-02-019-01 - Coating Operation
4-02-019-03 - Coating Mixing
4-02-019-04 - Coating Storage
4-02-019-99 - Other Not Classified (Specify
in Comments)
Metal Furniture Surface Coating - 2514. 2522
4-02-020-01 - Coating Operation
4-02-020-02 - Cleaning/Pretreatment
4-02-020-03 - Coating Mixing
4-02-020-04 - Coating Storage
4-02-020-05 - Equipment Cleanup
4-02-020-31 - Single Spray line: General
4-02-020-32 - Spray Dip Line: General
4-02-020-33 - Spray High Solids Coating
4-02-020-34 - Spray Water-Borne Coating
4-02-020-99 - Other Not Classified (Specify
in Comments)
Surface Coating of Flat Wood Products - 2435. 2492. 2499
4-02-021-01 - Base Coat
4-02-021-03 - Coating Mix
4-02-021-04 - Coating Storage
4-02-021-05 - Equipment Cleanup
4-02-021-06 - Topcoat
4-02-021-07 - Filler
4-02-021-08 - Sealer
4-02-021-09 - Inks
4-02-021-31 - Waterborne Coating
4-02-021-32 - Solvent-borne Coating
SO
Lbs/finit
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
NO
Lbs/Bnit
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
voc
Lbs/Unit
*200
*800
*2,000.0d
*200
*NEG
*1,600
*NEG
*200
*NEG
*200
13.1
15.3
3.9
2.45
*1,500
*200
•NEC
*200
*1,500
*60
*60
*2, 000.0
2.5
16.5
CO
Lbs/Unit
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
Units
Tons Solvent in Coating
Tons Solvent In Coating
Tons Solvent in Coating
Tons Solvent in Coating
Tons Solvent in Coating
Tons Solvent in Coating
Tons Solvent In Coating
Tons Solvent in Coating
Tons Solvent In Coating
Tons Solvent in Coating
Tons Solvent In Coating
Tons Solvent in Coating
10 Sq. Ft. Product
Surface Area Coated
10 Sq. Ft. Product
Surface Area Coated
10 Sq. Ft. Product
Surface Area Coated
10 Sq. Ft. Product
Surface Area Coated
Tons Solvent in Coating
Tons Solvent in Coating
Tons Solvent in Coating
Tons Solvent in Coating
Tons Solvent in Coating
Tons Solvent in Coating
Tons Solvent in Coating
Tons Solvent in Coating
Toos Solvent in Ink
10 Sq. Ft. Product
Surface Area
10 Sq. Ft. Product
Surface Area
Notes
293
293
293
293
294
294
294
294
294
293
293
293
293
293
293
293
Refer to numbered notes in Appendix A or lettered notes In Appendix B; factors without asterisks are from AP-42.
-------
ro
o
sec
PART SO
Process Lbs/Unit Lbs/Unit
Surface Coating of Flat Wood Products - 2435. 2492. 2499
4-02-021-33
- Ultraviolet Coating
(Continued)
0.
.0
NO
Lbs/Unit
0.0
voc
Lbs/Unit
0.8
CO
Lbs/Unit
0.0
Units
o
io3
Sq. Ft.
Notes
Product
Surface Area
4-02-021-99
- Other Not Classified (Specify
in Comments)
0.
.0
0.0
0.0
Tons
Solvent
in
Coating
Surface Coating of Plastics Parts - 3079
4-02-022-01
4-02-022-02
4-02-022-03
4-02-022-04
4-02-022-05
4-02-022-99
- Coating Operation
- Cleanlng/Pretreatment
- Coating Mix ing
- Coating Storage
- Equipment Cleanup
- Other Not Classified (Specify
in Coooents)
H
0,
0,
0.
0
0.
0
,0
.0
o
.0
.0
.0
0.0
0.0
0.0
0.0
0.0
0.0
*1600.0
*NEG
•200
*NEG
*200
0.0
0.0
0.0
0.0
0.0
0.0
Tons
Tons
Tons
Tons
Tons
Tons
Surface Coatixui of La rue Ships - 3731"
4-02-023-01
4-02-023-02
4-02-023-03
4-02-023-04
4-02-023-05
4-02-023-06
4-02-023-99
- Prime Coating Operation
- Cleaning/Pretreatment
- Coating Mixing
- Coating Storage
- Equipment Cleanup
- Topcoat Operation
- Other Not Classified (Specify
in Coooents)
A
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
*800
*NEG
*200
•NEC
*200
*800
Surface Coating of Lar«e Aircraft - 3721"
4-02-024-01
4-02-024-02
4-02-024-03
4-02-024-04
4-02-024-05
4-02-024-06
4-02-024-99
- Prime Coating Operation
- Cleaning/Pretreatment
- Coating Mixing
- Coating Storage
- Equipment Cleanup
- Topcoat Operation
- Other Not Classified (Specify
in Comments)
Surface Coating of Miscellaneous Metal Parts***
4-02-025-01 - Coating Operation
4-02-025-02 - Cleaning/Pretreatment
4-02-025-03 - Coating Mixing
4-02-025-04 - Coating Storage
»-u2-u25-05 - Equipment Cleanup
4-02-025-31 - Conveyor Single Flow
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
0.0
0.0
•800
•NEC
*200
*NEG
*200
•800
*1600
*NEG
•200
*NEG
*200
15.3
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
Tons
Tons
Tons
Tons
Tons
Tons
Tons
Tons
Tons
Tons
Tons
Tons
Tons
Tons
Tons
Tons
Tons
Tons
Tons
10
Solvent
Solvent
Solvent
Solvent
Solvent
Solvent
Solvent
Solvent
Solvent
Solvent
Solvent
Solvent
Solvent
Solvent
Solvent
Solvent
Solvent
Solvent
Solvent
Solvent
Solvent
Solvent
Solvent
Solvent
Solvent
Sq. Ft.
in
in
in
in
in
in
in
in
in
in
in
in
in
in
in
In
in
in
in
in
Coat ing
Coating
Coating
Coat ing
Coating
Coating
Coating
Coating
Coating
Coating
Coating
Coating
Coating
Coating
Coating
Coating
Coating
Coating
Coating
Coat ing
in Coating
in Coating
in Coating
in Coating
In Coating
Product
293
293
293
293
293
293
293
293
293
293
293
293
293
293
293
293
293
293
293
293
293
293
bur I ace Area
*Refer to numbered notes in Appendix A or lettered notes in Appendix B; factors without asterisks are from AP-42.
-------
sec
PART SO
Process Lbs/Unlt Lbs/Snit
NO
Lbs/dnlt
voc
Lbs/Unlt
CO
Lbs/Unit
Units
Notes
Surface Coat Inn of Miscellaneous Metal Parts (Continued)
4-02-025-32
4-02-025-33
4-02-025-34
4-02-025-35
4-02-025-36
4-02-025-37
4-02-025-99
4-02-026-01
4-02-026-02
4-02-026-03
4-02-026-04
4-02-026-05
4-02-026-06
4-02-026-07
4-02-026-99
- Conveyor Single Dip
- Conveyor Single Spray
- Conveyor Two Coat Flow and Spray
- Conveyor Two Coat, Dip and Spray
- Conveyor Two Coat, Spray
- Manual Two Coat, Spray and Air Dry
- Other Not Classified (Specify
in Comments)
- Coating Operation
- Cleanlng/Pretreatment
- Coating Mixing
- Coating Storage
- Equipment Cleanup
- Interior Coating
- Exterior Coating
- Other Not Classified (Specify
in Comments)
Organic Solvent Evaporation - Surface Coat In* - Punitive
4-02-888-01
4-02-888-02
4-02-888-03
4-02-888-04
4-02-888-05
- Specify In Comments Field
- Specify In Comments Field
- Specify in Comments Field
- Specify In Comments Field
- Specify in Comments Field
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
f
Emissions
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
15.3
27.5
42.8
42.8
55.0
54.8
*5.4
*NEG
*0.5
*NEG
*0.5
*2
*2
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
10 Sq. Ft. Product
Surface Area
10 Sq. Ft. Product
Surface Area
10 Sq. Ft. Product
Surface Area
10 Sq. Ft. Product
Surface Area
10 Sq. Ft. Product
Surface Area
10 Sq. Ft. Product
Surface Area
Tons Solvent in Coating
Gallons Paint Consumed
Gallons Paint Consumed
Gallons Paint Consumed
Gallons Paint Consumed
Gallons Paint Consumed
Gallons Paint Consumed
Gallons Paint Consumed
Gallons Paint Consumed
Tons Product
Tons Product
Tons Product
Tons Product
Tons Product
313
313
313
313
313
313
313
Organic Solvent Evaporation - Surface Coating - Fuel Fired Equipment
Flares
4-02-900-23 - Natural Gas
Organic Solvent Evaporation - Surface Coating - Miscellaneous
4-02-999-95 - Specify in Comments
4-02-999-96 - Specify in Comments
4-02-999-97 - Specify in Comments Field
4-02-999-98 - Specify in Comments Field
*5.6
10 Cubic Feet Burned
Tons Solvent in Coating
TODS Solvent
10 Units Produced
Gallons
130
*Refer to numbered notes in Appendix A or lettered notes in Appendix Bi factors without asterisks are from AP-42.
-------
sec
Process
FART
Lbs/Unit
PETROLEUM PRODUCT STORAGE (REFINERIES OIL AND GAS FIELDS ONLY)
so
Lbs/Unit
2911.
2992.
NO
Lbs/Unit
voc
Lbs/Unit
CO
Lbs/Unit
Units Notes
1311. 1321bbb
Fixed Roof Tanks (67.000 BBL. Tank Size)
4-03-010-01
4-03-010-02
4-03-010-03
4-03-010-10
4-03-010-13
4-03-010-16
4-03-010-19
4-03-010-97
- Gasoline RVP13: Breathing Loss
- Gasoline RVP10: Breathing Loss
- Gasoline RVP7: Breathing Loss
- Crude Oil RVP5: Breathing Loss
- Jet Naphtha (JP-4): Breathing
Loss
- Jet Kerosene: Breathing Loss
- Distillate Fuel »2: Breathing
Loss
- Specify Liquid: Breathing Loss
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
30
23
16
5
a
0
0
2
.5
.5
.4
.78
.8
.45
.39
.0
0
0
0
0
0
0
0
0
.0
.0
.0
.0
.0
.0
.0
.0
Fixed Roof Tanks (250.000 BBL. Tanks Size)
4-03-010-04
4-03-010-05
4-03-010-06
4-03-010-11
4-03-010-14
4-03-010-17
4-03-010-20
4-03-010-98
- Gasoline RVP13: Breathing Loss
- Gasoline RVP10: Breathing Loss
- Gasoline RVP7: Breathing Loss
- Crude Oil RVPS: Breathing Loss
- Jet Naphtha (JP-4): Breathing
Loss
- Jet Kerosene: Breathing Loss
- Distillate Fuel #2: Breathing
Loss
- Specify Liquid: Breathing Loss
Fixed Roof Tanks (Independent of Tank Diameter)
4-03-010-07 - Gasoline RV?13: Working Loss
4 03 010 OS Gasoline BVP10: VJcrkins Loss
4-03-010-09
4-03-010-12
4-03-010-15
4-03-010-18
- Gasoline RVP7: Working Loss
- Crude Oil RVPS: Working Loss
- Jet Naphtha (JP-4): Working Loss
- Jet Kerosene: Working Loss
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
.0
.0
Q
.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
22
17
12
4
6
0
0
4
10
S
5
2
2
0
.5
.4
.3
.15
.3
.3
.29
.8
.0
.7
.47
.5
.03
0
0
0
0
0
0
0
0
0
V
0
0
0
0
.0
.0
.0
.0
.0
.0
.0
.0
.0
n
.0
.0
.0
.0
3
10 Gallons
Capacity
10 Gallons
Capacity
10 Gallons
Capacity
10 Gallons
Capacity
10 Gallons
Capacity
10 Gallons
Capacity
10 Gallons
Capacity
10 Gallons
Capacity
10 Gallons
Capacity
10 Gallons
Capacity
10 Gallons
Capacity
10 Gallons
Capacity
10 Gallons
Capacity
10 Gallons
Capacity
10 Gallons
Capacity
10 Gallons
Capacity
3
10 Gallons
10 Gallons
3
10 Gallons
10 Gallons
10 Gallons
10 Gallons
Storage
Storage
Storage
Storage
Storage
Storage
Storage
Storage
Storage
Storage
Storage
Storage
Storage
Storage
Storage
Storage
Throughput
Throughput
Throughput
Throughput
Throughput
Throughput
-------
sec
Process
PART
Lbs/Unlt
so
Lbs/finit
NO
Lbs/finit
voc
Lbs/Unit
CO
Lbs/Unit
Fixed Roof Tanks (Independent of Tank Diameter) (Continued)
4-03-010-21 -
4-03-010-99 -
Float ing Roof
4-03-011-01 -
4-03-011-02 -
4-03-011-03 -
4-03-011-09 -
4-03-011-11 -
4-03-011-13 -
4-03-011-15 -
4-03-011-98 -
H— '
PG
(.1 Floating Roof
4-03-011-04 -
4-03-011-05 -
4-03-011-06 -
4-03-011-10 -
4-03-011-12 -
4-03-011-14 -
4-03-011-16 -
4-03-011-99 -
Floating Roof
4-03-011-07 -
4-03-011-08 -
4-03-011-17 -
4-03-011-18 -
Distillate Fuel 12: Working Loss
Specify Liquid: Working Loss
Tanks (67.000 BBL. Tank Size)
Gasoline RVP13: Standing Loss
Gasoline RVP10: Standing Loss
Gasoline RVP7: Standing Loss
Crude Oil RVP5: Standing Loss
Jet Naphtha (JP-4): Standing Loss
Jet Kerosene: Standing Loss
Distillate Fuel *2: Standing Loss
Specify Liquid: Standing Loss
Tanks (250.000 BBL. Tank Size)
Gasoline RVP13: Standing Loss
Gasoline RVP10: Standing Loss
Gasoline RVP7: Standing Loss
Crude Oil RVP5: Standing Loss
Jet Naphtha (JP-4): Standing Loss
Jet Kerosene: Standing Loss
Distillate Fuel 12: Standing Loss
Specify Liquid: Standing Loss
Tanks (Withdrawal Loss)
Gasoline RVP13/RVP10/RVP7
Gasoline RVP13/RVP10/RVP7
Crude Oil
Jet Naphtha (JP-4)
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
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
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.
18.
13.
8.
1.
3.
0.
0.
8.
6.
4.
0.
1.
0.
0.
0.
0.
*0.
*0.
02
2
4
6
76
5
035
026
9
5
2
89
7
017
013
0019
001
007
056
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
Units Notes
10* Gallons
10 Gallons
10 Gallons
Capacity
10 Gallons
Capacity
10 Gallons
Capacity
10 Gallons
Capacity
10 Gallons
Capacity
10 Gallons
Capacity
10 Gallons
Capacity
10 Gallons
Capacity
q
10 Gallons
Capacity
10 Gallons
Capacity
10 Gallons
Capacity
10 Gallons
Capacity
10 Gallons
Capacity
10 Gallons
Capacity
10 Gallons
Capacity
10 Gallons
Capacity
3
10 Gallons
1CT Gallons
10 Gallons
10 Gallons
Throughput
Throughput
Storage
Storage
Storage
Storage
Storage
Storage
Storage
Storage
Storage
Storage
Storage
Storage
Storage
Storage
Storage
Storage
Throughput
Throughput
Throughput 3
Throughput 63
Refer to numbered notes in Appendix A or lettered notes in Appendix B; factors without asterisks are from AP-42.
-------
PART
SCC Process Lbs/Unit
Floating Roof Tanks (Withdrawal Loss) (Continued)
4-03-011-19 - Jet Kerosene 0.0
4-03-011-20 - Distillate Fuel #2 0.0
4-03-011-97 - Specify Liquid 0.0
Tanks with External Float in« Roof - Primary Seal
4-03-011-30 - Specify Liquid: Standing Loss 0.0
4-03-011-31 - Gasoline: Standing Loss 0.0
4-03-011-32 - Crude Oil: Standing Loss 0.0
4-03-011-33 - Jet Naphtha (JP-4): Standing Loss 0.0
4-03-011-34 - Jet Kerosene: Standing Loss 0.0
4-03-011-35 - Distillate Fu«l *2: Standing Loss 0.0
*~~* Tanks with External Float Inn Roof - Secondary Seal
.pa, 4-03-011-40 - Specify Liquid: Standing Loss 0.0
4-03-011-41 - Gasoline: Standing Loss 0.0
4-03-011-42 - Crude Oil: Standing Loss 0.0
4-03-011-43 - Jet Naphtha (JP-4): Standing Loss 0.0
4-03-011-44 - Jet Kerosene: Standing Loss 0.0
4-03-011-45 - Distillate Fuel »2: Standing Loss 0.0
Tanks with Internal Floating Roofs
4-03-011-50 - Specify Liquid: Standing Loss 0.0
4-03-011-51 - Gasoline: Standing Loss 0.0
4-03-011-52 - Crude Oil: Standing Loss 0.0
4-03-011-53 - Jet Naphtha (JP-4): Standing Loss 0.0
4-03-011-54 - Jet Kerosene: Standing Loss 0.0
4-03-011-55 - Distillate Fuel *2: Standing Loss 0.0
SO NO VOC CO
Lbs/flnit Lbs/finit Lbs/Unit Lbs/Unit Units
0.0 0.0 0.0 103 Gallons Throughput
0.0 0.0 *0.0002 0.0 10 j Gallons Throughput
0.0 0.0 0.0 10 Gallons Throughput
0.0 0.0 0.0 103 Gallons Storage
Capacity
0.0 0.0 *14.5 0.0 10 Gallons Storage
Capacity
0.0 0.0 *1.6 0.0 10 Gallons Storage
Capacity
0.0 0.0 *2.7 0.0 10 Gallons Storage
Capacity
0.0 0.0 *0.3 0.0 10 Gallons Storage
Capacity
0.0 0.0 *0.2 0.0 10 Gallons Storage
Capacity
0.0 0.0 0.0 10 Gallons Storage
Capacity
0.0 0.0 *0.8 0.0 10 Gallons Storage
Capacity
0.0 0.0 *0.08 0.0 10 Gallons Storage
Capacity
0.0 0.0 *0.1 0.0 10 Gallons Storage
Capacity
0.0 0.0 *0.002 0.0 10 Gallons Storage
Capacity
0.0 0.0 *0.001 0.0 10 Gallons Storage
Capacity
0.0 0.0 *0.18 0.0 103 Gallons Storage
Capacity
0.0 0.0 *0.18 0.0 10 Gallons Storage
Capacity
0.0 0.0 *0.02 0.0 10 Gallons Storage
Capacity
0.0 0.0 *0.03 0.0 10 Gallons Storage
"~§~"1'7
0.0 0.0 *0.02 0.0 10 Gallons Storage
Capacity
0.0 0.0 *0.02 0.0 10 Gallons Storage
Capacity
Notes
150
315
315
315
315
315
315
315
315
315
315
143
315
315
315
315
315
Refer to numbered notes in Appendix A or lettered notes In Appendix B; factors without asterisks are from AP-42.
-------
ro
en
SCC Process
Variable Vapor Space Tanks - (10.500 BBL. Tank
4-03-012-01 - Gasoline RVP13: Pilling toss
4-03-012-02 - Gasoline RVP10: Filling Loss
4-03-012-03 - Gasoline RVP7: Filling Loss
4-03-012-04 - Jet Naphtha (JP-4): Filling Loss
4-03-012-05 - Jet Kerosene: Filling Loss
4-03-012-06 - Distillate Fuel 12: Filling Loss
4-03-012-07 - Benzene: Filling Loss
4-03-012-99 - Specify Liquid: Filling Loss
4-03-888-01 - Specify in Conments Field
4-03-888-02 - Specify in Comments Field
4-03-888-03 - Specify in Comments Field
4-03-888-04 - Specify in Comments Field
4-03-888-05 - Specify in Cooments Field
BULK TERMINALS - PETROLEUM STORAGE TANKS - MAJOI
Fixed Roof Tanks (67.000 BBL. Tank Size) - 5171
4-04-001-01 - Gasoline RVP13: Breathing Loss
4-04-001-02 - Gasoline RVP10: Breathing Loss
4-04-001-03 - Gasoline RVP7: Breathing Loss
4-04-001-04 - Gasoline RVP13: Breathing Loss
4-04-001-05 - Gasoline RVP10: Breathing Loss
4-04-001-06 - Gasoline RVP7: Breathing Loss
Fixed Roof Tanks (Independent of Tank Diameter)
4-04-001-07 - Gasoline RVP13: Working Loss
4-04-001-08 - Gasoline RVP10: Working Loss
4-04-001-09 - Gasoline RVP7: Working Loss
PART
Lbs/Unit
Size}
0.0
0.0
0.0
0.0
0.0
0.0
0.0
0.0
R GROUPS 51 AND
, 4226
0.0
0.0
0.0
0.0
0.0
0.0
- 5171, 4226
0.0
0.0
0.0
so,
Lbs/fJnlt
0.0
0.0
0.0
0.0
0.0
0.0
0.0
0.0
bob, ccc
0.0
0.0
0.0
0.0
0.0
0.0
0.0
0.0
0.0
NO
Lbs/Unit
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
voc
Lbs/Unit
9.6
7.7
5.4
2.3
0.025
0.022
*0.003
30.5
23.5
16.4
22.5
17.4
12.3
10.0
8.2
5.7
CO
Lbs/Unit
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
Units Notes
10 Gallons Throughput
10 Gallons Throughput
10 Gallons Throughput
10 Gallons Throughput
10 Gallons Throughput
10 Gallons Throughput
10 Gallons Throughput 73
10 Gallons Throughput
10 Gallons Storage
Capacity
10 Gallons Storage
Capacity
10 Gallons Storage
Capacity
10 Gallons Storage
Capacity
10 Gallons Storage
Capacity
10 Gallons Storage
Capacity
10 Gallons Storage
Capacity
10 Gallons Storage
Capacity
10 Gallons Storage
Capacity
10 Gallons Storage
Capacity
10 Gallons Storage
Capacity
10 Gallons Storage
Capacity
10 Gallons Storage
Capacity
10 Gallons Storage
Capacity
Refer to numbered notes in Appendix A or lettered notes in Appendix Bj factors without asterisks are from AP-42.
-------
sec
Float in* Roof
4-04-001-10 -
4-04-001-11 -
4-04-001-12 -
4-04-001-16 -
Float in* Roof
4-04-001-13 -
4-04-001-14 -
4-04-001-15 .-
4-04-001-17 -
PART
Process * Lbs/Unit
so
Lbs/Unit
NO
Lbs/Unit
voc
Lbs/Unit
CO
Lbs/Unit Units Notes
Tanks (67.000 BBL. Tank Size) - 5171. 4226
Gasoline RVP13: Standing Loss
Gasoline RVP10: Standing Loss
Gasoline RVP7: Standing Loss
Gasoline RVP13/10/7: Withdrawal
Loss
Tanks (250.000 BBL. Tank Size) - 5171.
Gasoline RVP13: Standing Loss
Gasoline RVP10: Standing Loss
Gasoline RVP7: Standing Loss
Gasoline RVP13/10/7: Withdrawal
Loss
Variable Vaoor Space - (10.500 BBL. Tank Size) - 5171
4-04-001-18 -
4-04-001-19 -
4-04-001-20 -
Miscellaneous
4-04-001-51 -
4-04-001-52 -
4-04-001-53 -
4-04-001-54 -
Gasoline RVP13: Filling Loss
Gasoline RVP10: Filling Loss
Gasoline RVP7: Filling Loss
Losses/Leaks - 5171. 4226
Valves, Flanges and Punps
Vapor Collection Losses
Vapor Control Unit Losses
Tank Truck Vapor Leaks
0.0
0.0
0.0
0.0
4226
0.0
0.0
0.0
0.0
. 4226
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
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
18
13
8
0
8
6
4
0
9
7
5
*0
*4
.2
.4
.6
.002
.9
.5
.2
.001
.6
.7
.4
.3
.8
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
10 Gallons
Capacity
10 Gallons
Capacity
10 Gallons
Capacity
10 Gallons
Capacity
10 Gallons
Capacity
10 Gallons
Capacity
10 Gallons
Capacity
10 Gallons
o
10 Gallons
1CT Gallons
10 Gallons
•*
1(T Gallons
10 Gallons
10 Gallons
10 Gallons
Storage
Storage
Storage
Storage
Storage
Storage
Storage
Throughput
Throughput
Throughput
Throughput
Transferred 289
Transferred
Transferred 143
Transferred
bbh. ddd
BULK PLANTS -
PETROLEUM STORAGE TANKS - MAJOR CROUPS
13. 42.
51
Fixed Roof Tanks (67.000 BBL. Tank Size) - 5171. 4226
4-04-002-01 -
4-04-002-02 -
4-04-002-03 -
A-04-002-04 -
4-04-002-05 -
4-04-002-06 -
Gasoline RVP13: Breathing Loss
Gasoline RVP10: Breathing Loss
Gasoline RVP7: Breathing Loss
Gasoline P.VP13: Herklas ~~"
Gasoline RVP10: Working Loss
Gasoline RVP7: Working Loss
0.0
0.0
0.0
0. 0
0.0
0.0
0.
0.
0.
n
0.
0.
0
0
0
V
0
0
0.
0.
0.
3.
0.
0.
0
0
0
V
0
0
30
23
*15
1G.
8
5
.5
.5
. C
.2
.7
0.0
0.0
0.0
0.0
0.0
0.0
o
10 Gallons
Capacity
10 Gallons
Capacity
10 Gallons
Capacity
10 Gallons
10 Gallons
10 Gallons
Storage
Storage
Storage 331
Throughput
Throughput
Throughput
* .JD*1UI1~*AD/.O
Refer to numbered notes in Appendix A or lettered notes in Appendix B; factors without asterisks are
-------
sec
Floating Roof
4-04-002-07 -
4-04-002-08 -
4-04-002-09 -
4-04-002-10 -
Process
PART
Lbs/Unit
SO
Lbs/unlt
NO
Lbs/finlt
voc
Lbs/Unit
CO
Lbs/Unit Units
Tanks (67.000 BBL. Tank Size) - 5171. 4226
Gasoline RVP13: Standing Loss
Gasoline RVP10: Standing Loss
Gasoline RVP7: Standing Loss
Gasoline RVP13/10/7: Withdrawal
Loss
Variable Vaoor Soace Tanks - (10.500 BBL. Tank)
4-04-002-11 -
4-04-002-12 -
4-04-002-13 -
Miscellaneous
4-04-002-50 -
4-04-002-51 -
4-04-002-54 -
Gasoline RVP13: Filling Loss
Gasoline RVP10: Filling Loss
Gasoline RVP7: Filling Loss
Losses/Leaks - 5171. 4226
Loading Racks
Valves, Flanges and Pumps
Tank Truck Vapor Losses
0
0
0
0
- 5171.
0
0
0
0
0
0
.0
.0
.0
.0
4226
.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
18.2
13.4
8.6
0.0019
9.6
7.7
5.4
*0.7
•0.025
0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
0
0
0
0
0
0
0
0
0
0
Oil Field Storace of Crude Oil - 1311
4-04-003-01 -
4-04-003-02 -
4-04-003-03 -
4-04-003-04 -
4-04-003-05 -
Fixed Roof Tank: Breathing Loss
Fixed Roof Tank: Working Loss
External Floating Roof Tank with
Primary Seals: Standing Loss
External Floating Roof Tank with
Secondary Seals: Standing Loss
Internal Floating Roof Tank:
Standing Loss
Petroleum Product Storace - Underground Tanks -
4-04-004-01 -
4-04-004-02 -
4-04-004-03 -
4-04-004-04 -
4-04-004-05 -
4-04-004-06 -
4-04-004-07 -
4-04-004-08 -
Gasoline RVP13: Breathing Loss
Gasoline RVP13: Working Loss
Gasoline RVP10: Breathing Loss
Gasoline RVP10: Working Loss
Gasoline RVP7: Breathing Loss
Gasoline RVP7: Working Loss
Crude Oil RVP5. Breathing Loss
Crude Oil RVP5: Working Loss
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
•28
•7.2
•1.6
•0.08
•0.02
0.
0.
0.
0.
0.
0
0
0
0
0
5171. 4226
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
*HEG
•14.7
•NEC
•11.9
•MEG
*8.3
•MEG
•4.9
0.
0.
0.
0.
0.
0.
0.
0.
0
0
0
0
0
0
0
0
10 Gallons
Capacity
10 Gallons
Capacity
10 Gallons
Capacity
10 Gallons
10 Gallons
l
-------
sec
Process
PART
Lbs/Unlt
so
Lbs/finlt
NO
Lbs/finlt
voc
Lbs/Unlt
CO
Lbs/Unlt
Petroleum Product Storage - Underground Tanks - 5171, 4226 (Continued)
4-04-004-09
4-04-004-10
4-04-004-11
4-04-004-12
4-04-004-13
4-04-004-14
4-04-004-97
4-04-004-98
- Jet Naphtha JP-4: Breathing Loss
- Jet Naphtha JP-4: Working Loss
- Jet Kerosene: Breathing Loss
- Jet Kerosene: Working Loss
- Distillate Fuel 12: Breathing
Loss
- Distillate Fuel »2: Working Loss
- Specify Liquid: Breathing Loss
- Specify Liquid: Working Loss
0
0
0.
0
0
o,
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
*NEG
*3.6
•NEC
*0.04
*NEG
*0.03
0.0
0.0
0.0
0.0
0.0
0.0
0.0
0.0
Units
3
10 Gallons
Capacity
10 Gallons
10 Gallons
Caoaclty
10 Gallons
10 Gallons
Caoaclty
10 Gallons
10 Gallons
Caoaclty
10 Gallons
Storage
Throughput
Storage
Throughput
Storage
Throughput
Storage
Throughput
Dotes
215
215
215
215
215
215
PRINTING/PUBLISHING - PRINTING PROCESS - MAJOR GROUP 27
Dryers - 2711
through 2782
4-05-001-01 - Dryer
4-05-001-99 - Dryer
ro Printing - 2751. 2752. 2754
00 4-05-002-01 -
4-05-002-11 -
4-05-002-12 -
4-05-003-01 -
4-05-003-11 -
4-05-003-12 -
4-05-004-01 -
4-05-004-11 -
4-05-004-12 -
4-05-004-13 -
4-05-005-01 -
4-05-005-11 -
4-05-005-12 -
4-05-005-13 -
4-05-006-01 -
4-05-007-01 -
Ink Thinning
4-05-003-02 -
4-05-003-03 -
4-05-005-02 -
4-05-005-03 -
4-05-003-04 -
Letter Press - 2751
Letter Press - 2751
Letter Press - 2751
Flexographlc - 2751
Flexographlc * 2751
Flexographlc - 2751
Lithographic - 2752
Lithographic - 2752
Lithographic - 2752
Llthographlc-Isopropyl Alcohol
Cleanup
Gravure - 2754
Gravure - 2754
Gravure - 2754
Gravure: Publication Printing -
2754
Ink Mixing: General
Solvent Storage: General
Solvents - 2700-2799*"
Carbltol
Cellosolve
Dljoethylformamlde
Ethyl Acetate
Ethyl Alcohol
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
*150
0.
0.
0.
0.
0.
0.
0,
0.
0,
0.
0.
0,
0.
0,
0.
0.
0.
0.
0.
0.
0
s
.0
0
.0
0
.0
,0
.0
.0
,0
,0
.0
.0
,0
.0
.0
,0
.0
.0
,0
.0
.0
*32
0.0
0.0
0.0
0.0
0.0
0.0
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
0.0
0.0
*2000.
420,
1200
1,
1240.
1910
4.
350
1000,
1
2000,
1240
1910
4
12
*2000,
•2000,
*2000,
•2000
*2000
*2000
d
.0
.0
.0
.5
.0
.0
.4
.0
.0
.24
.0
.0
.0
.4
.4
d
.od
I
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
Tons Solvent
Gallons Ink
Tons Ink
Tons Solvent
Gallons Ink
Tons Ink
Tons Solvent
Gallons Ink
Tons Ink
Tons Solvent
Gallons Ink
Tons Solvent
Tons Ink
Tons Solvent
Gallons Ink
Gallons Ink
Tons Solvent
Tons Solvent
Tons Solvent
Tons Solvent
Tons Solvent
Tons Solvent
Tons Solvent
In Ink 74, 291
In Ink
in Ink
In Ink
Used
in Ink
in Ink
Stored
Added
Added
Added
Added
Added
*Refer to numbered notes In Appendix A or lettered notes In Appendix B; factors without asterisks are from AP-42.
-------
SCO Process
Ink Thlnnln* Solvents - 2700-2799 (Continued!*"
4-05-003-05 - Isopropyl Alcohol
4-05-002-02 - Kerosene
4-05-005-06 - Methyl Ethyl Ketone
4-05-005-07 - Methyl Isobutyl Ketone
4-05-002-03 - Mineral Spirits
4-05-003-07 - Naphtha
4-05-003-06 - N-Propyl Alcohol
4-05-005-10 - Toluene
4-05-005-98 - Other Mot Classified (Specify
In Comments)
4-05-005-99 - Other Hot Classified (Specify
In Comments)
Printing/Publishing - Punitive Emissions*
4-05-888-01 - Specify In Comments Field*
4-05-888-02 - Specify In Cooments Field*
4-05-888-03 - Specify In Comments Field*
4-05-888-04 - Specify In Comnents Field*
4-05-888-05 - Specify In Comnents Field*
TRANSPORTATION AND MARKETING OF PETROLEUM PRODUCTS
Tank Cars and Trucks - Normal Service - 5161. 5171.
4-06-001-31 - Gasoline-Submerged Loading
4-06-001-32 - Crude Oil-Submerged Loading
4-06-001-33 - Jec Naphtha (JP- 4) -Submerged
Loading
4-06-001-34 - Jet Kerosene-Submerged Loading
4-06-001-35 - Distillate Oil *2-Submerged
Loading
4-06-001-36 - Gasoline-Splash Loading
4-06-001-37 - Crude Oil-Splash Loading
4-06-001-38 - Jet Naphtha- Splash Loading
4-06-001-39 - Jet Kerosene-Splash Loading
4-06-001-40 - Distillate Oil *2-Splash Loading
Tank Cars and Trucks - Balance Service - 5161, 5171
4-06-001-41 - Gasoline-Submerged Loading
4-06-001-42 - Crude Oil -Submerged Loading
4-06-001-43 - Jet Naphtha-Submerged Loading
4-06-001-44 - Gasoline-Splash Loading
4-06-001-45 - Crude Oil-Splash Loading
4-06-001-46 - Jet Naphtha-Splash Loading
PART
Lbs/Unlt
0.0
0.0
0.0
0.0
0.0
0.0
0.0
0.0
0.0
0.0
- MAJOR GROUPS
5172. 4582
0.0
0.0
0.0
0.0
0.0
0.0
0.0
0.0
0.0
0.0
. 5172, 4582
0.0
0.0
0.0
0.0
0.0
0.0
SO
Lbs/Qnlt
0.0
0.0
0.0
0.0
0.0
0.0
0.0
0.0
0.0
0.0
44. 45. 51
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
NO
Lbs/finlt
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
0.0
0.0
voc
Lbs/Unlt
*2000 . 0*|
•2000.0*
•2000.0*
•2000.0*
•2000.0*
•2000.0*
•2000.0*
•2000.0
5.0
2.8
1.5
0.02
0.01
12.0
6.6
4.0
0.04
0.03
8.0
4.7
2.5
8.0
4.7
2.5
CO
Lbs/Unlt
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
0.0
0.0
Units Notes
Tons Solvent Added
Tons Solvent Added
Tons Solvent Added
Tons Solvent Added
Tons Solvent Added
Tons Solvent Added
Tons Solvent Added
TODS Solvent Added
10 Gallons Solvent
Tons Solvent Added
Process Unit-Year
Process Unit-Year
Process Unit-Year
Process Unit-Year
Process Unit-Year
10 Gallons Transferred
10 Gallons Transferred
10 Gallons Transferred
10 Gallons Transferred
10 Gallons Transferred
q
10, Gallons Transferred
10 Gallons Transferred
10 Gallons Transferred
10 Gallons Transferred
10 Gallons Transferred
10 Gallons Transferred
10 Gallons Transferred
10 Gallons Transferred
10 Gallons Transferred
10 Gallons Transferred
10 Gallons Transferred
Note that fugitive emissions are reported In units of Ibs/process unit-year rather than Ibs/ton product as In the NEDS Source Classification Codes
and Emission Factor Listing dated October 1985.
Refer to numbered notes In Appendix A or lettered notes In Appendix B; factors without asterisks are from AP-42.
-------
sec
Process
PART
Lbs/Unit
so
Lbs/Unit
NO
Lbs/Unit
voc
Lbs/Unit
CO
Lbs/Unit
Units Notes
Tank Cars and Trucks - Clean Tanks - 5161, 5171. 5172. 4582
4-06-001-47
4-06-001-48
4-06-001-49
4-06-001-60
4-06-001-61
4-06-001-62
4-06-001-63
- Gasoline-Submerged Loading
- Crude Oil-Submerged Loading
- Jet Naphtha (JP-4) -Submerged
Loading
- Jet Kerosene-Submerged Loading
- Distillate Oil *2-Submerged
Loading
- Gasoline -Loaded with Fuel
- Gasoline-Return with Vapor
0.0
0.0
0.0
0.0
0.0
5172 458
0.0
0.0
0
0
0
0
0
1?
0
0
.0
.0
.0
.0
.0
.0
.0
0.0
0.0
0.0
0.0
0.0
0.0
0.0
4
2
1
0
0
0
0
.0
.4
.25
.02
.008
.005
.055
0.0
0.0
0.0
0.0
0.0
0.0
0.0
IO3 Gallons
io3
io3
"I
io3
io3
Gallons
Gallons
Gallons
Gallons
Gallons
Gallons
Transferred
Transferred
Transferred
Transferred
Transferred
Transferred
Transferred
Marine Vessels - 4463
4-06-002-31
4-06-002-32
4-06-002-33
4-06-022-34
4-06-002-35
4-06-002-36
4-06-002-37
4-06-002-38
4-06-002-39
4-06-002-40
4-06-002-41
4-06-002-42
4-06-002-43
4-06-002-44
4-06-002-45
4-06-002-46
4-06-002-48
4-06-002-49
4-06-002-50
4-06-002-51
- Gasoline-Ship Loading-Cleaned and
Vapor-free Tank
- Gasoline-Ocean Barges Loading
- Gasoline-Barges Loading-Cleaned
and Vapor-free Tank
- Gasoline-Ship Loading-Ballasted
Tank
- Gasoline-Ocean Barges Loading-
Ballasted Tank
- Gasoline-Ship Loadlng-Uncleaned
Tank
- Gasoline-Ocean Barges Loading-
Uncleaned Tank
- Gasoline-Barges Loading-Uncleaned
Tank
- Gasoline-Tanker-Ballasting Tank
Condition
- Gasoline-Barges Loading-Average
Tank Condition
- Gasoline-Tanker-Ballasting
- Gasoline-Transit
- Crude Oil-Loading Tankers
- Jet Fuel-Loading Tankers
- Kerosene-Loading Tankers
- Distillate Oil No. 2 Loading
- Crude Oil-Loading Barges
- Jet Fuel-Loading Barges
- Kerosene-Loading Barges
- Distillate Oil No. 2-Loading
Tankers
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
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
0.0
0.0
0.0
0.0
0.0
0.0
0.0
0.0
0.0
0.0
0.0
0.0
1
1
.0
.3
1.2
1.6
2.1
2.
3.
4.
1.
4.
0.
156.
0.
0.
0.
0.
1.
1.
0.
0.
,4
3
0
4
0
8
0
68
5
005
005
6
2
013
012
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
io3
io3
io3
io3
io3
io3
io3
io3
io3
io3
io3
io3
io3
10?
10
10
10?
103
10
10
Gallons
Gallons
Gallons
Gallons
Gallons
Gallons
Gallons
Gallons
Gallons
Gallons
Gallons
Gallons
Gallons
Gallons
Gallons
Gallons
Gallons
Gallons
Gallons
Gallons
Transferred
Transferred
Transferred
Transferred
Transferred
Transferred
Transferred
Transferred
Transferred
Transferred
Transferred
Transferred
Transferred
Transferred
Transferred
Transferred
Transferred
Transferred
Transferred
Transferred
-------
SCC Process
Marine Vessels - 4463 (Continued)
4-06-002-53 - Crude Oil-Tanker Ballasting
4-06-002-5* - Crude Oil-Transit-Los»
4-06-002-55 - Jet Fuel-Transit Loss
4-06-002-56 - Kerosene-Trans it-Loss
4-06-002-57 - Distillate Oil Ho. 2-Transit-Loss
4-06-002-59 - Tanker/Barge Cleaning
Gasoline Retail Operations - 5541
4-06-003-01 - Splash Filling
4-06-003-02 - Submerged Filling without Control
4-06-003-06 - Balanced Submerged Filling
4-06-003-07 - Underground Tank Breathing
Fillln* Vehicle Gas Tanks - 5541
4-06-004-01 - Vapor Loss: without Controls
4-06-004-02 - Liquid Spill Loss: without
Controls
4-06-004-03 - Vapor Loss: without Controls
4-06-888-01 - Specify in Comment i Field*
4-06-888-02 - Specify in Comments Field!
4-06-888-03 - Specify in Comments Field!
4-06-888-04 - Specify in Comments Field!
4-06-888-05 - Specify in Comments Field!
ORGANIC HHEMTr.AL STORAGE - FIXED ROOF TANKS - MAJOR
Acid Anhydrides
4-07-004-01 - Acetic Anhydride: Breathing Loss
4-07-004-02 - Acetic Anhydride: Working Loss
4-07-004-97 - Specify Liquid: Breathing Loss
4-07-004-98 - Specify Liquid: Working Loss
*
PART
Lbs/Onit
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
GROUPS 28.
0.0
0.0
0.0
0.0
rtf 1 K« /ni"n
SO
Lbs/Unit
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
29. 30. 51
0.0
0.0
0.0
0.0
fm «« iin 1 t* — ua»ai
NO
Lbs/unit
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
- *-»*-hj»*- frhan
voc
Lbs/Unit
0.57
49.0
36.4
0.26
0.26
11.5
7.3
0.3
1.0
11.0
0.67
0.9
•1.1
*0.13
iK«/m oal 1
CO
Lbs/Unit
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
rtn* trlSmnff Kr
Units Notes
10 Gallons Total Cargo
Capacity
10 Gallons Total Cargo
Capacity
10 Gallons Total Cargo
Capacity
10 Gallons Total Cargo
Capacity
10 Gallons Total Cargo
Capacity
10 Gallons Cargo
Capacity Cleaned
10 Gallons Transferred
10 Gallons Transferred
10 Gallons Throughput
10 Gallons Throughput
10 Gallons Pumped
10 Gallons Pumped
10 Gallons Transferred
Process Unit-Year
Process Unit-Year
Process Unit-Year
Process Unit-Year
Process Unit-Year
3
10 Gallons Storage 73
Capacity
10 Gallons Throughput 73
10 Gallons Storage
Capacity
10 Gallons Throughput
nit- a« In the NEDS Source
Classification Codes and Emission Factor Listing dated October 1985.
Refer to numbered notes in Appendix A or lettered notes in Appendix B: factors without
-------
GO
sec
Alcohols
4-07-008-01
4-07-008-02
4-07-008-03
4-07-008-04
4-07-008-05
4-07-008-06
4-07-008-07
4-07-008-08
4-07-008-09
4-07-008-10
4-07-008-11
4-07-008-12
4-07-008-13
4-07-008-14
4-07-008-15
4-07-008-16
4-07-008-17
4-07-008-18
4-07-008-97
4-07-008-98
Process
- N-Butyl Alcohol: Breathing Loss
- N-Butyl Alcohol: Working Loss
- Sec-Butyl Alcohol: Breathing Loss
- Sec-Butyl Alcohol: Working Loss
- Tert-Butyl Alcohol: Breathing
Loss
- Tert-Butyl Alcohol: Working Loss
- Cyclohexanol : Breathing Loss
- Cyclohexanol: Working Loss
- Ethyl Alcohol: Breathing Loss
- Ethyl Alcohol: Working Loss
- Isobutyl Alcohol: Breathing Loss
- Isobutyl Alcohol: Working Loss
- Isobutyl Alcohol: Breathing Loss
- Isopropyl Alcohol: Working Loss
- Methyl Alcohol: Breathing Loss
- Methyl Alcohol: Working Loss
- H-Propyl Alcohol: Breathing Loss
- N-Propyl Alcohol: Working Loss
- Specify Alcohol: Breathing Loss
- Specify Alcohol: Working Loss
PART
Lbs/Unit
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
so
Lbs/finit
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
NO
Lbs/finit
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
voc
Lbs/Unit
*0
*0
*2
*0
*3
*0
*0
*0
*2
*0
*1
*0
*3
*0
*3
*1
*1
*0
.73
.01
.2
.32
.6
.76
.73
.046
.9
.66
.5
.17
.6
.86
.6
.07
.8
.29
CO
Lbs/Unit Units
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
Alkanes (Paraffins )
4-07-016-01
4-07-016-02
4-07-016-03
4-07-016-04
4-07-016-05
4-07-016-06
4-07-016-09
4-07-016-10
- N-Decane: Breathing Loss
- N-Decane: Working Loss
- N-Dodecane: Breathing Loss
- N-Dodecane: Working Loss
- N-Heptane: Breathing Loss
- N-Heptane: Working Loss
- Pentadecane: Breathing Loss
- Pentadecane : Working Loss
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
*0.
*0.
*0.
*0.
*5.
*1.
*0.
*0.
73
04
15
004
8
3
04
0008
0.0
0.0
0.0
0.0
0.0
0.0
0.0
0.0
103 Gallons
Capacity
10 Gallons
10 Gallons
Capacity
10* Gallons
10 Gallons
Capacity
10 Gallons
10 Gallons
Capacity
10* Gallons
10 Gallons
Capacity
10 Gallons
10 Gallons
Capacity
10 Gallons
10 Gallons
Capacity
10 Gallons
10 Gallons
Capacity
10* Gallons
10 Gallons
Capacity
10. Gallons
10 Gallons
Capacity
10 Gallons
3
10 Gallons
Capacity
10 Gallons
10 Gallons
Capacity
10* Gallons
10 Gallons
Capacity
10* Gallons
10 Gallons
Capacity
10 Gallons
Storage
Throughput
Storage
Throughput
Storage
Throughput
Storage
Throughput
Storage
Throughput
Storage
Throughput
Storage
Throughput
Storage
Throughput
Storage
Throughput
Storage
Throughput
Storage
Throughput
Storage
Throughput
Storage
Throughput
Storage
Throughput
Notes
73
73
73
73
73
73
73
73
73
73
73
73
73
73
73
73
73
73
73
73
73
73
73
73
73
73
Refer to numbered notes in Appendix A or lettered notes in Appendix B; factors without asterisks are from AF-42.
-------
sec
Process
PART
Lbs/Unit
so
Lbs/Bnlt
NO
Lbs/Unit
VOC CO
Lbs/Unit Lbs/Unit Units
Alkanes (Paraffins) (Continued)
4-07-016-11
4-07-016-12
4-07-016-13
4-07-016-14
4-07-016-97
4-07-016-98
- Naphtha: Breathing Loss
- Naphtha: Working Loss
- Petroleum Distillate: Breathing
Loss
- Petroleum Distillate: Working
Loss
- Specify Alkane: Breathing Loss
- Specify Alkane: Working Loss
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
*0.15 0.
*0.006 0.
•0.15 0.
*0.006 0.
0.
0.
0
0
0
0
0
0
10 Gallons
Capacity
10 Gallons
10 Gallons
Capacity
10 Gallons
103 Gallons
Capacity
10 Gallons
Storage
Throughput
Storage
Throughput
Storage
Throughput
Notes
73
73
73, 227
73, 227
Alkenes (Oleflns)
4-07-020-01
4-07-020-02
4-07-020-03
4-07-020-04
4-07-020-97
i—1
CO 4-07-020-98
CO
Amines
4-07-032-01
4-07-032-02
4-07-032-03
4-07-032-04
4-07-032-05
4-07-032-06
4-07-032-97
4-07-032-98
Aromatics
4-07-036-01
4-07-036-02
4-07-036-03
4-07-036-04
- Dodecene: Breathing Loss
- Dodecene: Working Loss
- Heptanes-General: Breathing Loss
- Heptenes -General: Working Loss
- Specify Alkene: Breathing Loss
- Specify Alkene: Working Loss
- Aniline: Breathing Loss
- Aniline: Working Loss
- Ethanolamines : Breathing Loss
* Ethanolamines: Working Loss
- Ethyleneamines: Breathing Loss
- Ethyleneamines : Working Loss
- Specify Amine: Breathing Loss
- Specify Amlne: Working Loss
- Benzene: Breathing Loss
- Benzene: Working Loss
- Cresol: Breathing Loss
- Cresol: Working Loss
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.
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
0.0
0.0
0.0
0.0
0.0
0.0
*0.15 0.
•0.005 0.
0.
0.
0.
0.
*0.22 0.
•0.13 0.
*0.11 0.
•0.004 0.
*7.3 0.
•2.5 0.
0.
0.
•8.0 0.
•2.25 0.
•0.11 0.
•0.005 0.
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
10 Gallons
Capacity
10 Gallons
10 Gallons
Capacity
1CT Gallons
10 Gallons
Capacity
10 Gallons
103 Gallons
Capac ity
1CT Gallons
10 Gallons
Capacity
10 Gallons
10 Gallons
Capacity
1CT Gallons
10 Gallons
Capacity
10 Gallons
Q
10 Gallons
Capacity
1CT Gallons
10 Gallons
Capacity
10 Gallons
Storage
Throughput
Storage
Throughput
Storage
Throughput
Storage
Throughput
Storage
Throughput
Storage
Throughput
Storage
Throughput
Storage
Throughput
Storage
Throughput
73
73
73
73
73
73
73
73
73
73
73
73
*
Refer to numbered notes in Appendix A or lettered notes in Appendix B; factors without asterisks are from AP-42.
-------
CO
sec
Process
PART
Lbs/Unit
so
Lbs/unit
NO
Lbs/finlt
voc
Lbs/Unit
CO
Lbs/Unit Units
Notes
Aromatlcs (Cont inued )
4-07-036-05
4-07-036-06
4-07-036-07
4-07-036-08
4-07-036-09
4-07-036-10
4-07-036-11
4-07-036-12
4-07-036-13
4-07-036-14
4-07-036-15
4-07-036-16
4-07-036-17
4-07-036-18
4-07-036-19
4-07-036-20
4-07-036-21
4-07-036-22
4-07-036-23
4-07-036-24
4-07-036-97
4-07-036-98
- Cumene: Breathing Loss
- Cumene: Working Loss
- Diisopropyl Benzene: Breathing
Loss
- Diisopropyl Benzene: Working Loss
- Ethyl Benzene: Breathing Loss
- Ethyl Benzene : Working Loss
- Methylstyrene: Breathing Loss
- Methylstyrene : Working Loss
- Styrene: Breathing Loss
- Styrene: Working Loss
- Toluene: Breathing Loss
- Toluene: Working Loss
- m-Xylene: Breathing Loss
- m-Xylene: Working Loss
- o-Xylene: Breathing Loss
- o-Xylene: Working Loss
- p-Xylene: Breathing Loss
- p-Xylene: Working Loss
- Xylenes -mixed: Breathing Loss
- Xylenes-mixed: Working Loss
- Specify Aromatic: Breathing Loss
- Specify Aromatic: Working Loss
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
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
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
*1
*0
*0
*0
*1
*0
*0
*0
*1
*0
*3
*0
*1
*0
*1
*0
•1
*0
.5
.16
.03
.001
.8
.27
.73
.05
.5
.17
.6
.66
.8
.23
.5
.18
.8
.24
•0.02
*1.4
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
Carboxyllc Acids
4-07-040-01
4-07-040-02
4-07-040-03
4-07-040-04
4-07-040-05
- Acetic Acid: Breathing Loss
- Acetic Acid: Working Loss
- Acrylic Acid: Breathing Loss
- Acrylic Acid: Working Loss
- Adipic Acid: Breathing Loss
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
*1.5
*0.24
*0.73
*0.
*0.
64
0003
0.0
0.0
0.0
0.0
0.0
10 Gallons
Capacity
10 Gallons
10 Gallons
Capacity
10 Gallons
10 Gallons
Capacity
10 Gallons
10 Gallons
Capacity
10* Gallons
10 Gallons
Capacity
10 Gallons
10 Gallons
Capacity
1(T Gallons
10 Gallons
Capacity
10 Gallons
10 Gallons
Capacity
10 Gallons
10 Gallons
Capacity
10 Gallons
10 Gallons
Capacity
10 Gallons
10 Gallons
Capacity
10 Gallons
o
10 Gallons
Capacity
10 Gallons
10 Gallons
Capacity
10 Gallons
10 Gallons
Capacity
Storage
Throughput
Storage
Throughput
Storage
Throughput
Storage
Throughput
Storage
Throughput
Storage
Throughput
Storage
Throughput
Storage
Throughput
Storage
Throughput
Storage
Throughput
Storage
Throughput
Storage
Throughput
Storage
Throughput
Storage
73
73
73
73
73
73
73
73
73
73
73
73
73
73
73
73
73
73
73
73
73
73
73
73
73
Refer to numbered notes in Appendix A or lettered notes in Appendix B; factors without asterisks are from AP-42.
-------
sec
Process
PART
Lbs/Unit
so
Lbs/ftnit
NO
Lbs/Unit
voc
Lbs/Unit
CO
Lbs/Unit
Carboxylic Acids (Continued)
4-07-0*0-06
4-07-0*0-07
4-07-0*0-08
4-07-040-09
4-07-040-10
4-07-040-97
4-07-040-98
Esters
4-07-044-01
4-07-044-02
4-07-044-03
4-07-044-04
4-07-044-05
1 *
CO
en *-07-0**-06
4-07-044-07
4-07-044-08
4-07-044-09
4-07-044-10
*-07-0**-ll
4-07-044-12
4-07-044-13
4-07-044-1*
4-07-044-15
4-07-0**-16
4-07-0*4-17
4-07-044-18
4-07-044-19
4-07-044-20
4-07-044-21
- Adipic Acid: Working Loss
- Formic Acid: Breathing Loss
- Formic Acid: Working Loss
- Propionic Acid: Breathing Loss
- Propionic Acid: Working Loss
- Specify Acid: Breathing Loss
- Specify Acid: Working Los*
- Butyl Acetate: Breathing Loss
- Butyl Acetate: Working Loss
- Butyl Aery late: Breathing Loss
- Butyl Acrylate: Working Loss
- Ethyl Acetate: Breathing Loss
- Ethyl Acetate: Working Loss
- Ethyl Acrylate: Breathing Loss
- Ethyl Acrylate: Working Loss
- Isobutyl Acrylate: Breathing Loss
- Isobutyl Acrylate: Working Loss
- Isopropyl Acetate: Breathing Loss
- Isopropyl Acetate: Working Loss
- Methyl Acetate: Breathing Loss
- Methyl Acetate: Working Loss
- Methyl Acrylate: Breathing Loss
- Methyl Acrylate: Working Loss
- Methyl Methacrylate : Breathing
Loss
- Methyl Methacrylate: Working Loss
- Vinyl Acetate: Breathing Loss
- Vinyl Acetate: Working Loss
- n-Propyl Acetate: Breathing Loss
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
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
.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
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
*2
*0
*0
*0
*2
*0
*1
•0
*8
*2
*5
*1
*0
*0
*7
*1
*14
*4
*8
*2
•3
•0
*9
•2
•0
.0
.6
.57
.73
.06
.2
.34
.57
.2
.4
.3
.1
.1
.31
.006
.3
.8
.2
.8
.0
.2
.6
.7
.1
.7
.01
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
0.0
0.0
0.0
0.0
Units
3
10 Gallons
10 Gal Ions
Capacity
10 Gallons
Throughput
Storage
Throughput
Day - 10 Gallons Storage
Capacity
10 Gallons
Throughput
Notes
73
73
73
73
73
Day - 10 Gallons Storage
Capacity
10 Gallons
3
10 Gallons
Capacity
10 Gallons
10 Gallons
Caoaclty
10 Gallons
10 Gallons
Capacity
10 Gallons
10 Gallons
Capacity
10 Gallons
10 Gallons
Capacity
10 Gallons
10 Gallons
Capacity
10 Gallons
10 Gallons
Capacity
10 Gallons
10 Gallons
Capacity
10 Gallons
10 Gallons
Capacity
10 Gallons
10 Gallons
Capacity
10 Gallons
10 Gallons
Capacity
Throughput
Storage
Throughput
Storage
Throughput
Storage
Throughput
Storage
Throughput
Storage
Throughput
Storage
Throughput
Storage
Throughput
Storage
Throughput
Storage
Throughput
Storage
Throughput
Storage
73
73
73
73
73
73
73
73
73
73
73
73
73
73
73
73
73
73
73
73
73
*Refer to numbered notes in Appendix A or lettered notes in Appendix B; factors without asterisks are from AP-42.
-------
sec
Process
PART
Lbs/Unit
so
Lbs/unit
NO
Lbs/unit
voc
LbsfUnlt
CO
Lbs/Unit
Esters (Continued)
4-07-0*4-22 -
4-07-044-23 -
4-07-044-24 -
4-07-044-97 -
4-07-044-98 -
Ethers
4-07-048-01 -
4-07-048-02 -
4-07-048-97 -
4-07-048-98 -
*~~* Glvcol Ethers
CT> 4-07-052-01 -
4-07-052-02 -
4-07-052-03 -
4-07-052-04 -
4-07-052-05 -
4-07-052-06 -
4-07-052-07 -
4-07-052-08 -
4-07-052-09 -
4-07-052-10 -
4-07-052-11 -
4-07-052-12 -
4-07-052-13 -
4-07-052-14 -
4-07-052-15 -
4-07-052-16 -
4-07-052-17 -
n-Propyl Acetate: Working Loss
i-Butyl-l-Butyrete: Breathing
Loss
l-Butyl-i-Butyr»te: Working Loss
Specify Ester: Breathing Loss
Specify Ester: Working Loss
Methyl-tert-Butyl Ether:
Breathing Losa
Methyl-tert-Butyl Ether: Working
Loss
Specify Ether: Breathing Loss
Specify Ether: Working Loss
fff
Butyl Carbltol: Breathing Loss
Butyl Carbitol: Working Loss
Butyl Cellosolve: Breathing Loss
Butyl Cellosolve: Working Loss
Carbitol: Breathing Loss
Carbitol: Working Loss
Cellosolve: Breathing Loss
Cellosolve: Working Loss
Diethylene Glycol: Breathing Loss
Diethylene Glycol: Working Loss
Methyl Carbitol: Breathing Loss
Methyl Carbitol: Working Loss
Methyl Cellosolve: Breathing Loss
Methyl Cellosolve: Working Loss
Polyethylene Glycol: Breathing
Loss
Polyethylene Glycol: Working Loss
Trlethylene Glycol: Breathing
Loss
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
o
0
,0
0
,0
,0
.0
0
,0
,0
o
,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
0.0
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
0.0
0.0
0.0
0.0
0.0
0.0
0.0
0.0
0.0
*1.
*0.
*0.
*0.
*9.
*0.
*0.
*0.
*0.
•0.
*0.
*0.
*0.
*0.
*0.
*0.
*0.
*0.
*0.
*0.
*0.
*0.
1
006
27
07
2
001
01
001
03
0005
006
004
16
003
0
0004
006
004
22
0
0
0
0.0
0.0
P-
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
Units
3
10 Gallons
10 Gallons
Capacity
10 Gallons
10 Gallons
Capacity
10 Gallons
3
10 Gallons
Capacity
10 Gallons
3
10 Gallons
Capacity
10 Gallons
3
10 Gallons
Capacity
10 Gallons
10 Gallons
Capacity
10 Gallons
10 Gallons
Capacity
10 Gallons
10 Gallons
Capacity
10 Gallons
10 Gallons
Capacity
1CT Gallons
10 Gallons
Capacity
10 Gallons
10 Gallons
Capacity
10, Gallons
10' Gallons
Capacity
lo' Gallons
10 Gallons
Capacity
Throughput
Storage
Throughput
Storage
Throughput
Storage
Throughput
Storage
Throughput
Storage
Throughput
Storage
Throughput
Storage
Throughput
Storage
Throughput
Storage
Throughput
Storage
Throughput
Storage
Throughput
Storage
Throughput
Storage
Hotel
73
73
73
73
73
73
73
73
73
73
73
73
73
73
73
73
73
73
73
73
73
73
*Refer to numbered notes in Appendix A or lettered notes in Appendix B; factors without asterisks are from AP-42.
-------
CO
sec
Process
PART
Lbs/Unit
so
Lbs/ffnlt
HO
Lbj/finlt
voc
Lbs/Unit
CO
Lbs/Unit
Glycol Ethers (Continued)
4-07-052-18
4-07-052-97
4-07-052-98
Glycols
4-07-056-01
4-07-056-02
4-07-056-03
4-07-056-04
4-07-056-05
4-07-056-06
4-07-056-07
4-07-056-08
4-07-056-09
4-07-056-10
4-07-056-97
4-07-056-98
Halogenated
4-07-060-01
4-07-060-02
4-07-060-03
4-07-060-04
4-07-060-05
4-07-060-06
4-07-060-07
4-07-060-08
4-07-060-09
4-07-060-10
- Trlethylene Clycol : Working Loss
- Specify Glycol Ether: Breathing
Loss
- Specify Glycol Ether: Working
Loss
- 1,4-Butanediol: Breathing Loss
- 1,4-Butanedlol: Working Loss
- Ethylene Glycol: Breathing Loss
- Ethylene Glycol: Working Loss
- Dipropylene Glycol: Breathing
Loss
- Dipropylene Glycol: Working Loss
- Glycerol: Breathing Loss
- Glycerol: Working Loss
- Propylene Glycol: Breathing Loss
- Propylene Glycol: Working Loss
- Specify Glycol: Breathing Loss
- Specify Glycol: Working Loss
Organic*
- Benzyl Chloride: Breathing Loss
- Benzyl Chloride: Working Loss
- Caprolactan: Breathing Loss
- Caprolactaa: Working Loss
- Carbon Tetrachloride: Breathing
Loss
- Carbon Tetrachloride: Working
Loss
- Chlorobenzene: Breathing Loss
- Chlorobenzene: Working Loss
- o-Dichlorobenzene: Breathing Loss
- o-Dichlorobenzene: Working Loss
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
.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
.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
0.0
0.0
0.0
•0.0
•NEC
•NEC
•0.036
•0.02
•0.0002
•0.013
•0.0
•0.0
•0.007
•0.0
•0.05
•0 . 002
•MEG
•NEC
•17.9
•5.2
•2.5
•0.36
•0.73
•0.05
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
0.0
Units
3
10 Gallons
10 Gallons
Capacity
10 Gallons
103 Gallons
Capacity
lo' Gallons
10 Gallons
Capacity
10 Gallons
10 Gallons
Capacity
10, Gallons
10 Gallons
Capacity
10 Gallons
10 Gallons
Capacity
10* Gallons
10 Gallons
Capacity
10 Gallons
0
10 Gallons
Capacity
10 Gallons
10 Gallons
Capacity
10 Gallons
10 Gallons
Capacity
10 Gallons
.
10 Gallons
Capacity
10* Gallons
10 Gallons
Capacity
10 Gallons
Throughput
Storage
Throughput
Storage
Throughput
Storage
Throughput
Storage
Throughput
Storage
Throughput
Storage
Throughput
Storage
Throughput
Storage
Throughput
Storage
Throughput
Storage
Throughput
Storage
Throughput
Storage
Throughput
Notes
73
232
232
73
73
73
73
73
73
73
73
73
73
232
232
73
73
73
73
73
73
_ r i_ _ j , i_ A _.li_» A _~ 1 A* •• AV.A A w\*** ^m 1 *. AnnAnfl Iv R. fa/.*-m-« ul t-Kntif mmfmri «lrs air A f ran AP— A 2 .
-------
sec
Halogenated
4-07-060-11
4-07-060-12
4-07-060-13
4-07-060-14
4-07-060-15
4-07-060-16
4-07-060-17
4-07-060-18
4-07-060-19
4-07-060-20
4-07-060-21
4-07-060-22
,_. 4-07-060-23
CO
CD
4-07-060-24
4-07-060-97
4-07-060-98
Isocyanatea
4-07-064-01
4-07-064-02
4-07-064-03
4-07-064-04
4-07-064-97
4-07-064-98
Re tone 5
4-07-068-01
4-07-068-02
4-07-068-13
4-07-068-14
Process
Oraanl.es (Continued)
- p-Dichlorobensene : Breathing Loss
- p-Dichlorobenzene: Working Loss
- Epichlorohydrln: Breathing Loss
- Epichlorohydrln: Working Loss
- Ethylene Dibromlde: Breathing
Loss
- Ethylene Dlbroulde: Working Loss
- Ethylene Dlchlori.de: Breathing
Loss
- Ethylene Dlchlorlde: Working Loss
- Methylene Chloride: Breathing
Loss
- Methylene Chloride: Working Loss
- Perchloroethylene: Breathing Loss
- Perchloroethylene: Working Loss
- Trlchloroethylene: Breathing Loss
- Trlchloroethylene: Working Loss
- Specify In Comments: Breathing
Loss
- Specify In Cooments : Working Loss
- MDI: Breathing Loss
- MDI: Working Loss
- TDI : Breathing Loss
- TDI: Working Loss
- Specify Isocyanate: Breathing
Loss
- Specify Isocyanate: Working Loss
- Cyclohexanone: Breathing Loss
- Cyclohexanone: Working Loss
- Methylamyl Ketone: Breathing Loss
- Methylamyl Ketone: Working Loss
PART
Lbs/Unlt
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
0
0
0
0
so
Lbs/finit
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
0.0
0.0
NO
Lbs/finit
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
0.0
0.0
voc
Lbs/Unit
*0.73
*0.06
•2.5
*0.40
*4.75
*0.77
*8.8
*2.3
•0.0
*0.0
•5.1
*0.84
*4.4
•2.8
CO
Lbs/Unit Units
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
*NEG
*NEG
*0.036
*0.0008
*1.8
*0.2
*0.0005
*0.008
0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
0
0
0
0
0
0
0
0
0
0
10 Gallons
Capacity
10, Gallons
10 Gallons
Capac ity
10 Gallons
10 Gallons
Capacity
10 Gallons
10 Gallons
Capacity
10 Gallons
10 Gallons
Capacity
10 Gallons
10 Gallons
Capacity
10, Gallons
10 Gallons
Capacity
10 Gallons
10 Gallons
Capacity
10 Gallons
10 Gallons
Capacity
10 Gallons
10 Gallons
Capacity
10, Gallons
10 Gallons
Capacity
10 Gallons
103 Gallons
Capacity
10' Gallons
10 Gallons
Capacity
10 Gallons
Storage
Throughput
Storage
Throughput
Storage
Throughput
Storage
Throughput
Storage
Throughput
Storage
Throughput
Storage
Throughput
Storage
Throughput
Storage
Throughput
Storage
Throughput
Storage
Throughput
Storage
Throughput
Storage
Throughput
Notes
73
73
73
73
73
73
73
73
73
73
73
73
73
73
232
232
73
73
73
73
73
73
*
Refer to numbered notes in Appendix A or lettered notes in Appendix B; factors without asterisks are from AP-42.
-------
10
sec
Process
Ketone a (Continued)
4-07-068-97 - Specify Ketone: Breathing Loss
4-07-068-98 - Specify Ketone: Working Loss
Nltriles
4-07-076-01
4-07-076-02
4-07-076-97
4-07-076-98
- Acrylonltrile: Breathing Loss
- Acrylonltrlle: Working Loss
- Specify Nit rile: Breathing Loss
- Specify Nltrile: Working Loss
PART
Lbs/Unit
0.0
0.0
0
0
0
0
.0
.0
.0
.0
so
Lbs/finit
0
0
0
0
0
0
.0
.0
.0
.0
.0
.0
NO
Lbs/Unit
0.0
0.0
0.0
0.0
0.0
0.0
VOC CO
Lbs/Unit Lbs/Unit Units
0.0
0.0
•6.2 0.0
•1.8 0.0
0.
0
0.0
10 Gallons
Capacity
10 Gallons
103 Gallons
Capacity
10* Gallons
10 Gallons
Capacity
10 Gallons
Storage
Throughput
Storage
Throughput
Storage
Throughput
Notes
73
73
Nitro Compounds
4-07-080-01
4-07-080-02
4-07-080-97
4-07-080-98
Phenols
4-07-084-01
4-07-084-02
4-07-084-03
4-07-084-04
4-07-084-97
4-07-084-98
- Nitrobenzene: Breathing Loss
- Nitrobenzene: Working Loss
- Specify in Comments: Breathing
Loss
- Specify in Comments: Working Loss
- Nonylphenol: Breathing Loss
- Nonylphenol: Working Loss
- Phenol: Breathing Loss
- Phenol: Working Loss
- Specify Phenol: Breathing Loss
- Specify Phenol: Working Loss
ORGANIC CHEMICAL STORAGE - FLOATING ROOF TANKS -
Aldehydes
4-07-172-05
4-07-172-06
4-07-172-07
4-07-172-08
4-07-172-09
4-07-172-10
- N-Butraldehyde: Standing Loss
- N-Butraldehyde: Withdrawal Loss
- Formalin: Standing Loss
- Formalin: Withdrawal Loss
- Isobutraldehyde: Standing Loss
- Isobutraldehyde: Withdrawal Loss
0
0
0
0
0
0
0
0
0
0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
MAJOR GROUPS 28,
0
0
0
.0
.0
.0
0.0
0
0
.0
.0
0,
0
0
0.
0.
0.
0.
0.
0.
0.
29,
0.
0.
0.
0.
0.
0.
.0
.0
.0
,0
0
0
0
0
0
0
30, 51
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
*0.36 0.
•0.026 0.
0.
0.
•NEC 0.
•NEC 0.
*0.15 0.
•0.006 0.
0.
0.
*1.5 0.
•0.002 0.
•0.0004 0.
•0.002 0.
*2.2 0.
•0.002 0.
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
103 Gallons
Capacity
10, Gallons
10 Gallons
Capacity
10 Gallons
103 Gallons
Capacity
10* Gallons
10 Gallons
Capacity
10 Gallons
10 Gallons
Capacity
10 Gallons
3
10 Gallons
Capacity
10 Gallons
10 Gallons
Capacity
10* Gallons
10 Gallons
Capacity
10 Gallons
Storage
Throughput
Storage
Throughput
Storage
Throughput
Storage
Throughput
Storage
Throughput
Storage
Throughput
Storage
Throughput
Storage
Throughput
73
73
232
232
73
73
73
73
73, 256
73, 256
73
73
*
Refer to numbered notes in Appendix A or lettered notes in Appendix B; factors without asterisks are from AP-42.
-------
sec
Process
PART
Lbs/Unit
so
Lbs/ftnlt
NO
Lbs/Unit
voc
Lbs/Unit
CO
Lbs/Unit Units
Aldehydes (Cont Inued )
4-07-172-11
4-07-172-12
4-07-172-97
4-07-172-98
- Propionaldehyde: Standing Loss
- Propionaldehyde: Withdrawal Loss
- Specify Aldehyde: Standing Loss
- Specify Aldehyde: Withdrawal Loss
0.0
0.0
0.0
0.0
0.0
0.0
0.0
0.0
0.0
0.0
0.0
0.0
*3
*0
*0
.3
.002
.002
0.
0.
0.
0.
0
0
0
0
Alkanei (Paraffins )
4-07-176-01
4-07-176-02
4-07-176-03
4-07-176-04
4-07-176-97
4-07-176-98
Ethers
4-07-208-01
4-07-208-02
4-07-208-03
4-07-208-04
4-07-208-97
4-07-208-98
Halogenated
4-07-220-01
4-07-220-02
4-07-220-03
4-07-220-04
4-07-220-05
4-07-220-06
4-07-220-07
- Cyclohexane: Standing Loss
- Cyclohexane: Withdrawal Loss
- N-Hexane: Standing Loss
- N-Hexane: Withdrawal Loss
- Specify Alkana: Standing Loss
- Specify Alkane: Withdrawal Loss
- Ethyl Ether: Standing Loss
- Ethyl Ether: Withdrawal Loss
- Propylene Oxide: Standing Loss
- Propylene Oxide: Withdrawal Loss
- Specify Ether: Standing Loss
- Specify Ether: Withdrawal Loss
Organlcs
- Carbon Tetrachloride: Standing
Loss
- Carbon Tetrachloride: Withdrawal
Loss
- Chloroform: Standing Loss
- Chloroform: Withdrawal Loss
- Ethylene Dichloride: Standing
Loss
- Ethylene Dichloride: Withdrawal
Loss
- Methylene Chloride: Standing Loss
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
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
0.0
0.0
0.0
0.0
0.0
0.0
0.0
0.0
0.0
*1
*0
*2
*0
*0
*7
*0
*5
*0
*0
*2
*0
*4
*0
*1
*0,
*0,
.35
.002
.2
.002
.002
.2
.002
.5
.002
.002
.9
.004
.0
.004
.3
.003
.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
10 Gallons
Capacity
10 Gallons
10 Gallons
Capacity
10 Gallons
3
10 Gallons
Capacity
10 Gallons
10 Gallons
Capacity
10* Gallons
10 Gallons
Capacity
10 Gallons
3
10 Gallons
Capacity
10* Gallons
10 Gallons
Capacity
10 Gallons
10 Gallons
Capacity
10 Gallons
3
10 Gallons
Capacity
10 Gallons
3
10 Gallons
Capacity
10 Gallons
10 Gallons
10 Gallons
3
10 Gallons
Capacity
Storage
Throughput
Storage
Throughput
Storage
Throughput
Storage
Throughput
Storage
Throughput
Storage
Throughput
Storage
Throughput
Storage
Throughput
Storage
Throughput
Storage
Throughput
Storage
Throughput
Storage
Notes
73
73
233
73
73
73
73
233
73
73
73
73
233
73
73
73
73
73
73
73
*Refer to numbered notes in Appendix A or lettered notes In Appendix B; factors without asterisks are from AP-42.
-------
sec
Halogenated
4-07-220-08
4-07-220-09
4-07-220-10
4-07-220-97
4-07-220-98
Ketones
4-07-228-01
4-07-228-02
4-07-228-03
4-07-228-04
4-07-228-05
4-07-228-06
4-07-228-97
4-07-228-98
Mercaptans
4-07-232-01
4-07-232-02
4-07-232-97
4-07-232-98
Process
Oraanics (Continued)
- Methylene Chloride: Withdrawal
Loss
- 1,1,1-Trlchloroethylene: Standing
Loss
- 1,1,1-Trichloroethylene:
Withdrawal Los*
- Specify in Comment*: Standing
Loss
- Specify in Comments: Withdrawal
Loss
- Acetone: Standing Loss
- Acetone: Withdrawal Loss
- Methyl Ethyl Ketone: Standing
Loss
- Methyl Ethyl Ketone: Withdrawal
Loss
- MIBK: Standing Loss
- MIBK: Withdrawal Loss
- Specify Ketone: Standing Loss
- Specify Ketone: Withdrawal Loss
(Thiols)
- Ethyl Mercaptan: Standing Loss
- Ethyl Mercaptan: Withdrawal Loss
- Specify Mercaptan: Standing Loss
- Specify Mercaptan: Withdrawal
Loss
PART
Lbs/Unit
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
so
Lbs/unit
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
NO
Lbs/unit
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
voc
Lbs/Unit
*0.
*1.
*0.
*0.
*2.
*0.
*1.
*0.
*0.
*0.
*0.
*5.
*0.
*0.
0
5
004
004
2
002
1
002
29
002
002
8
002
002
CO
Lbs/Unlt
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
Units
3
10 Gallons
3
10 Gallons
Capacity
10 Gallons
3
10 Gallons
Capacity
10 Gallons
3
10 Gallons
Capacity
10 Gallons
10 Gallons
Capacity
10 Gallons
3
10 Gallons
Capacity
10 Gallons
10 Gallons
Capacity
10 Gallons
3
10 Gallons
Capacity
10 Gallons
10 Gallons
Capacity
10 Gallons
Throughput
Storage
Throughput
Storage
Throughput
Storage
Throughput
Storage
Throughput
Storage
Throughput
Storage
Throughput
Storage
Throughput
Storage
Throughput
Notes
73
73
73
233
73
73
73
73
73
73
233
73
73
233
ORGANIC CHEMICAL STORAGE - PRESSURE TANKS
Aldehydes
4-07-812-01
4-07-812-02
- Acetaldehyde : Withdrawal Loss
- Acroleln: Withdrawal Loss
Alkanes (Paraffins)
4-07-816-01 - Ethane: Withdrawal Loss
4-07-816-02 - Butane: Withdrawal Loss
0.0
0.0
0.0
0.0
0.
0.
0.
0.
0
0
0
0
0.0
0.0
0.0
0.0
*16.
*6.
*0.
*0.
1
0
0
0
0.0
0.0
0.0
0.0
3
10 Gallons
10 Gallons
10, Gallons
10 Gallons
Throughput
Throughput
Throughput
Throughput
292
292
292
292
*Refer to numbered notes in Appendix A or lettered notes in Appendix B; factors without asterisks are from AP-42.
-------
sec
Process
PART
Lbs/Unit
so
Lbs/Unit
NO
Lbs/Unit
voc
Lbs/Unit
CO
Lbs/Unit
Alkanes (Paraffins) (Continued)
4-07-816-03
4-07-816-04
4-07-816-05
4-07-816-99
- Methane: Withdrawal Loss
- Natural Gas: Withdrawal Loss
- Propane: Withdrawal Loss
- Specify Alkane: Withdrawal Loss
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
Alkenes (Olefinsl
4-07-820-01
4-07-820-02
4-07-820-03
4-07-820-04
4-07-820-05
4-07-820-06
4-07-820-07
4-07-820-08
4-07-820-09
4-07-820-10
4-07-820-11
4-07-820-99
- 1,3-Butadiene: Withdrawal Loss
- 1-Butene: Withdrawal Los*
- 2-Butene: Withdrawal Los*
- Ethylene: Withdrawal Loss
- Isobutylene: Withdrawal Loss
- Propylene: Withdrawal Loss
- Isoprene: Withdrawal Loss
- Methylallene: Withdrawal Loss
- 1-Pentane: Withdrawal Loss
- Plperylene: Withdrawal Loss
- Cyclopentene : Withdrawal Loss
- Specify Alkene: Withdrawal Loss
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
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
12.8
27.9
18.1
9.3
10.4
0.0
0.0
0.0
0.0
0.0
0.0
0.0
0.0
0.0
0.0
0.0
0.0
Alkynes (Acetylenes)
4-07-824-01
4-07-824-99
Amines
4-07-832-01
4-07-832-02
4-07-832-03
4-07-832-99
Ethers
4-07-848-01
4-07-848-99
Halogenated
4-07-860-01
4-07-860-02
4-07-860-03
4-07-860-04
4-07-860-99
Isocyanates
4-07-864-01
- Acetylene: Withdrawal Loss
- Specify Alkyne: Withdrawal Loss
- Methylamine : Withdrawal Loss
- Dljnethylamine: Withdrawal Loss
- TrUnethylamlne: Withdrawal Loss
- Specify Amine: Withdrawal Loss
- Ethylene Oxide: Withdrawal Loss
- Specify Ether: Withdrawal Loss
Organlcs
- Ethyl Chloride: Withdrawal Loss
- Methyl Chloride: Withdrawal Loss
- Phosgene: Withdrawal Loss
- Vinyl Chloride: Withdrawal Loss
- Specify in Comments: Withdrawal
Loss
- Methyl Isocyanate: Withdrawal
Loss
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
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
•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
103
10
10
10
3
103
103
103
103
103
103
103
103
103
10
103
10
3
103
10*
3
"3
103
10
3
103
10
3
103
10
103
10
10
3
Units
Gallons
Gallons
Gallons
Gallons
Gallons
Gallons
Gallons
Gallons
Gallons
Gallons
Gallons
Gallons
Gallons
Gallons
Gallons
Gallons
Gallons
Gallons
Gallons
Gallons
Gallons
Gallons
Gallons
Gallons
Gallons
Gallons
Gallons
Gallons
Gallons
Gallons
Throughput
Throughput
Throughput
Throughput
Throughput
Throughput
Throughput
Throughput
Throughput
Throughput
Throughput
Throughput
Throughput
Throughput
Throughput
Throughput
Throughput
Throughput
Throughput
Throughput
Throughput
Throughput
Throughput
Throughput
Throughput
Throughput
Throughput
Throughput
Throughput
Throughput
Notes
292
292
292
292
292
292
292
292
292
292
292
292
292
292
292
292
292
292
292
292
292
292
292
292
292
292
292
Refer to numbered notes in Appendix A or lettered notes in Appendix B; factors without asterisks are from AP-42.
-------
sec
Isocyanates
4-07-864-99
Mercaptans
4-07-872-01
4-07-872-99
Process
( Cont inued )
- Specify Isocyanate: Withdrawal
Loss
(Thlols)
- Methyl Mercaptan: Withdrawal Loss
- Specify Mercaptan: Withdrawal
PART SO
Lbs/Unit Lbs/unIt
0.0
0.0 0.0
0.0
NO VOC CO
Lbs/unit Lbs/Unit Lbs/Unit
0.0
0.0 *0.0 0.0
0.0
Units
10 Gallons Throughput
10, Gallons Throughput
10 Gallons Throughput
Notes
292
Loss
Miscellaneous
4-07-999-97 - Specify In Comments: Breathing
Loss
4-07-999-98 - Specify in Comments: Withdrawal
Loss
ORGANIC CHEMICAL TRANSPORTATION - MAJOR CROUPS 28. 29. 30. 51
10 Gallons Storage
Capacity
10 Gallons Transferred
CO
Specify Liquid
4-08-999-95 - Cars/Trucks: Loading Rack
4-08-999-97 - Marine Vessel »: Loading Rack
4-08-999-99 - Loading Rack
ORGANIC SOLVENT EVAPORATION - MISCELLANEOUS
0.0
0.0
0.0
0.0
10 Gallons Transferred
10 Gallons Transferred
10 Gallons Transferred
Solvent Extraction Processes
4-90-001-01 -
4-90-001-02 -
4-90-001-03 -
4-90-001-04 -
4-90-001-05 -
4-90-001-99 -
Waste Solvent
4-90-002-01 -
4-90-002-02 -
4-90-002-03 -
4-90-002-04 -
4-90-002-05 -
4-90-002-06 -
4-90-002-99 -
Petroleum Naphtha (Stoddard)
MEK
MIBK
Furfural
Trichloroethylene
Other Not Classified (Specify
in Comments)
Recovery Operations
Storage Tank Vent
Condenser Vent
Incinerator Stack
Solvent Spillage
Solvent Loading
Fugitive Leaks!
Other Not Classified (Specify
in Comments)
0
0
0
0
0
0
0
0
1
0
0
0
0
.0
.0
.0
.0
.0
.0
.0
.0
.44
.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
0.0
0.0
•2000.0
•2000.0'*
*2000 . 0
•2000.0*
•2000.0
•2000.0
0.02
3.3
0.02
0.2
0.72
0
0
0
0
0
0
0
0
0
0
0
0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
Tons
Tons
Tons
Tons
Tons
Tons
Tons
Tons
Tons
Tons
Tons
Solvent Consumed
Solvent Consumed
Solvent Consumed
Solvent Consumed
Solvent Consumed
Solvent Consumed
Reclaimed Solvent
Reclaimed Solvent
Reclaimed Solvent
Reclaimed Solvent
Reclaimed Solvent
Process Unit-Year
Tons
Reclaimed Solvent
Note that fugitive emissions are reported in units of Ibs/process unit-year rather than Ibs/ton product as in the NEDS Source Classification Codes
and Emission Factor Listing dated October 1985.
*Refer to numbered notes in Appendix A or lettered notes in Appendix B; factors without asterisks are from AP-42.
-------
PART
SCC Process Lbs/Unit
Rail Car Cleaninit - 4742. 4011. 4013
4-90-003-01 - Low Vapor Pressure, High Viscosity 0.0
Group (Ethylene Clycol)
4-90-003-02 - Medium Vapor Pressure, Medium 0.0
Viscosity Cargo (Chlorobencene)
4-90-003-03 - Low Vapor Pressure, Medium 0.0
Viscosity Cargo
(o-Dichlorobensene)
4-90-003-04 - Low Vapor Pressure, High Viscosity 0.0
Cargo (Creosote)
4-90-003-99 - Other Not Classified (Specify 0.0
in Contents)
Tank Trucks Cleaninx
4-90-004-01 - High Vapor Pressure, Low Viscosity 0.0
Cargo (Acetone)
4-90-004-02 - High Vapor Pressure, Low Viscosity 0.0
Cargo (Perchloroethylene)
4-90-004-03 - Medium Vapor Pressure, Medium 0.0
Viscosity Cargo (Methyl
Methacrylate)
4-90-004-04 - Low Vapor Pressure, Low Viscosity 0.0
Cargo (Phenol)
4-90-004-05 - Low Vapor Pressure, High Viscosity 0.0
Cargo (Propylene Glycol)
4-90-004-99 - Other Not Classified (Specify 0.0
in Comments)
Organic Solvent Evaporation — Fuel Fired Eaulpment
Incinerators
4-90-900-11 - Distillate Oil (No. 2)
4-90-900-12 - Residual
4-90-900-13 - Natural Gas
Flares
4-90-900-23 - Natural Gas
Miscellaneous Volatile Organic Compound Evaporation
Solvent in Comments
4-90-999-99 - Identify the Process and the 0.0
SO NO VOC
Lbs/Unit Lbs/Unit Lbs/Unit
0.0 0.0 0.0007
0.0 0.0 0.035
0.0 0.0 0.166
0.0 0.0 5.2
0.0 0.0
0.0 0.0 0.69
0.0 0.0 0.47
0.0 0.0 0.07
0.0 0.0 0.012
0.0 0.0 0.002
0.0 0.0
*0.4
•0.56
*5.6
*5.6
0.0 0.0
0.0 0.0 *2000.0d
CO
Lbs/Unit Units
0.0 Tank Cars Cleaned
0.0 Tank Cars Cleaned
0.0 Tank Cars Cleaned
0.0 Tank Cars Cleaned
0.0 Tank Cars Cleaned
0.0 Tank Trucks Cleaned
0.0 Tank Trucks Cleaned
0.0 Tank Trucks Cleaned
0.0 Tank Trucks Cleaned
0.0 Tank Trucks Cleaned
0.0 Tank Trucks Cleaned
10 Gallons Burned
Q
10, Gallons Burned
6
10 Cubic Feet Burned
10 Cubic Feet Burned
n n r?0ii*.n« c~l»«n* rArt*fun«/4
0.0 Tons Solvent Consumed
Notes
130
130
130
130
Refer to numbered notes in Appendix A or lettered notes in Appendix B; factors without asterisks are from AP-42.
-------
SCC Process
SOLID WASTE DISPOSAL - GOVERNMENT
Municipal Incineration - 4953
5-01-001-01 - Multiple Chamber
5-01-001-02 - Single Chamber
Open Burning Dump
5-01-002-01 - General Refuse
5-01-002-02 - Vegetation Only
Other Incineration
5-01-005-05 - Pathological
5-01-005-06 - Sludge
5-01-005-07 - Conical Design (Tee Pee)
Municipal Refuse
5-01-005-08 - Conical Design (Tee Pee) Wood
Refuse
5-01-005-10 - Trench Burner: Wood
5-01-005-11 - Trench Burner: Tires
5-01-005-12 - Trench Burner: Refuse
Fire fight Ing
5-01-006-01 - Structure: Jet Fuel
5-01-006-02 - Structure: Distillate Oil
5-01-006-03 - Structure: Kerosene
5-01-006-0* - Structure: Wood Pallets
Sewage Treatment
5-01-007-01 - Entire Plant
5-01-007-02 - Primary Settling Tank
5-01*007-03 - Secondary Settling Tank
5-01-007-04 - Aeration Tank
Auxiliary Fuel /No Emissions
5-01-900-05 - Distillate Oil
5-01-900-06 - Natural Gas
5-01-900-10 - Liquid Petroleum Gas (LPG)
SOLID WASTE DISPOSAL - COMMERCIAL /INSTITUTIONAL
Incineration - General
5-02-001-01 - Multiple Chamber
5-02-001-02 - Single Chamber
5-02-001-03 - Controlled Air
PART
Lbs/Unlt
30.0
15.0
16.0
17.0
8.0
100.0
20.0
7.0
13.0
138.0
37.0
0.0
0.0
0.0
7.0
15.0
1.4
SO
Lbs/8nit
2.5
2.5
1.0
*o.oc
0.0
1.0
2.0
0.1
0.1
2.5
0.0
0.0
0.0
2.5
2.5
1.5
NO
Lbs/flnit
3.0
2.0
6.0
*4.0°
3.0
5.0
5.0
1.0
4.0
0.0
0.0
0.0
3.0
2.0
10.0
VOC
Lbs/Unlt
1.5
15.0
30.0
19.0
•10.0
1.0
20.0
11.0
•19.0
*6.0
*13.3
*0.4
*0.4
*0.4
*19.0
*3
•1.5
*1.5
*NEG
0.0
0.0
0.0
3.0
15.0
NEC
CO
Lbs/Unlt
35.0
20.0
85.0
140.0
0.0
0.0
60.0
130.0
0.0
0.0
0.0
10.0
20.0
0.0
Units
Tons Burned
Tons Burned
Tons Burned
Tons Burned
Tons Burned
Tons Dry Sludge
Tons Burned
Tons Burned
Tons Burned
Tons Burned
Tons Burned
3
10 Gallons Burned
10 Gallons Burned
10 Gallons Burned
Tons Burned
6
10, Gallons Wastewater
10 Gallons Wastewater
10, Gallons Wastewater
10 Gallons Wastewater
3
10 Gallons Burned
10 Cubic Feet Burned
10 Gallons Burned
Tons Burned
Tons Burned
Tons Burned
Notes
244
312
164
164
312
312
312
312
258
258
258
258
*Refer to numbered notes In Appendix A or lettered notes In Appendix Bj factors without asterisks are from AP-42.
-------
cn
SCC Process
Incineration - General (Continued)
5-02-001-0* - Conical Design: Municipal Refuse
5-02-001-05 - Conical Design: Hood Refuse
Open Burning
5-02-002-01 - Wood
5-02-002-02 - Refuse
Apartment Incineration
5-02-003-01 - Flu* Fed
5-02-003-02 - Flue Fed (With Afterburner and
Draft Control*)
Incineration (Special Purpose)
5-02-005-05 - Pathological Hast*
5-02-005-06 - Sludge
PART
Lbs/Unlt
20.0
7.0
17.0
16.0
30.0
6.0
8.0
100.0
SO
Lbs/unit
2.0
0.1
*o.oc
1.0
0.5
0.5
8.0
1.0
NO
Lbs/finlt
5.0
1.0
-4.0°
6.0
3.0
10.0
3.0
5.0
VOC
Lbs/Unlt
20.0
11.0
19.0
30.0
15.0
3.0
*3.0
1.0
CO
Lbs/Unlt
60.0
130.0
140.0
85.0
20.0
10.0
0.0
0.0
Units Notes
Tons Burned
Tons Burned
Tons Burned
Tons Burned
Tons Burned
Tons Burned
Tons Burned 140
Tons Dry Sludge
Landfill Dui
5-02-006-01 - Waste Gas Flare
5*02-006-02 - Municipal: Fugitive Emissions
Asbestos Removal
*5.6
10 Cubic Feet Burned
Acres of Landfill
314
5*02-009-01 - General
Auxiliary Fuel/No Emissions
5-02-900-05 - Distillate Oil
5-02-900-06 - Natural Gas
5-02-900-10 - Liquified Petroleum Gas (LPG)
SOLID WASTE DISPOSAL - INDUSTRIAL
Incineration
5-03-001-01 -
5-03-001-02 -
5-03-001-03 -
5-03-001-04 -
5-03-001-05 -
5-03-001-06 -
5-03-001-07 -
5-03-001-08 -
3-OJ-UU1-U* -
Open Burning
5-03-002-01 -
5-03-002-02 -
Multiple Chamber
Single Chamber
Controlled Air
Conical Design: Refuse
Conical Design: Wood Refuse
Trench Burner: Wood
Trench Burner: Tires
Auto Body Components
Trench Burner: Refuse
Wood/Vegetation/Leaves
Refuse
0
0
0
7
15
1
20
7,
13.
138.
2.
37 .
17.
16.
.0
.0
.0
.0
.0
.4
.0
.0
.0
.0
.0
, 0
0
0
0
0
0
2
2
1
2
0
0
0
2
*0
1
.0
.0
.0
.5
.5
.5
.0
.1
.1
.0
. 5
.oc
.0
0.0
0.0
0.0
3.0
2.0
10.0
5.0
1.0
4.0
0.1
-4.0°
6.0
*0.0
0.0
0.0
0.0
3.0
15.0
NEC
20.0
11.0
0.0
-6.0
0.91
* J " "*
19.0
30.0
0
0
0
10
20
0
60
130
0
2.
140.
85.
.0
.0
.0
.0
.0
.0
.0
.0
.0
.5
.0
0
Tons Waste Removed 285
10 Gallons Burned
10 Cubic Feet Burned
10 Gallons Burned
Tons
Tons
Tons
Tons
Tons
Tons
Tons
Tons
Tnn*
Tons
Tons
Burned
Burned
Burned
Burned
Burned
Burned
Burned 164
Burned
Bti*-n««l 1 At
Burned
Burned
Refer to numbered notes In Appendix A or lettered notes in Appendix B; factors without asterisks are from AP-42.
-------
SCC Process
Open Burning (Continued)
5-03-002-03 - Auto Body Component*
5-03-002-04 - Coal Refuse Piles
Incineration
5-03-005-01 - Hazardous Waste
5-03-005-06 - Sludge
Landfill Dump
5-03-006-01 - Waste Gas Flare
5-03-006-02 - Liquid Waste Disposal
5-03-006-03 - Hazardous: Fugitive Emissions
Liquid Waste
5-03-007-01 - General
Asbestos Removal
5-03-009-01 - General
Auxiliary Fuel/Ho Emissions
5-03-900-05 - Distillate Oil
5-03-900-06 - Natural Gas
5-03-900-10 - Liquified Petroleum Gas (LPG)
PART SO NO
Lbs/Unlt Lbs/finlt Lbs/5nit
100.0 NEC 4.0
*0.9 *1.1 *0.1
*0.3 *0.13 *0.14
100.0 1.0 5.0
0.0 0.0 0.0
0.0 0.0 0.0
0.0 0.0 0.0
VOC
Lbs/Unit
32.0
*0.5
*0.3
1.0
*5.6
*4
*0.0
0.0
0.0
0.0
CO
Lbs/Unit Units
125.0 Tons Burned
*2.5 Cubic Yards of Pile
*0.5 10 BTU/Year Heat Input
0.0 Tons Dry Sludge
10 Cubic Feet Burned
Tons Liquid Waste Burned
Acres of Landfill
3
10 Gallons Waste Burned
Tons Waste Removed
0.0 10 Gallons Burned
0.0 10 Cubic Feet Burned
0.0 10 Gallons Burned
Notes
374
314
136
285
Refer to numbered notes in Appendix A or lettered notes in Appendix B; factors without asterisks are from AP-42.
-------
-------
APPENDIX A
FOOTNOTES FOR EMISSION FACTORS GENERATED
DURING PHASE I AND PHASE II UPDATE
1. Estimates of VOC emissions taken from emission factors listed in
Fugitive Emission Sources of Organic Compounds - Additional Information
on Emissions, Emission Reductions, and Costs. U. S. Environmental
Protection Agency. Research Triangle Park, North Carolina.
EPA-450/3-82-010 (NTIS PB82-217126), April 1982. p. 2-70.
2. Equipment counts taken from Problem-Oriented Report: Frequency
Occurrence for Fittings in Synthetic Organic Chemical Plant Process
Units. (Prepared for U. S. Environmental Protection Agency.) Research
Triangle Park, North Carolina. EPA-600/2-81-003 (NTIS PB81-141566),
September 1980. Emission estimate for equipment leaks of VOC (fugitive
emissions) are presented in this NAPAP listing as Ibs/yr. To have an
emissions estimate generated automatically (as in the NEDS inventory
computer program), a production rate of unity should be used for the
SCC's involving fugitive emissions from organic chemical process units.
This procedure and alternate estimate techniques are presented in
Appendix D of this document.
3. Based on one VOC emission factor value from State files (State A).
4. VOC emission factor estimated from Background Information for Proposed
New Source Performance Standards: Steam Generators, Incinerators,
Portland Cement Plants, Nitric Acid Plants, Sulfuric Acid Plants.
EPA Report APTD-0711 (NTIS PB 202459), U. S. Environmental Protection
Agency. 1971. p. 37-42.
5. VOC emissions were extracted from Table 5 in Source Assessment:
Plastics Processing, State of the Art. U. S. Environmental Protection
Agency. EPA-600/2-78-004c (NTIS PB 280926), March 1978. An emission
factor of negligible has been reported for processes where no
consumption of plastic is expected. A VOC factor for polyether resins
was estimated based on an average of the other resin products
described.
6. VOC emission factor based on the average of three emissions tests
submitted by the State of Tennessee as a response to the 1986
STAPPA/ALAPCO survey.
7. This VOC emission factor was estimated from the mean of two emission
factor values from State files (State A).
8. VOC emission factors estimated from "Sodium Carbonate Industry -
Background Information for Proposed Standards. Draft EIS."
EPA-450/3-80-029a (NTIS PB80-219678), August 1980.
149
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9. VOC emission factors estimated from information in "A Review of
Standards of Performance for New Stationary Sources - Sulfuric Acid
Plants." EPA-450/3-79-003 (NTIS PB 292278), January 1979.
p. 3-1 - 3-5.
10. This VOC emission factor was calculated from Tables in Polymer
Manufacturing Industry - Background Information for Proposed Standards.
Preliminary Draft. March 1983. p. 3.18. The emission rates for each
process section were summed and this value was converted to the proper
SCC units.
11. Ammonium Nitrate Manufacturing Industry - Technical Document.
EPA-450/3-81-002 (NTIS PB81-152928), January 1981. Chapter 3. No VOC
emissions are expected from ammonium nitrate manufacturing processes.
12. NOV emission factor based on five values from State data (States A and
E)?
13. VOC emission factor estimate based on information from Docket
No. A-83-29, (SOCMI Reactor Processes NSPS), Section II-D.
14. VOC emission factor from Control of Volatile Organic Compound Emissions
from Air Oxidation Processes in Synthetic Organic Chemical
Manufacturing Industry. EPA-450/3-84-015 (NTIS PB85-164275), December
1984. This VOC emission factor was calculated from Table C-l. The
midpoint of the range was calculated and converted to the proper SCC
units.
15. VOC emission factor from Urea Manufacturing Industry - Technical
Document. EPA-450/3-81-001 (NTIS PB81-158925), January 1981. From
Table 3-1.
16. VOC emission factor estimate based on information from Docket
No. A-81-22, (SOCMI Air Oxidation Processes NSPS), Section II-D,
17. VOC emission factor from Organic Chemical Manufacturing, Volume 9:
Selected Processes. EPA-450/3-80-028d (NTIS PB81-220584),
December 1980. Report 6. Table IV-1.
18. VOC emission factor from Organic Chemical Manufacturing, Volume 10:
Selected Processes. EPA-450/3-80-028e (NTIS PB81-220592),
December 1980. Report 3. Table IV-2.
19. VOC emission factor from Organic Chemical Manufacturing, Volume 10:
Selected Processes. EPA-450/3-80-028e (NTIS PB81-220592),
December 1980. Report 6. Table IV-1.
20. VOC emission factor estimate calculated from Tables in Section ?. of
Survey of Perchloroethylene Emission Sources. EPA-450/3-85-017
(NTIS PB85-233518/REB), June 1985. Emission factors were estimated by
taking the average of VOC emissions factor values from eight plants.
150
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21. VOC emission factor estimate calculated from Tables in Section 2 of
Survey of Trichloroethylene Emission Sources. EPA-450/3-85-021
(NTIS PB86-107943), July 1985. Emission factors were estimated by
taking the average of VOC emission factor values from two plants.
22. VOC emission factor values were extracted from Tables in Survey Reports
on Atmospheric Emissions from Petrochemical Industry - Volume 4. Vinyl
Chloride Chapter. EPA-450/3-73-005d (NTIS PB 245630), April 1974.
Emissions data were collected through Industry Questionnaires in the
early 1970's by the Houdry Division, Air Products and Chemicals, Inc.
These emission factors should only be used in the absence of more
recent source specific emissions data.
23. VOC emission factor from Organic Chemical Manufacturing, Volume 10:
Selected Processes. EPA-450/3-80-028e (NTIS PB81-220592),
December 1980. Report 4. Back calculated from Table V-l to estimate
uncontrolled emissions.
24. SO , NO , and VOC emission factor values were extracted from Tables in
Survey Reports on Atmospheric Emissions from the Petrochemical
Industry - Volume 1. Acetic Anhydride Chapter. EPA-450/3-73-005a
(NTIS PB 244957), April 1974. Emissions data were collected through
Industry Questionnaires in the early 1970's by the Houdry Division, Air
Products and Chemicals, Inc. These emission factors should only be
used in the absence of more recent source specific emissions data.
25. VOC emission factors from Table 2 in Locating and Estimating Air
Emissions from Sources of Vinylidene Chloride. EPA-450/4-84-007K
(NTIS PB86-117611/REB), September 1985.
26. VOC emission factor from Organic Chemical Manufacturing, Volume 10:
Selected Processes. EPA-450/3-80-028e (NTIS PB81-220592),
December 1980. Reports 7 and 8. Tables IV-1 and IV-2.
27. VOC emission factor from Organic Chemical Manufacturing, Volume 7:
Selected Processes. EPA-450/3-80-028b (NTIS PB81-220568),
December 1980. Reports 2 and 3. Tables IV-1 and IV-3.
28. VOC emission factor averaged from data presented in National Council on
Air and Stream Improvement for the Pulp and Paper Industry (NCASI).
Technical Bulletin 504. September 1986. They apply to dryers in the
wood panelboard industry and emissions are reported as loss of carbon.
29. VOC emission factor values were extracted from Tables in Survey Reports
on Atmospheric Emissions from the Petrochemical Industry - Volume 2.
Cyclohexanone Chapter. EPA-450/3-73-005b (NTIS PB 244958), April 1974.
Emissions data were collected through Industry Questionnaires in the
early 1970's by the Houdry Division, Air Products and Chemicals, Inc.
These emission factors should only be used in the absence of more
recent source specific emissions data.
151
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30. VOC emission factor from Organic Chemical Manufacturing, Volume (>:
Selected Processes. EPA-450/3-80-028a (NTIS PB81-220550),
December 1980. Reports 1 and 2. Tables IV-1 to IV-3.
31. VOC emission factor from Organic Chemical Manufacturing, Volume <>:
Selected Processes. EPA-450/3-80-028d (NTIS PB81-220584),
December 1980. Reports 4 and 5.
32. Locating and Estimating Air Emissions from Sources of Ethylene Oxide.
Draft Final Report. Radian Corporation. October 1985. This VOC
emission factor was calculated from Tables 6 and 7. It is the mean of
two values, and assumes that control methods of inspection and
maintenance arejn place.
33. VOC emission factor from Organic Chemical Manufacturing, Volume 10:
Selected Processes. EPA-450/3-80-028e (NTIS PB81-220592),
December 1980. Report 3. Chapters III and IV.
34. VOC emission factor values were extracted from Tables in Survey Reports
on Atmospheric Emissions from the Petrochemical Industry - Volume 2.
Glycerin Chapter. EPA-450/3-73-005b (NTIS PB 244958), April 1974.
Emissions data were collected through Industry Questionnaires in the
early 1970's by the Houdry Division, Air Products and Chemicals, Inc.
These emission factors should only be used in the absence of more
recent source specific emissions data.
35. VOC emission factor from Organic Chemical Manufacturing, Volume 7:
Selected Processes. EPA-450/3-80-028b (NTIS PB81-220568),
December 1980. Report 4. Table IV-1. An emission factor of 9.2 was
provided for solvent recovery, flash, and product purification
distillation. No breakdown of the individual processes was provided.
Therefore, this emission factor was divided evenly among the three
SCC's listed.
36. VOC emission factor from Organic Chemical Manufacturing, Volume 10:
Selected Processes. EPA-450/3-80-028e (NTIS PB81-220592),
December 1980. Report 5. Table IV-2.
37. VOC emission factor from Organic Chemical Manufacturing, Volume 7:
Selected Processes. EPA-450/3-80-028b (NTIS PB81-220568),
December 1980. Report 1. Table IV-1.
38. VOC emission factor values were extracted from Tables in Survey Reports
on Atmospheric Emissions from the Petrochemical Industry - Volume 2.
Ethylene Chapter. EPA-450/3-73-005b (NTIS PB 244958), April 1974.
Emissions data were collected through Industry Questionnaires in the
early 1970's by the Houdry Division, Air Products and Chemicals, Inc.
These emission factors should only be used in the absence of more
recent source specific emissions data.
152
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39. VOC emission factor values were extracted from Tables in Survey Reports
on Atmospheric Emissions from the Petrochemical Industry - Volume 3.
Phenol Chapter. EPA-450/3-73-005c (NTIS PB 245629), April 1974.
Emissions data were collected through Industry Questionnaires in the
early 1970's by the Houdry Division, Air Products and Chemicals, Inc.
These emission factors should only be used in the absence of more
recent source specific emissions data.
40. VOC emission factor from Organic Chemical Manufacturing, Volume 10:
Selected Processes. EPA-450/3-80-028e (NTIS PB81-220592),
December 1980. Report 1. Tables IV-1 through IV-3.
41. Based on two VOC emission factor values from State files (State A) and
on two values taken from Docket No. A-83-29 (SOCMI Reactor Processes
NSPS) Section II-D. The mean of these four values was used as this
emission factor estimate.
42. VOC emission factor from Organic Chemical Manufacturing, Volume 6:
Selected Processes. EPA-450/3-80-028a (NTIS PB81-220550),
December 1980. Reports 5 and 6. Table IV-1. The oleum reactor was
not described and was estimated to have negligible emissions based on
engineering judgement.
43. VOC emission factor from Organic Chemical Manufacturing, Volume 7:
Selected Processes. EPA-450/3-80-028b (NTIS PB81-220568),
December 1980. Report 7. Tables IV-2 and IV-4.
44. VOC emission factor from Organic Chemical Manufacturing, Volume 9:
Selected Processes. EPA-450/3-80-028d (NTIS PB81-220584),
December 1980. Reports 2 and 3. The emission factor presented for
compressor lube oil vent is an average of 20 model plants listed in
Report 3.
45. VOC emission factor from Organic Chemical Manufacturing, Volume 9:
Selected Processes. EPA-450/3-80-028d (NTIS PB81-220584),
December 1980. Report 9. Tables IV-1 and IV-2.
46. VOC emission factor from Organic Chemical Manufacturing, Volume 10:
Selected Processes. EPA-450/3-80-028e (NTIS PB81-220592),
December 1980. Report 2. Table IV-1.
47. VOC emission factor values were extracted from Tables in Survey Reports
on Atmospheric Emissions from the Petrochemical Industry - Volume 1.
Adiponitrile Chapter. EPA-450/3-73-005a (NTIS PB 244957), April 1974.
Emissions data were collected through Industry Questionnaires in the
early 1970's by the Houdry Division, Air Products and Chemicals, Inc.
These emission factors should only be used in the absence of more
recent source specific emissions data.
153
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48. VOC emission factor from Organic Chemical Manufacturing, Volume 6:
Selected Processes. EPA-450/3-80-028a (NTIS PB81-220550),
December 1980. Report 3. Table IV-1. No NO or SO emissions are
expected based on review of the process description.
49. VOC emission factor from Organic Chemical Manufacturing, Volume 8:
Selected Processes. EPA-450/3-80-028c (NTIS PB81-220576),
December 1980. Reports 2 and 3. Table IV-1.
50. VOC emission factor estimated for high density polyethylene by summing
the emission factors for each specific process listed. VOC emission
factors for polyethylene processes - general (3-01-018-60 to
3-01-018-66) are estimates based on the average of emission factors
listed for high and low density polyethylene production.
51. VOC emission factor from Organic Chemical Manufacturing, Volume 10:
Selected Processes. EPA-450/3-80-028e (NTIS PB81-220592),
December 1980. Report 3. Tables IV-1 and IV-2. The sum of three
vents was used to estimate emissions from the distillation system
condenser. Values for allyl chloride production represent the
mid-point of a range of emissions provided in the document for each
process.
52. VOC emission factor estimates were transferred from similar processes
listed for acrylonitrile production.
53. This VOC emission factor is based on emission factor values from State
files (State A). Five values were in initial sample size. This
source category includes all general storage and transfer processes
within the chemical manufacturing group which are uncategorized
otherwise. Processes therefore may be unrelated and emissions may
not be comparable. Due to extreme variance, the high and low values
were deleted and the mean of the remaining three values was used.
54. VOC emission factor based on Source Test Report submitted to the U. S.
Environmental Protection Agency by Washington State Department of
Ecology as a response to the 1986 STAPPA/ALAPCO survey.
55. VOC emission factors for vegetable oil production have been calculated
in units of Ibs/ton of extractor feed cake processed rather than
Ibs/ton of refined oil produced. Emission data were taken from
"Control of Volatile Organic Emission from Manufacture of Vegetable
Oils." EPA-450/2-78-035 (NTIS PB 286307), June 1978.
56. See note 55. These VOC emission factors were calculated from Table 2-2
and Figure 2-1 of "Control of Volatile Organic Emissions from
Manufacture of Vegetable Oils." EPA-450/2-78-035 (NTIS PB 286307). The
factors for the four different seed types were averaged and this number
was divided among the different processes as outlined in Figure 2-1.
154
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57. VOC emission factor from Organic Emissions from Ferrous Metallurgical
Industries: Compilation of Emission Factors and Control Technologies.
EPA-600/2-84-003 (NTIS PB84-141548), January 1984. Emission factors
are expressed as total organic emissions which may overestimate VOC
emissions. Tables 4-4 and 5-5.
58. Personal communication with Al Vervaert of EPA/OAQPS/ESED. January
1986. Metals-oriented hot processes are considered to have negligible
VOC emissions.
59. VOC emission factor from Organic Emissions from Ferrous Metallurgical
Industries: Compilation of Emission Factors and Control Technologies.
EPA-600/2-84-003 (NTIS PB84-141548), January 1984. Emission factors
are expressed as total organic emissions which may overestimate VOC
emissions. Table 6-3.
60. VOC emission factor for dryers was transferred from factors listed for
dryers in other mineral product industries. This factor is based on a
direct-fired dryer burning natural gas.
61. VOC emissions are estimated to be negligible. Small amounts of VOC may
contribute to odor problems, particularly in wet manure. Compounds
which give rise to the odor are organic acids, methylmercaptans,
ammonia, and amines; however, total VOC's have not been quantified.
(Personal communication with University of Georgia and Texas A&M
University, Agricultural Extension Offices. April 21, 1987.)
62. Based on the mean of seven VOC emission factor values provided for
crude oil sumps from State files (State A). This emission factor
estimate was transferred to crude oil pits as a best estimate for VOC.
63. Based on the mean of three VOC emission factor values from State files
(State A).
64. VOC emission factor from Locating and Estimating Air Emissions from
Sources of Ethylene Oxide. Draft Final Report. Radian Corporation.
October 1985. p. 53-55.
65. Based on the mean of five VOC emission factor values from State files
(State A). This source category includes a variety of adhesive coating
application processes which may not be comparable. The values listed
in the State files are highly variable and this emission factor
estimate has been rounded to the nearest hundred. It is an
approximation which should be used only in the absence of specific
emissions data.
66. Based on the mean of 12 VOC emission factor values from State files
(State A). This source category includes a variety of adhesive coating
application processes which may not be comparable. The values listed
in the State files are highly variable and this emission factor
estimate has been rounded to the nearest whole number. It is an
approximation which should be used only in the absence of specific
emissions data.
155
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67. Based on the average of 296 VOC emission factor values from State files
(States A, D, and E) rounded to the nearest hundred. This source
category includes all general coating oven operations. Processes may
vary widely between different plants. Data are highly variable and
this emission factor is an approximation which should be used only in
the absence of specific emissions data.
68. Based on the mean of 25 VOC emission factor values from State files
(States A and D). Emissions from State D are reported as total
hydrocarbons and may overestimate VOC's.
69. Based on 14 VOC emission factor values from State files (State A).
This source category includes fugitive emissions from various surface
coating operations where processes may not be comparable. Due to
extreme variability, the high and low values were dropped and the mean
of the remaining 12 values was used as an emission factor estimate.
70. VOC emissions from inorganic chemical manufacturing and storage is
expected to be zero using engineering judgement.
71. VOC emission factor based on nine VOC emission factor values from State
files (State A). This source category includes storage of various
petroleum liquids. The emission factor is an approximation which
should be used only in the absence of specific emissions data.
72. Personal communication with Mr. William Thomas (Florida Department of
Natural Resources, Southwest District office). Mr. Thomas is not aware
of any VOC testing ever having been done in the phosphate industry, but
feels there are small amounts of VOC's emitted from the phosphate rock
processing. Mr. Thomas also felt that there are no SO emissions from
phosphoric acid manufacturing processes.
73. VOC emission factors were calculated using equations from Section 4.3
of AP-42 dated September 1985. The same assumptions were used as those
from Table 4.3-4 on page 4.3-15 of tbe AP-42 Third Edition, dated
April 1977. Values smaller than 10 were considered negligible and
entered into the Table as 0.0.
74. SO emission factor was estimated using technology transfer from
oil-fired process heaters in other industries, assuming that the dryers
burn oil. Emissions are from the combustion source only.
75. VOC emission factors estimated through technology transfer from similar
fiber production, based on information in: Industrial Process Profiles
for Environmental Use: Chapter 11. The Synthetic Fiber Industry.
EPA-600/2-77-023k, February 1977. The factor for aramids was
transferred from polyamides. The factor for polyesters was transferred
from acrylics based on similarities in the physical properties of the
fibers.
156
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76. VOC emissions are estimated to be negligible from the process
description. Personal communication with the American Foundrymen's
Society. April 27, 1987. There may be some VOC's from the solid
process, but the shell process predominates. Combustion temperatures
are very high (greater than 1000 F) and complete combustion is
expected.
77. Emission factor is an average based on less than five VOC values
obtained from responses to Section 114 letters for the methylene
chloride NESHAP.
78. Emission factor based on a single VOC value obtained from a response to
a Section 114 letter for the methylene chloride NESHAP.
79. Emission factors transferred from kraft mill processes. Personal
communication with Mr. Bill Fuller, Oregon Department of Environmental
Quality. April 17, 1987.
80. Personal communication with Mr. Lee Gribovich, Wyoming Division of Air
Quality. January 1987. No test data are available on VOC's from
fuel-fired equipment in the sodium carbonate industry. Only the
calciners and the rotary dryer (if direct-fired) are expected to have
any SO , NO , or VOC's. Mr. Gribovich provided SO and NO data for
the coal-fifed calciner (two of six plants).
81. VOC emission factor transferred from other sintering processes which
are similar based on the descriptions given in AP-42 (8.8.1).
Clay/coke may produce higher VOC's due to the presence of the coke.
82. SO and NO emission factor values were extracted from Tables in Survey
Reports on Atmospheric Emissions from the Petrochemical Industry -
Volume 1. EPA-450/3-73-005a (NTIS PB 244957), April 1974. Emissions
data were collected through Industry Questionnaires in the early 1970s
by the Houdry Division, Air Products and Chemicals, Inc. These
emission factors should only be used in the absence more recent source
specific emissions data.
83. Emission factor based on a single VOC value on information from Docket
No. A-80-25, (SOCMI Distillation Operations NSPS) Section II-D.
84. VOC emission factor is an average of three values obtained from total
hydrocarbon emissions testing of a cupola furnace (Site MET-A). Draft
Final Test Report. National Dioxin Study. Tier 4: Combustion Sources.
Prepared for U. S. Environmental Protection Agency. Research Triangle
Park, North Carolina. January 10, 1986. pp. 5-6, 5-13, and 5-15.
85. VOC emission factor based on the mean of less than five VOC values
obtained from NEDS User Point File Data Selection Report.
March 27, 1986.
86. Reference 85, based on the mean of five to nine VOC values.
157
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87. Reference 85, based on the mean of 10 to 15 VOC values.
88. Reference 85, based on one VOC value.
89. VOC emissions are expected to be negligible based on a review of the
process description provided in "Kirk Othmer Concise Encyclopedia of
Chemical Technology, Phosphorus and the Phosphides." John Wiley and
Sons, Inc. 1985. Elemental phosphorus is produced in a one-step
process in an electric furnace. Carbon monoxide is the pollutant of
concern in this process.
90. VOC emissions from material handling and preparation for calcining are
estimated to be zero based on engineering judgement. Emissions from
the actual calcining process are included under each specific material
source category (gypsum, lime, etc.).
91. Emission factors listed for coating oven heaters are based on emissions
from the combustion source only. Emissions from the solvents and
coatings are included in the factors for coating ovens, general
(4-04-008).
92. VOC emission factor estimates for the single chamber incinerator were
calculated using the ratio of emissions from single versus multiple
chamber incinerators listed for solid waste disposal. VOC emission
factors for brake shoe debonding were transferred from those listed for
electrical windings reclamation assuming that they have similar
phenolic resin components. SO emission factor was transferred from
those listed for incineration 8f industrial solid waste (5-03-001).
93. SO and NO emission factors based on the average of four emission
tests submitted by companies to JACA Corporation. Summary information
in: Listing of Iron and Steel Stack Test Reports. September 1986
UPDATE. Prepared under EPA Contract No. 68-02-3962 by JACA
Corporation.
94. SO emission factors based on the average of four emission tests
submitted by companies to JACA Corporation. Summary information in:
Listing of Iron and Steel Stack Test Reports. September 1986 UPDATE.
Prepared under EPA Contract No. 68-02-3962 by JACA Corporation,
95. VOC emission factor based on a test report submitted by a company to
JACA Corporation. Emissions were reported as total organics and may be
an overestimate of VOC. Summary information in: Listing of Iron and
Steel Stack Test Reports. September 1986 UPDATE. Prepared under EPA
Contract No. 68-02-3962 by JACA Corporation.
96. NO emission factor based on the average of three emission tests
submitted by a company to JACA Corporation. Summary information in:
Listing of Iron and Steel Stack Test Reports. September 1986 UPDATE.
Prepared under EPA Contract No. 68-02-3962 by JACA Corporation,
158
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97. SO emission factor based on the average of three emission tests
submitted by companies to JACA Corporation. Summary information in:
Listing of Iron and Steel Stack Test Reports. September 1986 UPDATE.
Prepared under EPA Contract No. 68-02-3962 by JACA Corporation.
98. VOC emissions from Petroleum Refinery Wastewater Systems - Background
Information Document for Proposed Standards. EPA-450/3-85-001a.
February 1985. p. 3-53. The emission factor presented is for an
uncovered dissolved air floatation (OAF) unit and represents the worst
case for additional treatment. If an induced air floatation (IAF) unit
is used, an emission factor of 0.01 lb/10 gallons wastewater should be
used.
99. Reference 98, p. 3-57. The VOC emission factor presented is for an
uncovered dissolved air floatation (DAF) unit and represents the worst
case for additional treatment. If an induced air floatation (IAF) unit
is used, an emission factor of 0.20 lb/10 BBLs refinery feed should be
used.
100. VOC emission factor estimate is an average based on six values, from
Table 3-3, Survey of Carbon Tetrachloride Emission Sources (NESHAP).
EPA-450/3-85-018 (NTIS PB85-221661/REB), July 1985. The value is based
on total fugitive emissions of CC1. via the hydrocarbon chlorinolysis
process. A value of 23,800 Ibs/yelr is obtained based upon a mean of
six values via the hydrochlorination/direct chlorination process.
101. VOC emission factor estimate is an average based on 11 values
calculated from Table 2-6. Memo from Kuhn, K. Q. and R. A. Wassel to
Butadiene Source Category Concurrence File, Estimates of 1,3-Butadiene
Emissions From Production Facilities with Additional Controls.
March 25, 1986.
102. Emission factors are based on emission tests submitted by companies to
JACA Corporation. Summary information in: Listing of Iron and Steel
Stack Test Reports. September 1986 UPDATE. Prepared under EPA
Contract No. 68-02-3962 by JACA Corporation. VOC and SO emission
factors are the average of three test results. NO emission factor
based on one test.
103. VOC and NO emission factor from Organic Chemical Manufacturing,
Volume 6: Selected Processes. EPA-450/3-80-028a (NTIS PB81-220660),
December 1980. Report 7. Table IV-1. Based on uncontrolled emissions
from a model plant. Drying and cooling of adipic acid create primarily
particulate matter emissions.
104. VOC emission factor based on the average of two numbers reported in
Organic Chemical Manufacturing, Volume 8: Selected Processes.
EPA-450/3-80-028C (NTIS PB81-220576), December 1980. Report 4. The
product recovery column is synonymous with the distillation column
vent.
159
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105. VOC emission factor from Organic Chemical Manufacturing, Volume 10:
Selected Processes. EPA-450/3-80-028e (NTIS PB81-220592),
December 1980. Report 9. p. IV-2. The factor presented for methyl
ethyl ketone production is based on number for four different
processes.
106. VOC emission factor from Organic Chemical Manufacturing, Volume 6:
Selected Processes. EPA-450/3-80-028a (NTIS PB81-220550),
December 1980. Report 5. pp. IV-1 to IV-4.
107. VOC emission factor for kilns was transferred from factors listed for
the lime manufacturing industry. Emissions are from the combustion
source and it was assumed that the kiln is direct-fired burning natural
gas. A 98 percent combustion efficiency was assumed.
108. VOC emission factor from Organic Chemical Manufacturing, Volume 7:
Selected Processes. EPA-450/3-80-028b (NTIS PB81-220568),
December 1980. Report 6. pp. IV-1 to IV-3. NO emissions are
expected to be zero based on a review of the raw materials and process
description.
109. NO emission factor value was extracted from Tables in Survey Reports
on Atmospheric Emissions from the Petrochemical Industry - Volume 2.
EPA-450/3-73-005b (NTIS PB244958), April 1974. Emissions data were
collected through Industry Questionnaires in the early 1970s by the
Houdry Division, Air Products and Chemicals, Inc. These emission
factors should only be used in the absence of more recent source
specific emissions data.
110. VOC emission factor from Synthetic Fiber Production - Background
Information for Proposed Standards. EPA-450/3-82-011a
(NTIS PB83-153015), March 1982. Factors for dope preparation and fiber
extrusion were estimated using engineering judgement and review of
emission factors listed for similar processes in plastics production
industry.
111. VOC emission factor from Synthetic Fiber Production - Background
Information for Proposed Standards. EPA-450/3-82-011a
(NTIS PB83-153015), March 1982. Table C-8. The emission factor
reported is the average of five plant types.
112. VOC emission factor is the sum of emission factors for three processes:
washing, drying, and finishing. Washing emission factor is the average
of three plant values from Synthetic Fiber Production - Background
Information for Proposed Standards. EPA-450/3-82-011a
(NTIS PB83-153015), March 1982. Table C-8. Drying and finishing
emission factors are the average of values listed on the above table
and that of Table 17 in Source Assessment: Cotton and Synthetic Woven
Fabric Finishing. EPA-600/2-80-042a (NTIS PB81-161937), February 1980.
160
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113. VOC emission factor is the average of five plant types from Synthetic
Fiber Production - Background Information for Proposed Standards.
EPA-450/3-82-011a (NTIS PB83-153015), March 1982. pp. 6-16, 6-23,
6-28, 6-34, and 6-40.
114. VOC emission factors estimated from process descriptions provided in
Industrial Process Profiles for Environmental Use: Chapter 9. The
Synthetic Rubber Industry. EPA-600/2-77-0231 (NTIS PB 281480/4),
February 1977. The monomer is stored in pressure tanks and emissions
are expected to be negligible. Emissions from the steam stripper are
sent to a recovery system and under normal operations should be
negligible.
115. SO emission factor from Multimedia Pollution Assessment of the Wood
Products Industries (Final Report). EPA-600/2-81-008
(NTIS PB84-160266), February 1984. Table 55.
116. SO emission factor from Multimedia Pollution Assessment of the Wood
PrSducts Industries (Final Report). EPA-600/2-81-008
(NTIS PB84-160266), February 1984. Page 144 indicates neutral sulfite
semi-pulp and sulfite pulp should have similar values for this process.
This value is listed under sulfite pulping for MgO systems.
117. VOC emission factor from Textile Dyes and Dyeing Equipment:
Classification Properties and Environmental Aspects (Final Report).
EPA-600/2-85-010 (NTIS PB85-173771/REB), February 1985. Table 54.
118. VOC emission factor based on the average of eight stack tests. From
Source Assessment: Cotton and Synthetic Woven Fabric Finishing.
EPA-600/2-80-042a (NTIS PB81-161937), January 1980. Table B-5.
119. VOC emission factors from Source Category Survey: Refractory Industry.
Chapter 5. EPA-450/3-80-006 (NTIS PB81-111445), March 1980. Value
reported is for total hydrocarbon and may overestimate VOC emissions.
120. SO emission factor based on one emission test from State files
(State H).
121. NO and SO emission factor estimate based on reported emissions from
industry test results taken from State files (State H).
122. SO emission factor based on one value from State files (State D).
A
123. VOC emission factor based on reported emissions from industry test
results taken from State files (State H).
124. NO and SO emission factors based on the average of three emission
tests from State files (State D). VOC emission factor based on two
values from State files (State D). VOC emissions are reported as total
hydrocarbons and may overestimate VOC's.
161
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125. VOC emission factor from Organic Chemical Manufacturing, Volume 6:
Selected Processes. EPA-450/3-80-028a (NTIS PB81-220550),
December 1980. Report 4. Table IV-1. No NO or SO emissions are
expected based on a review of the raw materials and process
description.
126. VOC emissions are estimated from AP-42 (6.6-3) and "Modern Pollution
Control Technology," Volume 1, 1973, by the Research and Education
Association, New Mexico. Steam tube dryer emissions will be primarily
from the fish; VOC emission factor is transferred from stale fish
cookers. Direct-fired dryer emissions are from both the fish and
combustion products; VOC emission factor is the sum of emission factors
from fish cookers and residential furnaces and domestic/commercial
boilers with natural gas or distillate oil averaged. These factors
should only be used in the absence of better data.
127. VOC and NO emission factors are estimated to be negligible for
electric induction furnaces because the metal must be clean and dry if
it is to be charged to this type of furnace. SO emission factor was
transferred from 3-04-002-24. x
128. SO emission factor based on one value from State files (State F).
129. Emission factors for all process heaters were transferred from the
emission factors calculated for process heaters in the oil and qas
production source category. Assuming that emissions from process
heaters are dependent on the type of fuel burned rather than on the
material being heated, the emission factors have been transferred to
other industries.
130. VOC emission factors for incinerators and flares were estimated
assuming 98 percent combustion efficiencies, which is currently
accepted as achievable by EPA, in its standards development activities.
Speciated composites for ten natural gas samples were obtained from
"Emissions from Refinery Process Heaters Equipped with Low-NO
Burners" (KVB11-6019-1274), prepared by KVB, Inc., Research aftd
Analyses Division under EPA Contract No. 68-02-2645, March 1981 and
"NO Emissions from Petroleum Industry Operations," (API Publication
No. 4311), prepared by American Petroleum Institute, October 1979. The
calculated emission factor for natural gas-fired incinerators
represents an estimate which should be used only in the absence of
specific emissions data. There is great variability in the operating
parameters of incinerators (i.e., temperature, residence time) which
should be considered in applying these emission factor estimates.
VOC emission factors for oil-fired and process gas-fired incinerators
were estimated from emission factors presented for oil-fired process
heaters because no "typical" speciated profiles were obtained for oil
process gas. The ratio of emissions from gas-fired incinerators to
emissions from gas-fired process heaters was applied to the other
162
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fuel-fired heaters to obtain emission factor estimates for
incinerators. The estimated VOC emission factors for incinerators and
flares were transferred to other industries assuming that the emissions
from these combustion sources are dependent on the type of fuel burned,
rather than on the material being heated or burned.
131. NO emission factor based on the mean of two emission tests from State
fifes (State I).
132. SO emission factor based on the mean of nine emission tests from State
fifes (States D and I).
133. SO emission factor based on the mean of two emission tests from State
fifes (State I).
134. Emission factors based on data from State files. SO emission factor
based on the mean of two values. VOC emission facto? based on one
value. NO emission factor based on the mean of two values. (Data
from States D and I). State D reports VOC's as total hydrocarbon which
may overestimate VOC's.
135. NO., and SO., emission factors based on data from State files. NO^
136.
emission flctor is the mean of two values. SO emission factor
based on one value. (Data from States D and Ij.
VOC emission factor based on one to two values from State files
(State I).
137. NO emission factor based on the mean of five emission tests from State
fifes (State I).
138. VOC and NO emission factors based on the mean of three values from
State file? (States D and E). VOC emissions are reported as total
hydrocarbons and may overestimate VOC's. SO emission factor based on
two values.
139. SO and NO emission factors based on one emission test from State
fifes (State I). VOC emission factor was estimated through technology
transfer from other coal burning boilers using engineering judgement.
140. SO and VOC emission factors based on one value for each pollutant from
Stlte files (State D). VOC emissions are reported as total
hydrocarbons and may overestimate VOC's.
141.
NO emission factor based on one value from State files (State D).
142. Personal communication with one industry representative. VOC emissions
should be constant throughout and are determined by the reactor at the
beginning of the process. VOC emission factor is therefore based on
seven values for the industry from State files (States A and D).
Values from State D represents total hydrocarbons and may overestimate
VOC's.
163
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143. VOC emission factor based on the mean of two to four values from State
files (State D). Emissions are reported as total hydrocarbons and may
overestimate VOC's.
144. VOC emission factor based on the mean of five to nine values from State
files (State D). Emissions are reported as total hydrocarbons and may
overestimate VOC's.
145. NO emission factor based on the mean of 10 to 20 values from State
fifes (State D).
146. SO emission factor based on the mean of two to four values from State
files (State D).
147. NO emission factor based on the mean of five to nine values from State
fifes (State D).
148. Emission factors based on information from State files. SO emission
factor is the average of seven values. NO emission factor is the
average of 72 values. VOC emission factor is the average of 12 values
(State D). VOC emissions are reported as total hydrocarbons and may
overestimate VOC's.
149. NO emission factor based on two to four values from State files
(State D).
150. VOC emission factor based on one value from State files (State D).
Emissions are reported as total hydrocarbons and may overestimate
VOC's.
151. VOC emission factor based on personal communication with Mr. Andy Caron,
National Council for Air and Stream Improvement for the Pulp and Paper
Industry (NCASI). January 1987. Data were specific to the MgO process,
measured at the acid tank exit, however, Mr. Caron thought that similar
levels would be found at any acid plant. In the absence of better
data, this figure is supplied as an approximation.
152. VOC emission factors based on information from the National Council on
Air and Stream Improvement for the Pulp and Paper Industry (NCASI)
Technical Bulletin #371, May 1982. Data are in units of total gaseous
non-methane organics used as best estimate of VOC's.
153. VOC emission factors based on information from the National Council on
Air and Stream Improvement for the Pulp and Paper Industry (NCASI)
Technical Bulletin #358, September 1981. Data are in units of total
gaseous non-methane organics used as best estimate of VOC's.
154. VOC emission factors based on information from the National Council on
Air and Stream Improvement for the Pulp and Paper Industry (NCASI)
Technical Bulletin #112, February 1981. Emissions were measured after
an electrostatic precipitator and an induced fan draft. Values are
reported as total gaseous non-methane organics.
164
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155. SO and NO emission factor values were extracted from Tables in Survey
Reports onxAtmospheric Emissions from the Petrochemical Industry -
Volume 4. EPA-450/3-73-005d (NTIS PB 245630), April 1974. Emissions
data were collected through Industry Questionnaires in the early 1970's
by the Houdry Division, Air Products and Chemicals, Inc. These
emission factors should only be used in the absence of more recent
source specific emissions data.
156. SO and NO emission factor values were extracted from Tables in Survey
Reports onxAtmospheric Emissions from the Petrochemical Industry -
Volume 2. EPA-450/3-73-005b (NTIS PB 244958), April 1974. Emissions
data were collected through Industry Questionnaires in the early 1970's
by the Houdry Division, Air Products and Chemicals, Inc. These
emission factors should only be used in the absence of more recent
source specific emissions data.
157. These VOC emission factors were calculated from emission factors
reported for 4-01-002-01 through 4-01-002-07. Unit conversions were
made using information on specific gravities for different solvents
from Table 10 of Source Assessment: Solvent Evaporation - Degreasing
Operations. EPA-600/2-79-019f (NTIS PB80-128812), August 1979.
158. NO and VOC emission factors extracted from Table 5-7 in Source
Category Survey: Mineral Wool Manufacturing Industry.
EPA-450/3-80-016 (NTIS PB80-202781), March 1980. An emission factor of
negligible is listed where no emissions were reported in this document.
159. Information from "Source Category Survey: Perlite Industry" indicate
that SO , NO , and VOC emissions from this industry are negligible.
Chapterx5. EPA-450/3-80-005 (NTIS PB80-194822), May 1980.
160. No emissions are expected based on information from Source Category
Survey: Ceramic Clay Industry. Chapter 1. EPA-450/3-80-017
(NTIS PB80-227507), March 1980.
161. Negligible amounts of NO and VOC emissions are expected from thermal
process phosphoric acid plants. Information from Source Category
Survey: Thermal Process Phosphoric Acid Manufacturing Industry.
EPA-450/3-80-018 (NTIS PB80-193469), May 1980. Chapter 5.
162. VOC emission factors were transferred from that listed for 3-05-014-02.
According to process descriptions and emissions described in "Glass
Manufacturing Plants - Background Information for Proposed Standards of
Performance," the melting furnaces are the same and hydrocarbon
emissions should be independent of the type of glass produced.
EPA-450/3-79-005a (NTIS PB 298528/1), June 1979. Chapter 3.
163. VOC emission factor estimated from personal communication with the
South Coast Air Quality Management District, California.
March 31, 1987. VOC emission factor is based on AP-42 information for
reduction cookers and is therefore only an estimate of hydrocarbons.
165
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164. VOC emissions factors from "The Effects of the Operating Variables and
Refuse Types on the Emissions from a Pilot Scale Trench Incinerator."
John 0. Burckle, National Center for Air Pollution Control. Fairfax
Facility, Cincinnati, Ohio. Paper was prepared for presentation at the
1968 National Incinerator Conference, May 5-8, 1968 in New York City
and publication in the proceedings of the conference. SO and NO data
were measured but not reported.
165. Benzene emissions from Maleic Anhydride Industry - Background
Information for Proposed Standards. Draft EIS, February 1980. NO
calculation based on data from one plant. Sample was taken at exit of
incineration after product recovery absorber, using EPA Method #7.
166. VOC emission factor based on the mean of two values from State permit
files (States E and K).
167. VOC and NOW emission factor based on one value from State permit files
(State K).
168. VOC, NO. and SO emission factors based on one value from State permit
files (State K).x The VOC and SO factors listed for the general
categories (3-01-043-01) were transferred to those listed in each
specific process.
169. VOC, NO , and SO emission factor based on the average of five values
from State permit files (State K).
170. VOC, NO , and SO emission factor based on two reported values from
State pirmit fills (State K).
171. NO and SO emission factor based on the average of two values from
Stlte permtt files (State K).
172. Personal communication with Mr. Victor Gallons, National Council on Air
and Stream Improvement for the Pulp and Paper Industry (NCASI).
January 1987. The emissions from these processes are usually vented
and burned, either at the recovery furnace, the lime kiln, or an
auxiliary system; therefore, only fugitive emissions would be found at
these sources.
173. Personal communication with Mr. Bill Fuller, Oregon Department of
Environmental Quality. January 26, 1987. NO emission factor from
National Council on Air and Stream Improvement for the Pulp and Paper
Industry (NCASI) Technical Bulletin #105, December 1977. SO emission
factor from three monitoring data figures (1978-1986) averagid.
174. Personal communication with Mr. Victor Dallons, National Council on Air
and Stream Improvement for the Pulp and Paper Industry (NCASI).
January 1987. Mr. Dallons felt that veneer dryers would overestimate
the VOC emissions; however, he was not aware of any data generated in
this industry. Numbers are from NCASI Technical Bulletin #405,
August 1983. The coe dryer is assumed to be a steam-heated type of
dryer. Units are in Ibs CH4/10 square feet as best estimate of VOC's.
166
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175. Personal communication with Mr. Victor Gallons, National Council on Air
and Stream Improvement for the Pulp and Paper Industry (NCASI).
January 1987. Mr. Gallons felt that in the absence of other data (he
was not aware of any generated in this industry), particleboard
pressing might approximate the VOC emissions, NCASI Technical
Bulletin #493, June 1986.
176. SO emission factor based on the average of five test values from State
fifes (State C).
177. SO emission factor based on the average of 11 test values from State
fifes (State C).
178. VOC emission factors based on information from EPA Guideline Series:
Control of Volatile Organic Compound Emissions from Manufacture of
High-Density Polyethylene, Polypropylene, and Polystyrene Resins.
EPA-450/3-83-008 (NTIS PB84-134600), November 1983. Figures are based
on emissions from a model plant which are flared at exit as a means of
control. Conveying - closed loop drying system. Storage • polymer
fluff storage and mixers.
179. VOC emission factor based on information from EPA Guideline Series:
Control of Volatile Organic Compound Emissions from Manufacture of
High-Density Polyethylene, Polypropylene and Polystyrene Resins.
EPA-450/3-83-008 (NTIS PB84-134600), November 1983. Figure is based on
emissions from a model plant and is a combination of two sources: the
devolatilizer condenser vent, and the styrene recovery unit condenser
vent.
180. VOC emission factor estimates are based on information from "Rubber
Tire Manufacturing Industry - Background Information for Proposed
Standards." Draft EIS. EPA-450/3-81-008a (NTIS PB83-163543),
July 1981. Approximately 90 percent of the solvent applied to the
rubber during tire manufacturing evaporates within 30 seconds. For
green tire spraying, approximately 8 percent of the VOC's applied to
the rubber are absorbed and the other 92 percent evaporates. In the
absence of test data, emission factor estimates were generated using
these percentages. Swabbing is a similar process to dipping. Solvent
storage is considered negligible based on engineering judgement.
181. VOC emission factor based on information from "Industrial Process
Profiles for Environmental Use: Chapter 25. Primary Aluminum
Industry." EPA-600/2-77-023y (NTIS PB 281491/1), February 1977.
p. 22. Hydrocarbon emissions are estimated to be 0.025 to
0.075 percent of the aluminum produced. The mid-point of this
percentage was used to calculate an estimated VOC emission factor.
182. SO. NO. and VOC emissions are assumed to be zero based on information
from "Industrial Process Profiles for Environmental Us6: Chapter 29.
Primary Copper Industry." EPA-600/2-80-170 (NTIS PB81-164915),
July 1980. p. 94. The only pollutant emitted to the air by an
electrolytic refinery is a fine sulfuric acid.
167
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183. SO , NO , and VOC emission factors based on information from
"Ifidustml Process Profiles for Environmental Use: Chapter 24. The
Iron and Steel Industry." EPA-600/2-77-023x (NTIS PB 266226/0),
February 1977. p. 116. The only atmospheric emissions occurring
during this process are acid fumes.
184. NO emission factor was transferred from that listed for cupolas in
gray iron foundries (3-04-003-01).
191
185. VOC emission factor was transferred from 3-04-009-01 (annealing for
malleable iron foundry), based on process descriptions from "Organic
Emissions from Ferrous Metallurgical Industries: Compilation of
Emission Factors and Control Technologies." EPA-600/2-84-003
(NTIS PB84-141548), January 1984. p. 5-25 to 5-33.
186. VOC emission factors based on information from "Organic Emissions from
Ferrous Metallurgical Industries: Compilation of Emission Factors and
Control Technologies." EPA-600/2-84-003 (NTIS PB84-141548),
January 1984. p. 6-8. Emissions from transfer, cooling, grinding, and
packaging of the produced alloy are expected to contain very little, if
any, organic components.
187. SO , NO , and VOC emission factors were transferred from 3-04-001-04
(FTuxin§, Chlorination). According to AP-42 Fourth Edition,
Section 7.8 (April 1981), "emissions from reverberatory (fluorine)
smelting/refining are similar to those from reverberatory (chlorine)
smelting/refining."
188. VOC emission factor for charging was transferred from 3-03-009-16
(Charging: BOF). Emissions during charging should be independent of
the type of furnace to which the charge is delivered.
189. SO emission factor calculated from information in "Industrial Process
Profiles for Environmental Use. Chapter 27: Primary Lead Industry."
EPA-600/2-80-168 (NTIS PB81-110926), July 1980. p. 42-43. SO
emissions were reported as a volume-percent3with a given flowrlte.
Using an assumed density of S02 - 0.61 Kg/m and a production rate
supplied by Table 24, the factor was calculated.
190. SO , NO , and VOC emissions are expected to be zero based on
information from "Industrial Process Profiles for Environmental Use.
Chapter 27: Primary Lead Industry." EPA-600/2-80-168
(NTIS PB81-110926), July 1980. p. 64.
NO , SO , and VOC emissions from materials crushing and handling are
expectea to be zero based on process descriptions in "Metallic Mineral
Processing Plants: Background Information for Proposed Standards,
Volume 1." EPA-450/3-81-009a (NTIS PB83-113746), August 1982.
Chapter 3.
168
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192. These SO , NO , and VOC emission factors were transferred from
3-05-020-01 t8 3-05-020-04 (Crushing and screening of stone quarrying),
from 3-05-025-10 to 3-05-025-11 (Crushing and screening of sand and
gravel), and 3-05-040-21 to 3-05-040-31 (Conveying, crushing, and
screening in the mining of nonmetallic minerals).
193. SO emission factor based on reported emissions from State files
(Sifate G) and production rates given by industries. This emission
point is for bronze melting in induction furnaces and would be similar
for electric arc furnaces.
194. SO , NO , and VOC emission factors based on the annual usage of core
oil, sand, and amount of cores produced provided by industries in
State G. The assumption made was that the core oil burned completely
off of the core and behaved the same as combusted fuel oil used in an
industrial boiler. Based on information from "Environmental Assessment
of Coal- and Oil-Firing in a Controlled Industrial Boiler; Volume II.
Comparative Assessment," EPA-600/7-78-164b (NTIS PB 289941/7).
Tables 4-3 and 4-6. These emission factors were used for core ovens in
iron foundries and steel foundries.
195. VOC emission factors transferred from 3-03-008-20 and 3-03-008-21
(Sinter transfer and unloading). Since no VOC emissions are expected
from sinter transferring and unloading, it was assumed that no VOC
emissions should result from transferring of charge materials or raw
materials.
196. VOC, NO , and SO emission factors were transferred from similar
operations in the gray iron foundry industry, based on information
about the processes from "Organic Emissions from Ferrous Metallurgical
Industries: Compilation of Emission Factors and Control Technologies"
EPA-600/2-84-003 (NTIS PB84-141548), January 1984. Emission factors
are expressed as total organic emissions which may overestimate VOC's.
197. SO emission factor based on reported emissions from State files
(State G) and production rates provided by industries.
198. VOC emission factor transferred from 3-03-008-11 (Raw material
stockpiles) which is considered a similar process description.
199. These SCC's have been added to NEDS for particulate emissions only.
SO , NO , and VOC emissions, which are products of combustion, are
considered under the SCC's for the actual process listed.
200. Emission factors were based on data taken from "Source Category Survey
for the Acrylonitrile Industry" (Draft), prepared by Energy and
Environmental Analysis, Inc. for the U. S. Environmental Protection
Agency. July 1981. The data were provided by industry with some
storage and fugitive emission figures missing. This estimate
represents acrylonitrile emissions only.
169
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201. NO and SO emission factors based on data from State files (State E).
SO value TS the average of two reported values and NO value is the
average of five values.
202. VOC emission factor is an estimate using technology transfer from
similar processes listed for beer production. VOC emission factors for
fermentation tanks are an estimate based on the average of the two
factors listed for fermentation of wines, brandy, and brandy spirits.
203. SO emission factor based on the mean of three values from State files
(State E).
204. NO emission factors are based on data from State files (State E). NO
emtssion estimates were reported for three SCC's in this source x
category. The emission factor was then transferred to the other SCC's
with the assumption that NO emissions are independent of th« present
conversion of sulfuric acid.
205. SO , NOV, and VOC emission factors based on one value from State files
(S*ate £).
206. NO and VOC emission factors for waste handling of acetylene are the
avlrage of three values from State files (State E). Negligible VOC
emissions are expected from material handling, grinding, and mixing
based on process descriptions provided by Agency personnel in State E.
207. VOC emission factor based on one value from State files (State E).
208. SO and NOV emission factors are the average of two values from State
fifes (State E).
209. NOV emission factor based on one value submitted from State files
(State E).
210. SO emission factor based on one value submitted from State files
(State E).
211. SO emission factor is the average of four values from State files
(State E).
212. NO emission factor is the average of 58 values from State files
(States 0 and E).
213. Personal communication with Mr. Harry Kelly, Montana Air Bureau.
February 1987. Engineering estimation methods were used to derive
figures. Emissions are from the fuel used in the boilers and dryer of
the one facility in Montana. They estimate VOC's are not zero, but no
data are available.
170
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214. Personal communication with Mr. Al Carlucci, Erie County Regional
Office, New York. February 1987. Production data and solvent use data
are from one plant. Solvent mixing is an estimated figure. Emission
factor is also based on data provided by the State (State G) and is for
total hydrocarbon emissions as the best estimate of VOC's.
215. Atmospheric emissions from breathing losses from underground storage
tanks are considered negligible. Information from "Underground Storage
Tanks: Problems, Technology and Trends" by Paul H. Woods, Jr. and
Dale E. Webster, Pol 1ution Enqineerino. July 1984 and "Underground Tank
Management" by Paul V. Knopp, Pollution Engineering. September 1985.
VOC emission factors for working losses from underground storage tanks
were calculated using correlations in AP-42 Fourth Edition,
Section 4.4-5, assuming an ambient temperature of 60 F.
216. NO and SO emission factors were transferred from 3-05-001-01 to
3-05-001-04. VOC emission factor for blowing was calculated from
averaging eight results from emissions tests reported in "Asphalt
Roofing Manufacturing Industry: Background Information for Proposed
Standards." EPA-450/3-80-021a (NTIS PB80-212111), June 1980.
(Appendix C.) VOC emission factors for dipping and spraying were
transferred from 3-05-001-03 and 3-05-001-04, based on information
about the processes provided in the above document (Chapter 3).
217. SO emission factor estimate was calculated using feed and production
"ates presented in "Level 1 Assessment of Uncontrolled Sinter Plant
Emissions." EPA-600/2-79-112 (NTIS PB 298005/5), May 1979. Profiles
listing typical quantities of sulfur in feed coke were obtained from
"Applicability of Coke Plant Control Technologies to Coal Conversion."
EPA-600/7-79-184 (NTIS PB80-108954), August 1979. p. 35. SO emission
factor was calculated assuming all sulfur is converted to SO-.
218. SO emission factor was calculated from information contained in
"Industrial Process Profiles for Environmental Use, Chapter 28:
Primary Zinc Industry." EPA-600/2-80-169 (NTIS PB80-225717),
July 1980. p. 53. SO. emissions are given in ppm, along with flow
rates and temperatures of carrier gas and the density of SO-.
219. SO and VOC emission factors based on information contained in
"Industrial Process Profiles for Environmental Use, Chapter 28:
Primary Z1nc Industry." EPA-600/2-80-169 (NTIS PB80-225717),
July 1980. SO- emission factors were calculated using information on
flow rates, concentrations, feed capacities, and zinc content.
p. 33-38. VOC emissions are considered to be zero based on qualitative
descriptions of atmospheric emissions from these sources: "Waste
streams contain SO,, oxygen, nitrogen, carbon dioxide, and water vapor
only." £
171
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220. SO , NO , and VOC emission factors for ore dryers in the metallic
mifierali industry were calculated using information from "Calciners and
Dryers in Mineral Industries - Background Information for Proposed
Standards." EPA-450/3-85-025a (NTIS PB86-196904/XAB), October 1985.
The majority of dryers used in this industry are direct rotary dryers
fired with natural gas (Chapter 3). A 98 percent efficiency of
combustion was assumed.
221. VOC emission factor based on emissions data from State files (State G).
Production rates and heating load of the equipment were provided by
company.
222. NO and VOC emissions are expected to be zero based on information from
"Industrial Process Profiles for Environmental Use, Chapter 28:
Primary Zinc Industry." EPA-600/2-80-169 (NTIS PB80-225717),
July 1980. p. 70-72.
223. VOC emission factor calculated from information in "Calciners and
Dryers in Mineral Industries - Background Information for Proposed
Standards." EPA-450/3-85-025a (NTIS PB86-196904/XAB), October 1985.
The majority of calciners in these industries are fired with natural
gas (Chapter 3). Typical capacities of these calciners were listed and
a 98 percent combustion efficiency was assumed.
224. VOC emission factor based on 11 values from State files (State D).
Emissions are reported as total hydrocarbons and may overestimate
VOC's.
225. VOC emission factors for coal cleaning thermal dryers were transferred
from the AP-42 derived emission factor for fluidized bed thermal
dryers. All dryers listed are direct-fired and operate at similar
temperatures. Seventy-five percent of the dryers used in coal cleaning
are fluidized-bed dryers. Descriptions of dryers used in this industry
are found in "Assessment of Coal Cleaning Technology: First Annual
Report." EPA-600/2-78-150 (NTIS PB 287091/3), July 1978, p. 127-132,
and in "A Review of Standards of Performance for New Stationary
Sources - Coal Preparation Plants." EPA-450/3-80-022
(NTIS PB82-193053), December 1980.
226. VOC emission factors were calculated from information in "Standards
Support and Environmental Impact Statement, Volume 1: Proposed
Standards of Performance for Lime Manufacturing Plants."
EPA-450/2-77-007a (NTIS PB 226942/2), April 1977. Calciners and kilns
are fired with natural gas and a 98 percent combustion efficiency was
assumed. VOC emission factors were calculated using heats of reactions
given for calcination reactions.
227. VOC emission factors for storage of petroleum distillate were
transferred from those listed for naphtha due to similar volatilities.
Petroleum distillates differ from source to source and this factor
should be used only in the absence of specific information on the
components of the distillate.
172
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228. NO and VOC emission factors were calculated based on information from
"Industrial Process Profiles for Environmental Use, Chapter 29:
Primary Copper Industry." EPA-600/2-80-170 (NTIS PB81-164915),
July 1980. p. 30-45. A 98 percent combustion efficiency was assumed.
229. VOC emission factors were calculated based on information from
"Industrial Process Profiles for Environmental Use, Chapter 27:
Primary Lead Industry." EPA-600/2-80-168 (NTIS PB81-110926),
July 1980. p. 49. Natural gas is the fuel used and a 98 percent
combustion efficiency was assumed. SO and NO emissions calculated
from "Compilation of Air Pollutant Emission Factors" (Section 1.4) and
were assumed to result only from fuel combustion.
230. VOC and NO emission factors based on emissions from State files
(State G) and emissions provided by companies. An average of four
emission tests was taken to generate an emission factor estimate for
this general category. The number listed for VOC represents total
hydrocarbons and may be an overestimate of VOC.
231. Personal communication with Mr. Steve Jenness, Army Environmental
Hygiene Agency, Maryland. February 1987. Mr. Jenness only had the
AP-42 data (Table 5.6-2) and said that VOC's (toluene and
trinitromethane) were found to be negligible. Personal communication
with Mr. James Morris at Radford Army Ammunition Manufacturing Plant.
February 1987. He thought that the batch process was no longer being
used, but emissions would be similar. Emissions from the incinerator
were assumed to be similar to those from open burning of waste.
232. These chemicals are solids at ambient temperatures and are stored in
containers or tanks which could, theoretically, be classified as fixed
roof tanks. VOC emissions would be negligible (if any) when storing
these solids.
233. VOC emission factors for withdrawal losses from these general
categories were transferred from emission factors calculated for
withdrawal losses from specific chemicals listed in each category.
Withdrawal losses are very small for all chemicals and variations are
minimal between different chemicals.
234. VOC emission factor was calculated using heat load information from
"Industrial Process Profiles for Environmental Use, Chapter 24: Iron
and Steel Industry." EPA-600/2-77-023X (NTIS PB 266226/0),
February 1977. p. 30-35.
235. VOC emissions for casting operations are considered negligible based on
information from "Industrial Process Profiles for Environmental Use,
Chapter 24: Iron and Steel Industry." EPA-600/2-77-023x
(NTIS PB 266226/0), February 1977. p. 111.
173
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236. VOC emission factors for solid waste and liquid waste-fired boilers
were transferred from those listed for industrial solid waste and
liquid waste-fired boilers. These emission factors are estimates at
best, and emissions will vary greatly depending on the type of waste
being burned. NO and SO emission factor estimates for waste oil were
transferred from those listed for residual oil.
237. NO and VOC emission factors were calculated using information on
process descriptions from "Industrial Process Profiles for
Environmental Use, Chapter 24: Iron and Steel Industry."
EPA-600/2-77-023X (NTIS PB 266226/0), February 1977. Heating values
for the fuels and emission factors for the fuel combustion are from
AP-42 Third Edition, "Compilation of Air Pollutant Emission Factors"
(Sections 1.1, 1.3, 1.4, and Appendix A-10). VOC emissions are assumed
to result only from the fuel combustion.
238. VOC emission factor was calculated from data in Table 7-7 in
"Assessment of Atmospheric Emissions from Petroleum Refining:
Volume 1." EPA-600/2-80-075a (NTIS PB80-225253), July 1980. The
numbers and types of sources are highly variable, and emissions are
dependent on process conditions. This factor is best used only when
individual refinery data are not available.
239. VOC emission factor was transferred from 3-04-002-23 (electric
induction furnace). Since both furnace types operate on electricity,
emissions are assumed to be similar.
240. VOC and SO emission factors were transferred from other heaters listed
in the fooa and agriculture Industry. SO emissions come only from the
combustion source. AP-42 lists emission factors for aldehydes arid
organic acids from roasting of coffee beans. VOC also are generated
from the combustion materials. The emission factors presented are
estimates at best and should only be used in the absence of specific
emissions data.
241. VOC emissions are expected to be zero based on qualitative information
provided in AP-42 Third Edition, "Compilation of Air Pollutant Emission
Factors" (Section 7.5).
242. VOC, NO , and SO emission factors were transferred from annealing
furnaces in othe? industries based on process descriptions provided in
AP-42 Third Edition, "Compilation of Air Pollutant Emission Factors"
(Section 7.5).
243. VOC emission factor was estimated based on process descriptions given
in "Electric Arc Furnaces in Ferrous Foundries - Background Information
for Proposed Standards." EPA-450/3-80-020a (NTIS PB80-202997),
May 1980. When working with alloys, tapping emissions are somewhat
greater than charging emissions due to the higher temperatures
required. Using engineering judgement, the emission factors for
charging were doubled to give a best estimate of VOC emissions from
tapping operations.
174
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244. VOC emission factor was transferred from the listing for commercial/
institutional pathological waste incinerator as the best estimate of
VOC emissions from government pathological waste incinerators.
Emissions will vary depending on the type of waste burned and this
emission factor should only be used in the absence of source specific
test data.
245. VOC emission factor was transferred from the listing for aluminum
sweating furnace (3-04-001-01) based on the similarity of process
descriptions for foil converting.
246. SO , NO , and VOC emission factors estimated to be zero based on
process descriptions given in "Industrial Process Profiles for
Environmental Use, Chapter 24: Iron and Steel Industry."
EPA-600/2-77-023X (NTIS PB 266226/0), February 1977, and AP-42 Third
Edition, "Compilation of Air Pollutant Emission Factors"
(Section 7.10).
247. VOC emission factor was transferred from a similar process description
in the primary and secondary zinc industry.
248. VOC emission factor was transferred from emission factors calculated
for similar furnaces in the secondary aluminum industry.
249. VOC emission factor was transferred from an emission factor calculated
for a similar furnace used in gray iron melting.
250. VOC emission factor was transferred from emission factor calculated for
similar processes in the lime manufacturing industry assuming that
emissions are from the fuel combustion only.
251. SO emission factor was transferred from a similar furnace in the
secondary aluminum industry (3-04-001-12).
252. VOC emission factors were transferred from emission factors calculated
for similar furnaces used in the primary steel industry.
253. NO and SO emission factors were transferred from listings for an
electric arc furnace heating alloy steel.
254. No VOC emissions are expected from these sintering processes because
all vents are tied into the sintering wind box.
255. VOC emissions for teeming were transferred from listings for tapping.
Teeming is the process of pouring hot iron or steel into molds.
Temperatures of the molten iron or steel would be similar to
temperatures during tapping, therefore, similar emissions are expected.
256. The characteristics for formalin were calculated assuming the solution
contained 40 percent formaldehyde and 60 percent water.
175
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257. Personal communication with Mr. Jay Willenberg, Washington Department
of Ecology. March 1987. No test data are available on NO or VOC's.
NO emissions are expected to be zero due to low temperatures of
operation.
258. VOC emission factor estimates were assigned based on information
provided from two studies on wastewater treatment plants conducted by
U. S. EPA Region I. The factor for the entire plant was generated from
data provided. This factor was then divided among the primary and
secondary settling tanks by engineering judgement. VOC emissions are
dependent on the treatment method and the content of the VOC's in the
wastewater influent; therefore, these estimates should be used oily in
the absence of site specific data.
259. Personal communication with Mr. Jay Willenberg, Washington Department
of Ecology. March 1987. No NO and negligible VOC's are expected; the
first due to low operating temperatures, the second because there is no
apparent source.
260. NO and SO emissions are expected to be zero due to the lack of a
potential source. Organic emissions result mainly from the wood itself
and these naturally occurring organic species (i.e., terpenes) are not
considered volatile using EPA's definitions. Therefore, VOC emissions
are estimated to be negligible.
261. Personal communication with Mr. Mike Styk, New York Regional Office.
February 1987. Mr. Styk thought that SO and NO would be zero because
the operation takes place in an inert atmosphere. Personal
communication with one company representative from the State files
provided the production information. February 1987. The emission
factor for VOC is based on one facility.
262. SO , NO , and VOC emissions are considered negligible for these
physical processes based on engineering judgement.
263. SO and NO emissions are considered to be zero due to the type of
chemical being stored.
264. Personal communication with industry personnel. March 1987. Industry
provided data on four facilities, from which an SO emission factor was
calculated. x
265. "Negligible VOC emissions" was taken from the Food and Wood Products
Branch Program on Wood Preserving Industry Summary Status (Handout),
Draft. February 18, 1982.
266. Personal communication with Mr. Victor Dallons, NCASI
(January 26, 1987) and Mr. Jay Willenberg, Washington Department, of
Ecology (March 2, 1987), indicated that emissions from the fluid bed
calciner would probably be similar to those from the lime kiln.
176
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267. NO emission factor was transferred from other calciners in the mineral
products industry using engineering judgement.
268. VOC emissions were derived from "Organic Chemical Manufacturing,
Volume 8: Selected Processes." EPA-450/3-80-028c (NTIS PB81-220576),
December 1980. The general SCC is an underestimate of VOC's. No NO
or SO emissions are expected from review of the process.
^
269. VOC emissions (except for fugitive emissions) are based on a model
plant and data from industry presented in "Organic Chemical
Manufacturing, Volume 8: Selected Processes." EPA-450/3-80-028c
(NTIS PB81-220576), December 1980. From the process description
(assuming methane chlorination process), no NO emissions are expected.
SOX emissions from the H2$04 dryers are expected to be negligible.
270. SO and NO emission factors were transferred from factors listed for
otner calciners in the mineral products industry.
271. SO emission factor based on personal communication with Mr. Lloyd
Kostaw, Oregon Department of Environmental Quality. March 12, 1987.
There is no potential source for SO emissions.
272. VOC emission factor is based on personal communication with one plant
from State I data. Cold mix asphalt cement was assumed.
273. No VOC emissions are expected from these processes. Process
descriptions supplied by "Kirk Othmer Concise Encyclopedia of Chemical
Technology, Metal Surface Treatment." John Wiley and Sons, Inc. 1985.
274. NO emission factor was calculated using an estimated average emission
rate provided in "Background Information for Proposed Standards:
Primary Aluminum Industry, Volume 1." EPA-450/2-74-020a
(NTIS PB 237612/7B.E), October 1974, and average capacities provided in
"Industrial Process Profiles for Environmental Use, Chapter 25:
Primary Aluminum Industry." EPA-600/2-77-023Y (NTIS PB 281491/1),
February 1977.
275. NO emission factor is estimated to be negligible based on process
description provided in "Industrial Process Profiles for Environmental
Use, Chapter 29: Primary Copper Industry." EPA-600/2-80-170
(NTIS PB81-164915), July 1980. No mention of NO emissions was
provided; therefore, it was inferred that they aPe negligible.
276. NO and SO emissions are considered negligible based on information on
process descriptions from "Industrial Process Profiles for
Environmental Use, Chapter 24: Iron and Steel Industry."
EPA-600/2-77-023X (NTIS PB 266226/0), February 1977.
177
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277. SO , NO , VOC, and CO emission factors were calculated using stack gas
concentrations, flowrates, and charge rates given in "Draft Final Test
Report - Site 10: Secondary Copper Recovery Cupola Furnace, National
Dioxin Study, Tier 4: Combustion Sources." Prepared for U. S.
Environmental Protection Agency. Research Triangle Park, North
Carolina. January 1986.
278. VOC, NO , and SO emission factors are estimated to be zero based on
engineering judgement and a review of the process provided in AP-42
Fourth Edition.
279. NO , SO , and VOC emission factors are estimates using technology
transfer* from atmospheric fluidized beds used for
commercial/institutional external combustion boilers (1-03-002-17).
280. NO and SO emissions are expected to be zero based on personal
coifonuni cation with industry representatives. These are physical
processes in which particulates are the main pollutant of concern.
281. VOC, NO , and SO emission factors were transferred from those listed
for core ovens (3-04-003-51) based on process descriptions provided by
industry personnel.
282. No NO , SO , or VOC emissions are evolved during this process.
"Kirk Othmer Concise Encyclopedia of Chemical Technology, Powder
Coatings." John Wiley and Sons, Inc. 1979.
283. No SO emissions are expected for this process from review of the
process description. Negligible NO emissions are expected due to the
temperature of the process. "Kirk Othmer Concise Encyclopedia of
Chemical Technology, Metallic Coatings." John Wiley and Sons, Inc.
1979.
284. VOC emission factors were transferred from similar processes listed in
vinyl chloride manufacturing.
285. VOC emissions are expected to be negligible from these processes based
on engineering judgement.
286. VOC emission factor based on process description from "Control of
Volatile Organic Emissions from Manufacture of Synthesized
Pharmaceutical Products." EPA-450/2-78-029 (NTIS PB 290580/0),
December 1978. Chapter 3. Four companies submitted emission estimates
indicating that VOC from reactors is well under 100 tons/year. Assumes
that centrifuges and crystallizers are completely enclosed and the only
source of VOC emissions is while product is being loaded and unloaded
to the process unit. Using this information, the emission factor for
3-01-060-05 was applied. Emission factors for solvent usage for
coating and granulation processes were estimated to be 10 percent of
total solvent used, by engineering judgement and typical emissions from
other coating processes.
178
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287. VOC emission factors estimated from process emission ranges in "Control
of Volatile Organic Emissions from Existing Stationary Sources -
Volume II: Surface Coating of Cans, Coils, Papers, Fabrics,
Automobiles, and Light-Duty Trucks." EPA-450/2-77-008
(NTIS PB 272445/8), May 1977. Engineering judgement was used to assign
an approximate percent to each part of the coating process where a
percent was not otherwise given:
Cleaning/pretreatment = NEG
Coating storage = NEG (compared to other operations)
Coating mixing - 10 percent
Equipment cleanup = 10 percent
Coating operation(s) - 80 percent
These are to be used only in the absence of better information.
288. VOC emission factors were estimated from information in Table 5.4-1 in
"Control Techniques for Organic Gas Emissions from Fiberglass
Impregnation and Fabrication Processes." SAI-068-83-001
(NTIS PB82-251103), June 1982. These factors represent total organic
emissions from non-vapor suppressed process operations.
289. VOC emission factor for solvent consumption based on three values from
State files (States A and 0). This emission factor was transferred to
adhesive consumption to provide an estimate of emissions in the absence
of better data. Values from State D represent total hydrocarbon and
may overestimate VOC's.
290. VOC emission factors based on percentages of solvent loss for each
operation in the fabric surface coating industry and estimated from
process descriptions in "Industrial Surface Coating: Appliances -
Background Information for Proposed Standard," Draft EIS.
EPA-450/3-80-037a (NTIS PB82-152174), November 1980. Approximate
ratios of emissions from primer coating and top coat application
derived from AP-42 data. These are to be used only in the absence of
better information.
291. NO emission factors based on 30 to 40 values from State files
(State D).
292. VOC emission factors for chemicals stored in pressure tanks were
estimated based on information in Section 4.3 of AP-42 (September 1985)
and physical properties of the chemicals obtained from chemistry
handbooks. For chemicals stored at pressures higher than 30 psia, no
emissions are expected. For chemicals stored at lower pressure (less
than 30 psia), emissions were estimated assuming 1000 gallon removal.
293. VOC emission factors based on estimated percentages of solvent loss for
each operation in the fabric surface coating industry (see
footnote 287). These are to be used only in the absence of better
information.
179
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294. VOC emission factors based on percentages of solvent loss for an
operation in the fabric surface coating industry and estimated from
process descriptions in "Surface Coating of Metal Furniture -
Background Information for Proposed Standards," Draft EIS.
EPA-450/3-80-007a (NTIS PB81-113938), September 1980. These ar« to be
used only in the absence of better information.
295. No NO emissions are expected based on the process description
presented in "Organic Chemical Manufacturing, Volume 7: Selected
Processes." EPA-450/3-80-0286 (NTIS PB81-220568), December 1980.
296. VOC emission factor based on 11 values from State files (States A and
D). Values from State D are for total hydrocarbon and may overestimate
VOC's. SO emission factor is an estimate derived from the factor
listed for coating oven, general (4-02-008-01), using the same ratio of
emissions as those listed for NO .
^
297. SO emission factor calculated from AP-42 Supplement A value for
screening and grinding less the value for grinding, also given.
298. Particulate matter emission factor is updated from values given in
AP-42 Supplement A (December 1986).
299. SO emission factor is updated from values given in AP-42 Supplement A
(December 1986).
300. NO emission factor is updated from values given in AP-42 Supplement A
(December 1986).
301. VOC emission factor is updated from values given in AP-42 Supplement A
(December 1986).
302. CO emission factor is updated from values given in AP-42 Supplement A
(December 1986).
303. NO emission factor was estimated based on personal communication with
Mr. Willard Hanes, Florida Bureau of Air Quality Management.
March 20, 1987. No NO emissions are expected from the ammoniator
because there is no source.
304. Emission factors for NO , SO , and VOC were transferred from
3-05-016-11. Emissions are expected to be zero.
305. SO emission factor from "Air Pollution Control Technology for Electric
Are Furnaces in the Iron and Steel Foundry Industry." EPA-450/2-78-024
(NTIS PB 283650/0), June 1978.
306. VOC emission factor was transferred from that listed for
hexamethylenediamine which was based on a stack test. Process
descriptions were reviewed in "Organic Chemical Manufacturing,
Volume 9: Selected Processes." EPA-450/3-80-028d (NTIS PB81-220584),
December 1980. Report 7. VOC process emissions for three different
ethanolamines are listed as "trace."
180
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307. NO and SO emissions are estimated to be negligible based on personal
coftmunicatfon with industry representatives. Emissions are less than
100 tons per year for NOX and SOX>
308. VOC, NO , and SO emissions are estimated to be negligible based on
persona? communication with industry representatives. Emissions are
less than 100 tons per year for these pollutants.
309. VOC and NO emissions are estimated to be negligible based on personal
communication with industry representatives. Emissions are less than
100 tons per year for VOC and NO .
A
310. VOC emissions are expected to be zero for these processes based on
technology transfer from plastics production, general (3-01-018-16).
311. NO , SO , and VOC emissions are estimated to be negligible based on
personal communication with Mr. Robert Kulp, Department of Emissions
Inventory, Harrisburg, Pennsylvania Regional Air Office. March 1987.
312. VOC emission factor for wood pallets was transferred from open burning
of vegetation. The VOC factors for fuel burning was transferred from
those listed for similar fuels burned in incinerators assuming that
combustion efficiencies are similar.
313. VOC emission factor was calculated using an average density of paint of
9 pounds/gallon and an average solvent percentage of 60 percent (these
estimates were provided by the industry). Based on technology transfer
from other surface coating operations, it was assumed that all solvent
is emitted during the process. The solvent loss was then divided out
among the different coating processes using ratios from other surface
coating operations.
314. VOC emission factor was transferred from the factors estimated for
natural gas and process gas-fired flares.
315. VOC emission factors were calculated using equations in Section 4-3 of
AP-42 Third Edition (September 1981) which separated emissions from
primary and secondary seals. The Fourth Edition of AP-42 contains a
revised Section 4-3 which does not include separate equations for
emissions from primary and secondary seals.
316. SO and NO emission factors estimated to be zero or negligible based
on engineering judgement.
317. SO emission factor estimated to be zero or negligible based on
engineering judgement.
318. NO and SO emission factors are estimated to be zero based on
information^ in "Organic Chemical Manufacturing, Volume 8: Selected
Processes." EPA-450/3-80-028c (NTIS PB81-220576), December 1980.
Report 4.
181
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319. SO and VOC emission factors are based on personal communication with
Coffee Information Institute. March 26, 1987. Negligible emissions
are expected from this physical process.
320. VOC emission factor is based on data from State files as a result of
engineering estimates (State M). Data were provided specifically for
the NH- Digester/Blow Pit/Dump Tank but should be similar for the other
digester/blow pit/dump tanks.
321. VOC emission factors were calculated using organic particulatei
information and the assumption that all total organic particulate
matter will volatilize. "Secondary Zinc Industry Emission Control
Problem Definition Study." EPA-APTD-0706. Table VII-1.
322. VOC emission factor considered negligible for pouring and casting of
zinc; transferred from lead pouring and casting (3-03-010-20 and
3-04-004-09), based on similar melting points of zinc and lead.
323. VOC emission factors were estimated from information in "Secondary Zinc
Industry Emission Control Problem Definition Study." EPA-APTD-0706,
May 1971. Tables IV-1 and IV-2. No mention of VOC in retort
operations. Zinc oxides, metal oxides, chlorides, air, and nitrogen
are listed. No VOC emissions are expected from clean metallic scrap.
324. NO , SO , and VOC emission factors considered negligible by engineering
judgement. Sodium carbonate leaching is an inorganic aqueous process
with negligible sulfur or NO present.
^
325. VOC emissions transferred from 3-04-008-71, alloying retort
distillation. No organic material present in the alloying process.
Alloying and galvanizing are similar processes.
326. VOC emission factor transferred from 3-04-008-51, retort and muffle
distillation: pouring. The distillation process produces
predominantly zinc oxide vapor. The main difference between
distillation processes is the zinc vapor cooling rate to produce zinc
slabs or zinc dust.
327. VOC emission factor transferred from similar sweating furnaces based on
engineering judgement. The emissions will be similar from all the
sweat processes for the same type of charge.
328. SO emission factor calculated from technology transfer of 3-04-002-07,
secondary copper scrap dryer, and using a 50 percent recoverable
aluminum scrap charge.
329. VOC and NO emission factor estimates are based on technology transfer
from hand-fired bituminous-coal boilers in commercial/institutional
facilities (1-03-002-14). Coal usage provided by one company operating
four plants.
182
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330. Personal communication with the Michigan Air Quality Division.
April 2, 1987. NO and SO emission factors for the dryers are based
on calculations for the use of natural gas at one plant. NO from the
presses are considered negligible due to the lack of an obvious source.
Predryers reduce moisture before pressing; therefore, VOC's are
expected to be similar to those of the dryer. VOC and NO emissions on
the bake oven are also based on natural gas use of one oven.
331. VOC emission factor was estimated using the same ratio of emissions
listed for gasoline RVP13, gasoline RVP10, and gasoline RVP7 for other
storage tanks. The emission factor for gasoline RVP7 was estimated to
be approximately half the value of the emission factor listed for
gasoline RVP13 using engineering judgement.
332. Emission factors for all five criteria pollutants were estimated using
technology transfer from other open-top vapor degreasing SCC's and
other thinning solvent SCC's.
333. SO , NO , VOC, and CO emissions are expected to be zero based on
emission factors presented for the same processes with different units
(3-04-005-05 to 3-04-005-12).
334. VOC emission factors were transferred from similar storage tanks
storing crude oil on-site at refineries (4-03-011).
335. VOC emission factor was calculated using information supplied by
Mr. C. R. DeRose, Celanese Chemical Company, Inc. Letter dated
April 21, 1978, to Mr. L. Evans, U. S. Environmental Protection Agency.
336. VOC emission factor was calculated using information provided in
Mr. J. W. Blackburn, Hydroscience, Inc. Trip Report. "Emission
Control Options for SOCMI." June 1, 1978. Prepared for U. S.
Environmental Protection Agency.
337. VOC, NO , and SO emission factors were calculated based on two tests
reportea by Mr. R. OeRosier and Mr. L. R. Water!and, Acurex Corporation.
"Environmental Assessment of a Watertube Boiler Firing a Coal-Water
Slurry, Volume I." Technical Results. Prepared for U. S.
Environmental Protection Agency. EPA-600/7-86-004a
(NTIS PB86-159845/REB), February 1986.
338. NO and SO emission factors were estimated using technology transfer
from curintj ovens in the mineral wool industry (3-05-017-04).
339. VOC emissions are estimated to be negligible because the blowing agent
is not considered a volatile organic compound using EPA's definition.
183
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340. VOC emission factors were estimated using information provided in AP-42
Fourth Edition (Section 4.2.2.7). September 1986. Based on average
percentages of emissions lost during the coating operations. The
coating contains approximately 60 percent solvent and all solvent is
evaporated during the coating process. Using engineering judgement, it
was assumed that 10 percent of the solvent evaporates during
impregnation and hot melt coating.
341. VOC, NO , and SO emission factors are estimates which were transferred
from those listed for pressed and blown glass melting furnace
(3-05-014-04). Information could not be located on ground cullet
beading furnaces in the literature, through State contacts, or through
industry contacts. This description may need updating to better
reflect the furnace type used in the industry.
342. SO , NO , and VOC emission factors based on two values from State files
(State 0). VOC emissions are reported as total hydrocarbon and may
overestimate VOC's.
343. SO , NO , and VOC emission factors based on one value from State files
(State 0). VOC emissions are reported as total hydrocarbons and may
overestimate VOC's.
344. SO emission factor based on one value, NO emission factor on four
vatues, and VOC emission factor on two values from State files
(State D). VOC emissions are reported as total hydrocarbon and may
overestimate VOC's.
345. SO emission factor based on two values, NO emission factor on six
vafues, and VOC emission factor on five values from State files
(State 0). VOC's are reported as total hydrocarbon and may
overestimate VOC's.
346. VOC emission factor is calculated from data given in "Locating and
Estimating Air Emission from Sources of Vinylidene Chloride."
EPA-450/4-84-007k, (NTIS PB86-117611/REB), September 1985. The numbers
are for a hypothetical plant and a continuous operation is assumed.
347. SOV emission factor based on two values from State files (States C and
D)?
348. VOC emission factors for SCC's 4-02-010-02 through 4-02-010-05 are
based on percentages of solvent loss for each operation in the fabric
surface coating industry and from process descriptions in "Automobile
and Light-Duty Truck Surface Coating Operations - Background
Information for Proposed Standards." EPA-450/3-79-030,
(NTIS PB80-123540), September 1979. The coating application estimates
are derived from AP-42 data, assuming a ratio of four automobiles to
every truck produced. Repair topcoat application is expected to
produce fewer VOC's; an estimate of 10 percent is assigned. These are
to be used only in the absence of better information.
184
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349. VOC emission factors calculated from ratios given in AP-42 data. Two-
and three-piece can manufacturing are considered separately. Process
description taken from "Control of Volatile Organic Emissions from
Existing Stationary Sources, Volume II: Surface Coating of Cans,
Coils, Papers, Fabrics, Automobiles, and Light-Duty Trucks," Guidance
Series. EPA-450/2-77-008 (NTIS PB 272445/8), May 1977. Overvarnish
(4-02-017-28) emissions are expected to be lower than metal coating and
are estimated at 10 percent of total solvent loss. These are to be
used only in the absence of better information.
350. VOC emission factor transferred from sulfuric acid production based on
engineering judgement.
351. VOC and NO emissions are expected to be negligible based on the
process description provided by the Michigan Department of Natural
Resources. April 8, 1987. The heat source is assumed to be steam.
352. SO emission factor transferred from siliconmanganese electric smelting
fuPnace due to process similarities.
353. SO , NO , and VOC emission factors transferred from a similar process
in the gray iron foundry industry.
354. VOC emission factor transferred from 50 percent ferrosilicon electric
smelting furnace due to similarities in the furnace and charge
composition.
355. VOC emission factor transferred from ferromanganese blast furnace due
to similarities in charge composition.
356. VOC emission factor transferred from a similar process in the sintering
industry.
357. SO , NO , and VOC emission factors transferred from by-product coke
manufacturing oven/door leaks by engineering judgement.
358. VOC, SO , and NO emission factors transferred from a similar process
in the mineral products industry.
359. NO emission factor transferred from secondary aluminum
roTling/drawing/extruding due to similarities in metal treatment.
360. NO emission factor transferred from electric arc furnace in the steel
inaustry due to process similarities.
361. VOC emission factor transferred from a similar process in the primary
copper industry.
362. SO , NO , and VOC emission factors transferred from a similar process
in the primary copper industry.
185
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363. SO , NO , and VOC emission factors transferred from a similar process
in the secondary aluminum industry.
364. SO and VOC emission factor transferred from a similar process in the
gray iron foundry industry.
365. SO , NO , and VOC emission factor transferred from similar process in
otfier metals industries. Pickling/neutralizing emission factors were
transferred from the primary steel industry and EAF with carbon
electrode emission factors were transferred from the primary aluminum
prebaked reduction cell due to process and metal similarities.
366. VOC emission factor transferred from pulverized bituminous coal due to
similarities in flue gas.
367. VOC emission factor transferred from anode baking furnace by
engineering judgement. It is assumed that the VOC's driven off in the
anode baking furnace are primarily those evolved during the use of a
Soderberg cell. It was also assumed that all the cell binder
volatilized. VOC emission factor for the prebaked reduction cell was
estimated assuming that 10 percent of the emissions from a Soderberg
cell would be emitted in the prebaked cell during normal operating
conditions (engineering judgement).
368. VOC emission factors were transferred from similar operations in other
chemical manufacturing industries.
369. VOC emission factor for gas stripping is calculated from data on a
typical gas plant presented in "Equipment Leaks of VOC in Natural Gas
Production Industry - Background Information for Proposed Standards."
Draft EIS. EPA-450/3-02-024a (NTIS PB84-155126/REB), December 1983.
In the absence of an SCC for gas plants and an identification for gas
stripping, gas plant operations as a whole are assumed. The VOC
emission factor for gas lifts was transferred from that listed for
compressors due to process similarities.
370. VOC emissions for asphalt melting kettle are assumed negligible because
the process requires melting at low temperatures (less than 45Q°F) and
decomposition or volatilization is not expected. If solvents are used,
then VOC's will result from solvent evaporation. VOC emission factors
for dipping, spinning, and wrapping are based on coal tar epoxy use and
associated solvent loss. Coal tar epoxies may be sprayed and require
no heat use. The units of lbs/10 square feet are for 3 7 mm thick
coating.
371. NO and SO emission factors transferred from factors listed for hot
buPning fufnaces in the metals industry.
372. VOC emission factors are estimates based on a review of the process
descriptions provided in "SOCMI Reactor Processes - Background
Information for Proposed Standards." Draft EIS. October 1984. These
factors were transferred from similar processes in the organic chemical
manufacturing industry as best estimates.
186
-------
373. VOC emission factor for process gas-cogeneration was transferred from
petroleum refining gas as a best estimate. VOC emission factor for
process gas-reciprocating was transferred from natural
gas-reciprocating due to similarities in the gas composition.
374. Emission factors for all five pollutants were provided by the State of
Minnesota, when they requested that this SCC be added to NEDS.
187
-------
-------
APPENDIX B
FOOTNOTES FROM ORIGINAL NEDS DOCUMENTS
aBoth boiler capacities and throughputs must be reported to NEDS for all
boilers.
This emission factor is an approximation. Particulate emissions from
residual oil combustion can be more accurately estimated from the equation
lb/1000 gallon - 10S + 3. See AP-42, page 1.3-2.
cThe emission factor(s) are non-standard. The factor(s) are derived from
AP-42 data for another similar source category.
The emission factor(s) are not from AP-42. The factor(s) are from other EPA
documents, State data, or other miscellaneous sources.
eThis emission factor is an approximation. Particulate emissions from waste
oil combustion can be more accurately estimated by the factor 75A, where A =•
weight (%) percent of ash in the waste oil. See AP-42, page 1.11-1.
Fugitive emissions occur from numerous locations within industrial facilities,
as of 1978, most of these sources have not been fully characterized. To
allow these fugitive sources to be represented in NEOS, common SCC codes
have been developed. These codes should be used in addition to the main
process SCC codes associated with the facility. Specific fugitive emissions
that have been characterized are also contained in this table.
gThese emission factors are from an earlier edition of AP-42. This is an
obsolete process. The last channel black plant in the U.S. closed in 1976.
These emission factors are from an earlier edition of AP-42. This is an
obsolete process. The gas furnace process 1s being phased out in the U.S.
Manufacture of inorganic pigments 1s classified under SCC 3-01-035-**.
JFor molded and fabricated rubber and plastics products, see SCC 3-08-***-***,
3-30-002-**, and 4-02-002-**.
L,
This emission factor Is an assumed average value from a range of values
given in AP-42, Table 5.17-2.
Also applies to the sulfur recovery plant at petroleum refineries and
natural gas production fields.
mSee 3-01-301-** for other chlorobenzene process codes.
nGrain processing and milling are Included 1n SCC's 3-02-007-** thru
3-02-008-**. For grain elevators, see SCC 3-02-005-**, 3-02-006-**, and
3-02-031-**.
°Units refer to amount of grain processed through each operation. If only the
total amount of grain received or shipped is known, see AP-42, Table 6.4-2
for typical ratios of tons processed to tons shipped or received.
189
-------
pThe participate emission factor is on emissions at the inlet to the baghouse
or other control device. Indicate the control device and efficiency to
properly estimate the actual emissions.
qCodes 3-03-003-09, -10, and -11 represent individual operations within this
SCC (3-03-003-07).
rThese emission factors are from an earlier edition of AP-42. The current
version of AP-42, Fourth Edition, no longer reports emission factor(s) for
this process.
3This emission factor is a weighted average of values given in AP-42,
Table 7.3-2.
Represents total CO generated, report control equipment as 022 for CO boiler
or 060 for process gas .recovery to properly account for actual emissions.
"Represents total CO generated, report control equipment as 022 for CO boiler
or 023 for flaring to properly account for actual emissions.
vThese emission factors are derived from AP-42 data. A units adjustment has
been made to the AP-42 data. See AP-42, Table 7.6-1.
wApply for all metallic minerals except as noted. Low moisture ore 1s
defined as having less than 4 percent moisture content by weight for ore
entering the primary crusher. High moisture ore has over 4 percent by
weight.
xEmission factor does not apply to bauxite ore.
yEmission factor does not apply to drying of titanium/zirconium sands. See
SCC 3-03-012-** for titanium processing.
Calculated from emission factors given 1n Table 7.9-2, Footnotes b-e.
aaThis emission factor is an approximation. To more accurately estimate SO.
emissions, use the factor 1.25S, where S - weight (%) percent of sulfur in
the coke. See AP-42, Table 7.10-1.
This emission factor 1s an approximation. To more accurately estimate SO,
emissions, use the factor .292 S, where S » weight (X) percent of sulfur Tn
the fuel. See AP-42, Table 8.1-1.
ccThis emission factor 1s from an earlier edition of AP-42. Currently, AP-42,
Fourth Edition calculates an emission factor in a different manner. See
AP-42, Section 11.2.3.
Use kiln code and appropriate 3-90 code for fuel used in kilns to properly
account for all SOX emissions.
eeThese SCC codes are also applicable to Coal Cleaning Operations at power
plants.
ffThis emission factor 1s from an earlier version of AP-42. See AP-42,
Table 8.14-1.
190
-------
^Expressed as emission rate at point of release. For uncontrolled sources,
to account for emissions that settle out within the plant, code a fictitious
control device code for particulate of 006 (low efficiency gravitational
collector) with appropriate control efficiency. See AP-42, Section 8.2.0
for table of typical control efficiencies for gravitational settling.
Several processes that routinely occur in Major Group 29 can be found under
other major groups. Specifically, note the following:
- waste of process gas and/or liquid fired boilers - SCC 1-02-***-**.
- internal combustion compressor engines - SCC 2-02-***-**.
- amine sweeting process - SCC 3-10-002-**.
- sulfur recovery process - SCC 3-01-032-**.
- sulfuric acid plant - SCC 3-01-022-** or 3-01-023-**.
11 Represents total CO and VOC generated. Report control device as 022 if CO
boiler is present to properly account for actual emissions.
JJUnits expressed as the equivalent number of valves, seals, flanges, or
drains in the refinery on an annual operating basis (8,760 hours/year).
For example, if there are 1,000 seals, all operating 8,760 hours/year, then
operating rate « 1,000. However, if the average operating time is
6,570 hours/year (3/4 of the total hours in a year), then operating rate -
1,000 x (6,570, 8,760) • 750 seals. All counts of valves, seals, flanges,
and drains should be similarly adjusted to account for the average annual
hours of operation in the refinery.
kk
Process changes may include such measures as raising the pH of the cooking
liquor, thereby lowering the free SO-, relieving the pressure in the
digester before the contents are discharged, and pumping out the digester
contents instead of blowing them out.
The emission factor is non-standard. The factor is derived from AP-42 by a
units conversion. See AP-42, Section 10.4.
mmFor Surface Coating Operations, see SCC 4-02-019-** and 4-02-021-**.
nnFor tire retreading operations, see SCC 3-08-005-**.
°°The sulfur content of the fuel as H-S on a mole percent basis.
ppFor specific printing SCCs, see SCC 4-05-***-**.
^In-process fuel codes must always be used in conjunction with the
appropriate process code.
rrThis emission factor 1s non-standard. The factor 1s derived from AP-42 and
Bureau of Mines data. See AP-42, Section 8.6.
SSA table of typical solvent densities can be found 1n Section 3, Chapter 16
of AEROS Volume V.
These solvents are estimated to be of negligible photochemical reactivity.
uuUse these SCCs to provide a rough estimate of emissions only when information
on the identity and/or quantity of make-up solvent used is not available.
191
-------
vvThese are general SCCs applicable to all Industrial categories.
emission factor is non-standard. The factor is derived from average
coating density data in AP-42, Section 4.2.2.
xxThese solvents are used to thin coatings and thus should be used with one
of the coating codes.
yyThis SCC should only be used to provide rough estimates of emissions for
cases when information on amount of fabric processed is not available.
zzFor surface coating of small appliances, see SCC 4-02-025-**, surface
coating of miscellaneous metal parts.
aaalncludes Major Group 34 fabricated metal products, Major Group 35 small
appliances, and other coating operations Major Group 33-39 not specified
elsewhere.
The VOC emission factors are non-standard. The emission factors are
derived from Information found 1n AP-42, Section 4.3.
cccBulk terminals are defined as facilities with dally throughputs of
20,000 gallons or more.
dddBulk plants are defined as facilities with dally throughputs of
20,000 gallons or less.
eeeThese solvents are often added by the user to the inks used in printing
processes. Thus, the solvent SCC's should not be used alone, but rather
in conjunction with a printing process SCC.
These organic chemicals are designated in this listing by their trade
names. The following 11st Indicates the trade name and its corresponding
chemical name:
Trade Name Chemical Name
Butyl Carbltol 01 ethyl ene Glycol Monobutyl Ether
Butyl Cellosolve Ethyl ene Glycol Monobutyl Ether
Carbltol 01 ethyl ene Glycol Monoethyl Ether
Methyl Carbltol D1 ethyl ene Glycol Monomethyl Ether
Methyl Cellosolve Ethyl ene Glycol Monoethyl Ether
192
-------
APPENDIX C
SUMMARY TABLES OF STATE'S SUBMITTALS TO NEDS
REQUIRING EMISSION FACTOR DEVELOPMENT
The following tables present the SCC's for which State's have submitted
emissions information to NEDS and emission factor development is needed.
Reports were received which required emission factor development for
293 SCC's. Of the 293 SCC's, 179 are considered legitimate source
categories for which emission factors are appropriate. These SCC's are
presented in Table C-l. For the remaining 114 SCC's, emission factor
development is not appropriate because they are general categories which do
not represent a specific process or vent. These SCC's are presented in
Table C-2.
193
-------
TABLE C-l. EMISSION FACTOR DEVELOPMENT FROM
STATE QUICK LOOK REPORTS
sec
PROC. INSCRIPTION
vac
NOX
SOX
STATE
10201201
10201301
10201302
10301201
30101304
30101501
30101502
30101503
30101505
30101703
30101704
30101832
30102301
30102308
30102321
30102401
30103002
30103021
30103102
30103103
30103104
30103105
30103201
30103202
30103204
30103551
30103553
30112510
30112520
30112701
30187009
30187010
30200202
30200203
30201301
30201601
30201911
30202601
30203601
30300101
30300104
30300306
30300503
30300504
30300507
30300604
30300814
30300817
30300904
30300908
30300911
30300922
30300932
30302316
BOILER, SOLID WASTE
BOILER, LIQUID WASTE
BOILER, WASTE OIL
BOILER, SOLID WASTE
NITRIC ACID-CONCENTRATION
VARNISH MNF. BODYING OIL
VARNISH MNF. OLEORESIN
VARNISH MNF. ALKYD
VARNISH MNF. ACRYLIC
PHOSPHORIC ACID, ABSORBER
PHOSPHORIC ACID, VENTURI SCR.
PLASTICS, UREA-FORMAL. RESIN
SULFURIC ACID, ABSORBER
SULFURIC ACID, ABSORBER
SULFURIC ACID, STOR. TANK VNT
SYN. ORGANIC FIBER, POLYAMIDE
AMM. PHOSPHATE, AMMONIATOR, GR
AMMONIUM PHOSPHATE-DEN
TEREPHTHALIC ACID, REACT. VENT
TEREPHTH. ACID-CRYSTALL.
TEREPHTH. ACID-DISTILLATION
TEREPHTH. ACID-TRANSFER VENT
ELEM. SULFUR - MOD. CLAUS
ELEM. SULFUR PROD. MOD. CLAUS
ELEM. SULFUR (REM PROC.)
INORGANIC PIGMENT ORE DRYER
INORGANIC PIGMENT, DRYER
CHLORMETHANES- GENL.
PERCH. PROD. GENL.
FLUOROCARBONS-GENL.
INORGAN. STQR., SULFURIC ACID
INOR6AN. STOR., SULFURIC ACID
COFFEE ROAST. IND. FIRED ROAST
COFFEE ROAST. STONER/COOL
MEAT SMOKEHOUSE
SUGAR BEET PROC. DRYER
VEGETABLE OIL PROD. -OIL EXTR.
SEED PROD.
DEEP FAT FRYING, VATS
ALUM. ORE, PREBAKED RED. CELL
ALUM. ORE ELECTRO-RED. HAND.
COKE MNF. OVEN UNDERFIRING
COPPER SMELT. REV. FURNACE
COPPER SMELT. CONVERTER
COPPER SMELT. FURNACE
FERROALLOY-ELECT SMLT FURN
SINTER, DISCHARGE END
SINTER, COOLER
STEEL PROD. ELECT ARC FURN
STEEL PROD. EAF (CARBON ST)
STEEL PROD. SOAKING PITS
STEEL PROD. CONT. CASTING
STEEL PROD. MACHINE SCARFING
TACONITE ORE PELLET TRANSF.
2
1
1
2
0
40
150
160
20
NEG
NEG
20
0
0
-
-
NEG
NEG
30
3
2
3
3
2
2
0
0
30
3
17
-
-
2
NEG
-
0
17
NEG
18
0
0
-
0.0
NEG
0
72
0
NEG
0.
0.
0
-
NEG
0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.8
.2
.6
.0
.1
. 1
.0
.0
.0
.5
.1
.6
.2
.0
.5
. 1
.0
15
.0
.0
.0
35
35
.6
.0
5.9
23.0
60.0
5.9
-
NEG
NEG
NEG
NEG
NEG
NEG
X
0.004
0.004
-
NEG
NEG
NEG
0.0
0.0
0.0
0.0
0.35
0. 1
O.I
0.0
0.0
0.0
0.0
0.0
0.0
0.0
-
-
0.7
0.06
NEG
NEG
NEG
0.003
-
0.0
5.8
0.0
10.3
0.1
NEG
NEG
O.I
-
NEG
0.05
NEG
0.0
1
28
130
-
-
0
0
0
0
0
0
0
4
27
0
NEG
0
NEG
0
0
0
0
280
189
4
0
0
NEG
0
0
-
-
0
NEG
0
0.
NEG
NEG
NEG
-
-
-
173
623
320
0.
NEG
0.
0
0
NEG
-
NEG
0
.6
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
. 1
.3
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.0
.4
. 1
41
.0
.0
.0
07
14
.7
.7
.0 '
NC
CT
cr
NC
MO
MI
MI
MI,KS,MN
MI.KS
NC
NC
MO, OR
NC
NC
MO
TN
KS
NC
NC
NC
NC
NC
DE
MI,MN
MN
MN
MN
KS
KS
MN
MO
MO
KS
KS
KS,MN
OR
KS
KS
MN
OR
MO
MO
MI
MI
MI
WV
IN
IN
WV
CO
CT
CO
IN, MO
MN
194
-------
TABLE C-l. EMISSION FACTOR DEVELOPMENT FROM
STATE QUICK LOOK REPORTS (Continued)
sec
C'OC. DESCRIPTION
VQC
NDX
SOX
STATE
30400103
30400104
30400109
30400112
30400208
30400224
30400239
30400301
30400303
30400315
30400320
30400325
30400331
30400332
30400333
30400341
30400342
30400350
30400351
30400352
30400353
30400355
30400356
30400357
30400358
30400370
30400371
30400403
30400704
30400708
30400716
30400803
30400805
30402201
30402210
30500203
30500204
30500206
30500208
30500301
30500501
30500504
30500606
30500802
30500803
30501101
30501410
30501414
30501501
30501502
30501512
30501603
30501604
30501609
ALUMINUM SMELT. FURNACE
SEC. ALUMINUM-FLUXING
SEC. ALUM. BURN/DRYING
SEC. ALUM. ANNEALING FURN.
SEC. COPPER SMELT. WIRE BURN.
EIF CHARGE W/ BRASS & BRONZE
FUGITIVE CASTING OPER.
6RAV IRON FOUND. CUPOLA
GRAY IRON FOUND. EIF
GRAY IRON FOUND., CHARGE HAND.
GRAY IRON FOUND. POUR/CAST
GRAY IRON FOUND., CAST COOLING
BRAY IRON FOUND. CAST SHAKEOUT
GRAY IRON FOUND. CAST KNOCKOUT
GRAY IRON FOUND. SHAKEOUT MAC.
GRAY IRON FOUND. CAST. CLEANIN
GRAY IRON FOUND. CAST. CLEANIN
GRAY IRON FOUND., SAND GRIND/H
GRAY IRON FOUND., CORE OVEN
GRAY IRON FOUND. SAND GRIND/HA
GRAY IRON FOUND. CORE OVENS
GRAY IRON FOUND. SAND DRYER
GRAY IRON FOUND. SAND SILO
GRAY IRON FOUND. CONVEYERS
GRAY IRON FOUND. SAND SCREENS
GRAY IRON FOUND. SHELL CORE MA
GRAY IRON FOUND. CORE MACH.
SEC. LEAD SMELT. CUPOLA
STEEL FOUND. -HEAT TREAT FURN.
STEEL FOUND. -POUR/CAST
STEEL FOUND. -SAND GRIND.
SEC. ZINC, POT FURNACE
SEC ZINC GALVANIZ. KETTLE
METAL HEAT TREAT. FURNACE
METAL HEAT TREAT. -QUENCH BATH
ASPHALTIC CONCRETE STOR. PILES
ASPHALTIC CON. COLD A6G. HAND
ASPHALT HEATER, NATL. GAS
ASPHALT HEATER, DIST. OIL
BRICK MAN. RAM MAT. DRYING
CASTABLE REFRACTORY, DRYER
CASTABLE REFRACTORY, OVEN
CEMENT MNF. KILNS
CERAMIC CLAY MNF., GRINDING
CERAMIC CLAY MNF. STORAGE
CONCRETE BATCHING-GENL
GLASS MNF. RAM MAT. HANDL.
GLASS MNF. BEADING FURN.
GYPSUM, ROTARY ORE DRYER
GYPSUM, GRINDER/ROLLER MILL
GYPSUM, FLASH CALCINER
LIME MNF. CALCINER-VERT. KILN
LIME MNF. CALCINER-ROTARY KLN
LIME MNF. HYDRATOR
5.2
0.0
32.0
0.004
0.6
NEG
0.0
0.18
NEG
NEG
0.14
NEG
1.2
1.2
1.2
0.0
0.0
6.0
0.0008
0.0
0.0008
0.0
0.0
0.0
0.0
0.0008
0.0008
NEG
1.1
0.14
0.0
2.4
0.0
0.1
280.0
NEG
0.13
-
0.2
0.004
0.004
1.0
0.02
0.0
0.0
0.0
0.0
0.3
0.004
0.0
0.02
0.02
0.06
0.0
0.76
-
0.5
1.5
1.7
NEG
0.0
-
NEG
NEG
0.01
NEG
0.0
0.0
0.0
0.0
0.0
0.0
0.5
0.0
0.5
1.6
0.0
0.0
0.0
0.5
0.5
O.t
80.0
0.01
0.0
1.9
0.4
4.0
NEG
-
0.0
140.0
20.0
-
1.6
0.016
-
-
-
0.0
-
8.5
1.6
0.0
2.8
2.8
-
-
-
-
3.0
0,002
12.8
0.03
0.0
-
0.03
NEG
0.02
NEG
0.0
0.0
0.0
0.0
0.0
0.0
0.32
0.0
0.32
0.0
0.0
0.0
0.0
0.32
0.32
-
280.0
0.02
0.0
0.002
0.002
0.002
NEG
-
0.12
0.6
144.0
0.002
0.002
0.0
-
-
-
-
0.0
5.6
0.002
0.0
8.2
8.2
6.4
-
MI.AL
MO
MN
MN
KS,MO
MI,KS,MN
KS,MN
MI, MO
GA,MI,KS
MN
MI,KS,MN
MN
MN
MI.MN
MI
MI
MI
GA,MI,KS
IA,KS,IA
MN
MN
MI
MI
MI
MI
MI
MI
OR
KS,MN
KS
KS
MI
MO,WV
MN
KS,MN
MO
MN
CO
CO,SC,AL
MI, MO
GA
3A
OR
MO
MO
KS
KS
MN
MI
MI
MI
MI
MI,MT
MN
195
-------
TAitE C-l. EMISSION FACTOR DEVELOPMENT FROM
STATE QUICK LOOK REPORTS (Continued)
sec
PRQC. DESCRIPTION
VOC
NOX
SOX
STATE
30501617
30501901
30501905
30502012
30502106
30502509
30502510
30700101
30700102
30700103
30700104
30700105
30700106
30700107
30700109
30700110
30700501
30700705
30700706
30700707
30700708
30700709
30700802
30700803
30800501
30800701
30800702
30890002
30890003
30900303
30900304
30901001
30901101
30901102
30901104
30901604
30902501
30904001
31000202
31307002
31401101
31401102
40200501
40200701
40200710
40200801
40200810
40301117
40301118
40301153
40400413
40400414
40500101
40700809
LIME MNF. MULT. HEARTH CALCINE
PHOSPHATE ROCK DRYING
PHOSPHATE ROCK CALCINING
STONE QUARRYING- DRYING
SALT MINING, CONVEYING
SAND/GRAVEL-COOLER
SAND/GRAVEL-CRUSHING
PULPING, DIGESTER
PULPING, WASHERS/SCREENS
PULPING, EVAPORATOR
PULPING, RECOVERY FURN.
PULPING, SMELT DISSOLVING TANK
PULPING, LIME KILN
PULPING, TURPENTINE CQNDENSOR
PULPINQ-LIQUOR QXID, TOWER
PULPING, RECOVERY FURNACE
WOOD PRESSURE TREAT-CREOSOTE
PLYWOOD, COE DRYER
PLYWOOD, PRE-DRYER
PLYWOOD, PRESSING
PLYWOOD, TEMPERING
PLYWOOD, BAKE OVEN
SAWMILL OPER. LOG SAWING
SAWMILL, SAWDUST PILE HAND
TIRE RETREAD, BUFFING MACH.
FAB. PLASTICS-MACHINING
FAB. PLASTICS, MOLD RELEASE
PROCESS HEATER-RES. OIL
PROCESS HEATER-NATL.GAS
ABRAS. CLEAN. METAL POLISHING
ABRAS. CLEAN. METAL BUFFIN8
ELECTROPLATIN6-GENL.
CONV. COAT METAL-ALK. CLEAN. B
CLEAN. METAL PARTS-PICKLING
CONV. COATING METAL-RINSING
METAL PIPE COATING, COAL TAR
DRUM CLEAN. FURNACE
METAL DEP PROC. -METALLIZING
NATL. GAS PROD. -GAS STRIPPING
ELECT. WINDINGS REC.
AUTO BODY SHREDDING
AUTO BODY SHREDDING
SURFACE COATING, ENAMEL
COATING ADHESIVES APPLIC.
COATIN6-ADHESIVES
COATING OVEN, 6ENL.
COATING OVEN-GENL
STORAGE, CRUDE OIL
STORAGE, JET NAPTHA
STORAGE, JET NAPTHA
UNDERGROUND STOR. DIS. FUEL
UNDERGROUND STOR. DIS. FUEL
PRINTING/PUB. -DRYERS
STORAGE, ETHYL ALCOHOL
0.02
0.004
0.0
0.0
0.0
0.0
0.0
0.0
0.2
0.0
1.95
0.16
0.25
0.07
0.43
0.8
NE8
1.0
1.0
1.45
NE6
0.003
NEG
NE6
600.0
13.0
NEG
0.28
2.8
NEG
NEG
0.026
0.0
0.0
100.0
NEG
0.002
340.0
-
190.0
NEG
NEG
-
900.0
4.4
800
42
0.007
0.056
31.0
NEG
NEB
2000.0
2.9
2.G
1.6
0.0
0.0
0.0
0.0
0.0
0.0
0.0
0.0
-
2.9
-
-
0.0
2.0
-
0.3
0.3
NEG
NEG
0.1
0.0
0.0
NEG
NES
0.0
55.0
140.0
NEG
NEG
0.009
0.3
13.0
8.0
X
-
-
X
0.1
NEG
NES
0.0
-
-
54
13
-
-
-
-
-
32.0
-
8.2
0.002
0.0
0.0
0.0
0.0
0.0
0.0
0.01
0.01
-
0.1
-
-
0.02
1.5
-
NEG
NEG
0.0
0.0
0.0
0.0
0.0
NEG
NEG
0.0
159.0
0.6
NEG
NEG
0.0
NEG
0.6
NEG
X
0.002
-
310
2.5
NEG
NEG
0,0
-
-
5
1
-
-
-
-
-
150
-
MI
NC
NC
KS
MI
MI
MI
MI,MN,NC
MI,MN
MI,MN,NC
MI,AL,OR,NC
MI,MN,AL,NC
MI,AL,OR,NC
MI
NC
QR,NC
MN
MI
MI
MI
MI
MI
KS
MI,KS,MN
KS
NC
MI
NC
NC
MI
MI
MN
MN
MI.MN
MN
KS
KS
MN
NM
NC
KS
KS
RI
MN
MN
TN,KS,MN,NC
MN
MI
MI
MN
MO
MO
NC
MN
196
-------
TABLE C-l. EMISSION FACTOR DEVELOPMENT FROM
STATE QUICK LOOK REPORTS (Continued)
sec
PROC. DESCRIPTION
VQC
NOX
SOX
STATE
40700810
40701605
40701606
40701611
40701612
40701613
40701614
40703613
40703614
40705204
40705207
40705208
40706019
40706020
40722801
40722802
40784801
STORAGE
STORAGE
STORAGE
STORAGE
STORAGE
STORAGE
STORAGE
STORAGE
STORAGE
STORAGE
STORAGE
STORAGE
STORAGE
STORAGE
STORAGE
STORAGE
STORAGE
, ETHLY ALCOHOL
.N-HEPTANE
, N-HEPTANE
, NAPTHA
, NAPTHA
, PET. DISTILLATE
, PET. DISTILLATE
, STYRENE
, STYRENE
, BUTYL CELLOSOLVE
, CELLOSOLVE
, CELLOSOLVE
, METHYLENE CHLOR.
, METHYLENE CHLOR.
, ACETONE
, ACETONE
, ETHYLENE OXIDE
0.66
5.8
1.3
0.15
0.006
0.15
0.006
1.5
0.17
0.03
).0036
0.16
0.0
0.0
2.2
0.002
0.0
MN
IN
IN
IN
IN
IN
IN
UN
MN
IN
IN
IN
IN
IN
IN
IN
MO
197
-------
TABLE C-2. SCC's FROM QUICK LOOK REPORTS FOR WHICH EMISSION
FACTOR DEVELOPMENT WAS NOT APPROPRIATE
STATE
SCC
PROC. DESCRIPTION
VOC
NOX
SOX
AL
AL
AL
AZ
CO
CT
CT
DE
GA
GA
GA
IA
IA
IN
IN
IN
IN
IN
IN
IN
IN
IN
KS
KS
KS
KS
KS
KS
KS
KS
KS
KS
KS
KS
KS
KS
KS
KS
KS
KS
KS
10200799
30199999
30699999
20100401
30609903
30106099
30799999
10200799
30400399
30700701
30702099
30999999
40399999
30102699
40700897
40700898
40701697
40701698
40703697
40703698
40705297
40705298
30100799
30101199
30103099
30112599
30188801
30199999
30299998
30299999
30400199
30405001
30700401
30700898
30703098
30703099
30800799
31000299
40200998
40301097
40301099
BOILER, PROCESS GAS - OTHER
CHEM. MANF. - NEC
NO SCC IN LISTING
NO SCC IN LISTING
NO SCC IN LISTING
PHARMACEUTICALS - NEC
WOOD PRODUCTS - NEC
BOILER, PROCESS GAS-OTHER
GRAY IRON FOUND. - NEC
PLYWOOD MANF. GENL. - NEC
FURNITURE MANF. - NEC
FABRICATED METALS-NEC
NO SCC IN LISTING
SYNTHETIC RUBBER PROD. - NEC
STORAGE-SPECIFY ALCOHOL
STORAGE-SPECIFY ALCOHOL
STORAGE-SPECIFY ALKANE
STORAGE-SPECIFY ALKANE
STORAGE-SPECIFY AROMATIC
STORAGE-SPECIFY AROMATIC
STORAGE-SPEC. GLYCOL ETHER
STORAGE-SPEC. GLYCOL ETHER
INORGANIC CHEM., CHLORINE-NEC
HYDROCHLORIC ACID - NEC
AMMONIUM PHOSPHATE - NEC
CHLORINE ORQANICS- NEC
CHEM MNF. FUGITIVES-SPEC. PROC
CHEM. MANF. - NEC
FOOD fc A6. NEC-SPEC. PROC.
FOOD (c AG. NEC-SPEC. PROC.
NO SCC IN LISTING
MISC. CAST b FABRICATINB-NEC
POULPBOARD OPERATIONS- GENL.
SAWMILL OPER. - NEC
WOODWORKING QPER. SPEC. IN COM
WOODWORKIN6 OPER. SPEC. IN COM
FAB. PLASTICS PROD. - NEC
NATURAL GAS PROD. - NEC
THINNING SOLVENTS - NEC
STORAGE-SPECIFY LIQUID
STORAGE-SPECIFY LIQUID
X
X
X
X
X
X
X
X
X
-
X
X
X
-
X
X
X
X
X
X
X
X
X
X
X
X
X
X
X
X
X
X
X
X
X
X
X
X
X
X
X
-
X
X
X
X
X
X
X
X
X
X
X
-
X
-
-
-
-
-
-
-
-
X
X
X
X
X
X
X
X
X
X
X
X
X
X
X
X
-
-
-
-
X
-
X
-
X
X
-
X
X
X
X
-
X
-
-
-
-
-
-
-
-
X
X
X
X
X
X
X
X
X
X
X
X
X
X
X
X
-
-
-
**NEC * PROCESS NOT ELSEWHERE CLASSIFIED
198
-------
TABLE C-2. SCC's FROM QUICK LOOK REPORTS FOR WHICH EMISSION
FACTOR DEVELOPMENT WAS NOT APPROPRIATE (Continued)
STATE
KS
MI
MI
MI
MI
MI
MI
MI
MI
MI
MI
MI
MI
MI
MI
MI
MI
MI
MI
MI
MI
MI
MI
MI
MI
MI
MI
MI
MI
MI
MI
MI
MI
MI
MI
MI
MI
MN
MN
MN
MN
MN
MN
MN
MN
MN
MN
sec
40301299
30101499
30101599
30102099
30199999
30200799
30299998
30300599
30400199
30400204
30400299
30400399
30400499
30400899
30700799
30799999
30800799
30901098
30903099
30999999
31000199
31000299
39999995
39999999
40100296
40100297
40100398
40299998
40301097
40301099
40301197
40301299
40399999
40600197
40600198
40799998
50300701
30101899
30103599
30187097
30187098
30188801
30188802
30199998
30203099
30288801
30299998
PROC. DESCRIPTION
STOR.-VAR. VAPOR SP.-SPEC. LIQ
PAINT MANF. - NEC
VARNISH MANF. - NEC
PRINTING INK MANF. - NEC
CHEM. MANF. - NEC
NO SCC LISTED
FOOD & A6. NEC-SPEC. PROC.
COPPER SMELT. -NEC
NO SCC IN LISTING
NO SCC IN LISTING
SEC. COPPER SMELT, FUG. NEC
GRAY IRON FOUND. - NEC
SEC. LEAD SMELT. - NEC
SEC. ZINC PROD. - NEC
PLYWOOD - NEC
WOOD PRODUCTS - NEC
FAB. PLASTICS PROD. - NEC
ELECTROPLATING OPER. - NEC
NO SCC IN LISTING
FABRICATED METALS-NEC
CRUDE OIL PROD. - NEC
NATURAL GAS PROD. - NEC
MISC INDUSTRIAL PROC. - NEC
MISC INDUSTRIAL PROC. - NEC
NO SCC IN LISTING
NO SCC IN LISTING
COLD SOLVENT CLEAN. - NEC
MISC. ORG SOLVENT EVAP. - NEC
STORAGE-SPECIFY LIQUID
STORAGE-SPECIFY LIQUID
STORAGE-SPECIFY LIQUID
STOR.-VAR. VAPOR SP.-SPEC. LIQ
NO SCC IN LISTING
NO SCC IN LISTING
NO SCC IN LISTING
NO SCC IN LISTING
INCINERATOR, LIQUID WASTE
PLASTICS PRODUCTION - NEC
INORGANIC PIGMENTS - NEC
INORGANIC STOR, SPEC. LIQUID
INORGANIC STOR. SPEC. LIQUID
CHEM MNF. FUGITIVES-SPEC. PROC
CHEM MNF. FUGITIVES-SPEC. PROC
CHEM MANF. SPEC. IN COMM.
DAIRY PROD. SPEC. IN COMM.
FOOD * AG. FUG. -SPEC. PROC.
FOOD d AG. NEC-SPEC. PROC.
VOC
X
X
X
X
X
X
X
X
X
X
X
X
X
X
X
X
X
X
X
X
X
X
X
X
X
X
X
X
X
X
X
X
X
X
X
X
X
X
X
X
X
X
X
X
X
X
X
NOX
-
X
X
X
X
X
X
X
X
X
X
X
X
X
X
X
X
X
X
X
X
X
X
X
-
-
X
-
-
-
-
-
-
-
-
-
X
X
X
X
X
X
-
X
X
X
X
SOX
-
X
X
X
X
X
X
X
X
X
X
X
X
X
X
X
X
X
X
X
X
X
X
X
-
-
X
-
-
-
-
-
-
-
-
-
—
X
X
X
X
X
-
X
X
X
X
««NEC = PROCESS NOT ELSEWHERE CLASSIFIED
199
-------
TABLE C-2. SCC's FROM QUICK LOOK REPORTS FOR WHICH EMISSION
FACTOR DEVELOPMENT WAS NOT APPROPRIATE (Continued)
STATE
MN
MN
UN
MN
MN
MN
MN
MN
MN
MN
MN
MN
MN
MN
MN
MN
MN
MN
MN
MN
MN
MN
MN
MO
MO
MO
MO
MO
MO
MO
MO
MO
MO
MO
MO
MO
MO
MO
MO
MO
MO
NC
NC
NC
NC
NC
NC •
sec
30488801
30501299
30700799
30700899
30701199
30701399
30788801
30788802
30800699
30800799
30899999
30988801
32099999
40188801
40188802
402BB801
40288802
40299998
40301097
40301099
40688801
40703697
40703698
30103399
30199999
30200799
30201599
30203299
30299999
30588801
30699998
30901099
39999198
39999998
40299999
40300198
40300199
40600197
40799997
40799998
50300801
30103199
30113299
30199999
30700199
30700799
30700899
PROC. DESCRIPTION
SEC. METAL PROD. FUQ.-NEC
TEXTILE TYPE GLASS - NEC
PLYWOOD - NEC, SPEC. IN COMM.
SAWMILL OPER. - NEC
PAPER COATING It SLAZINB - GENL
MISC. PAPER PROD. - NEC
WOOD PROD. FUG. SPEC. IN CQMM.
WOOD PROD. FUG. SPEC. IN COMM.
FAB. RUBBER PROD. - NEC
FAB. PLASTICS PROD. - NEC
RUBBER «t PLASTICS - NEC
FAB. METALS FUG. -SPEC. IN COMM
LEATHER PROD. - NEC
ORG. SOLVENT EVAP.-SPEC. IN CO
ORG. SOLVENT EVAP.-SPEC. IN CO
ORG. SOLVENT EVAP. FUG.- NEC
ORG. SOLVENT EVAP. FUG.- NEC
MISC. ORB SOLVENT EVAP. - NEC
STORAGE-SPECIFY LIQUID
STORAGE-SPECIFY LIQUID
PETROLEUM MKT. FUG.-SPEC-IFY
STORAGE-SPECIFY AROMATIC
STORAGE-SPECIFY AROMATIC
PESTICIDES - NEC
CHEM. MANF. - NEC
NO 5CC LISTED
SUGAR CANE PROC. - NEC
BAKERIES - NEC
FOOD I A6. NEC-SPEC. PROC.
MINERAL PROD. FUG. -NEC
NO SCC IN LISTING
ELECTROPLATING OPER. - NEC
NO SCC IN LISTING
MISC INDUSTRIAL PROC. - NEC
MISC. ORG SOLVENT EVAP. - NEC
NO SCC IN LISTING
NO SCC IN LISTING
NO SCC IN LISTING
NO SCC IN LISTING
NO SCC IN LISTING
TSDF-SURFACE IMPOUNDMENT
TEREPHTHALIC ACID- NEC
ORGANIC ACIDS PROD. -NEC
CHEMICAL MANF.- NEC
SULFATE PULPING- NEC
PLYWOOD/PART. BOARD- NEC
SAMMILL OPERATIONS- NEC
VOC
X
X
X
X
X
X
X
X
X
X
X
X
X
X
X
X
X
X
X
X
X
X
X
X
X
X
X
-
X
-
X
-
-
X
X
X
X
X
X
X
X
X
X
X
X
X
X
NOX
X
-
X
X
X
X
X
X
-
X
X
X
X
X
X
X
X
-
-
-
X
-
-
X
X
X
X
X
X
-
-
-
X
-
-
-
-
-
-
-
-
X
X
X
X
X
X
SOX
<
,-
I
<
X
<
X
X
-
X
X
X
X
X
X
X
X
-
-
-
X
-
-
X
X
X
X
-
X
X
-
X
-
X
-
-
-
-
-
-
-
X
X
X
X
X
X
»«NEC * PROCESS NOT ELSEWHERE CLASSIFIED
200
-------
TABLE C-2. SCC's FROM QUICK LOOK REPORTS FOR WHICH EMISSION
FACTOR DEVELOPMENT WAS NOT APPROPRIATE (Continued)
STATE SCC PROC. DESCRIPTION VOC NOX SOX
"~NC30702699~~FGRNlTURE~MANF7~-~NicX X x"~"
NM 30600999 NO SCC IN LISTIN8 - - X
OR 30101899 PLASTICS PROD.- NEC XXX
OR 30399999 PRIM. METALS IND. - NEC XX-
TN 30999999 FABRICATED METALS-NEC X X X
WV 30300999 STEEL PRODUCTION - NEC X
WV 30501499 NO SCC IN LISTING X X X
201
-------
-------
APPENDIX D
FUGITIVE EMISSIONS OF VOC FROM CHEMICAL UNITS
Fugitive emissions, or equipment leaks, of VOC represent a major
portion of the total VOC emitted to the atmosphere from organic chemical
manufacturing process units. Numerous studies have been conducted to
quantify the emissions and the effect of various control techniques on
emissions. An important finding of these studies is that emissions from
equipment leaks are related to process complexity, as described by equipment
counts. This differentiates fugitive emissions from process-related
emissions which generally vary with production volume.
Through its standards development activities, EPA conducted much
research in developing emission factors for the different equipment types
comprising fugitive emission sources. The factors generated during these
studies form the basis of the emissions estimation procedures discussed
below.
Emission Factors in NAPAP Listing
In the NAPAP listing presented in this document, fugitive emission
factors are presented for a limited number of organic chemical process
units. The emission values are given in units of Ibs/year and thus need to
be handled in a special manner to yield an emissions estimate. If employing
one of these listed factors, the data need to be coded with NEDS emission
estimation method code 3 (emissions to be calculated by a computerized
method) with a production rate of unity. This procedure enables the NEDS
computer inventory program to generate the correct annual emission estimate
automatically.
Emission factor estimates for fugitive emissions appear in this NAPAP
listing for fourteen process units: vinyl acetate, ethylene, cumene,
acetone/phenol, ethylene dichloride, vinyl chloride (monomer), formaldehyde,
methyl ethyl ketone, acetaldehyde, methylmethacrylate, adipic acid,
trichloroethylene/perchloroethylene, 1,1,1-trichloroethane, and
acrylonitrile. The estimates are based on average equipment counts for the
203
-------
associated process units included in the 24-unit study of SOCMI process
units (EPA-600/2-81-003). These average equipment counts were combined
with the average emission factors for individual equipment components
published in the Additional Information Document (AID) (EPA-450/3-82-010) to
yield an estimate of annual emissions (assuming 8,760 hours of operation).
These emission estimates are average values based upon limited
equipment count data. They represent an approximation only and should,
therefore, be used with some caution. More accurate estimates of fugitive
emissions can be generated using the following procedures.
Estimates Using the AID
The AID contains background information on the development of the
emission factors for equipment leaks in chemical process units. In
Appendix B of that document, the procedure for estimating total fugitive
emissions from a process unit is presented. That procedure, which uses
specific equipment counts for each equipment type and service, can also be
used to provide a more accurate estimate of fugitive emissions for any given
process unit.
As illustrated in Table D-l, the estimation technique is founded in the
specific equipment counts for the process unit of interest. As shown for
this example, the number of sources are grouped by equipment type (pump
seal, valve, etc.) and service (gas, light liquid, heavy liquid). The
individual component emission factors are provided in the table in terms of
Ib/hr/source. These are the SOCMI average emission factors that are
applicable to the industry overall, in the absence of unit-specific emission
factors (see below). The annual emissions estimate for each equipment type
and service is merely the product of the number of components and the
individual component emission factor, applied over the number of hours of
operation annually. In the example in Table D-l, one operating year was
taken to be 8,760 hours. The total of fugitive emissions is then estimated
as the sum of the estimates by equipment type and service.
This approach yields an estimate of fugitive emissions that is more
specific to the process unit of interest. Emissions can be even more
closely estimated provided certain additional data are gathered for the
204
-------
TABLE D-l. EXAMPLE OF EMISSIONS ESTIMATE USING THE AID APPROACH
Emissions
Source
Pump seals
Light Liquid
Heavy Liquid
Valves
Gas
Light Liquid
Heavy Liquid
Safety/relief valves
Gas
Open-ended lines
Compressors
Sampling connections
Flanges
TOTAL
Number of
Sources
29
30
402
524
524
11
410
2
26
2400
Emission Factor
Ib/hr/source
0.1087
0.0471
0.0123
0.0154
0.00051
0.229
0.0037
0.502
0.0330
0.0018
Annual Emissions
lbs/yra
27,600
12,800
43,400
70,700
2,300
22,000
13,400
8,800
7,500
38,400
246,900
For estimating purposes, one operating year was assumed to be 8,760 hours.
205
-------
specific process unit. These data require that a rigorous Method 21 survey
be conducted in the process unit to determine the number of sources leaking
and the number not leaking according to a given leak definition. This final
procedure, which is an extension of the AID procedure described above, is
detailed in a report on estimating emissions from equipment leaks of VOC and
hazardous air pollutants (HAP's) published in 1986 by EPA.
206
-------
APPENDIX E
SUMMARY TABLES OF CHANGES TO THE
SCC LISTING SINCE OCTOBER 1985
The following tables present the changes to the SCC listing since the
October 1985 Report was released. These changes reflect recommendations
from State agencies, the U. S. Environmental Protection Agency (EPA), and
Radian Corporation. All SCC's shown as deleted from this listing have been
retained in the NEDS computerized data base and can be accessed for
historical records. However, they will be suppressed from future printed
listings. More information about additions or deletions of SCC's to NEDS
can be obtained from the U. S. EPA's Office of Air Quality, Planning and
Standards (OAQPS).
207
-------
TABLE E-l. CHANGES TO THE SCC LISTING SINCE
THE 1985 NEDS REPORT
ACTION
SCC
DESCRIPTION
PREVIOUS UNITS
RECOMMENDED UNITS
CHANGE UNITS
CHANGE UNITS
CHANGE UNITS
CHANGE UNITS
CHANGE UNITS
CHANGE UNITS
CHANGE UNITS
CHANGE UNITS
CHANGE UNITS
CHANGE UNITS
CHANGE UNITS
CHANGE UNITS
CHANGE UNITS
301«**80
40200101
40200201
40200301
40200401
40200501
40200601
40200701
40200898
50300801
50300810
50300820
50300830
CHEMICAL MANF. -FUGITIVES
SURFACE COATING: PAINT
SURFACE COATING) PAINT
SURFACE COATING: VARNISH
SURFACE COATING: LACQUER
SURFACE COATING: ENAMEL
SURFACE COATING: PRIMER
SURFACE COATING: ADHESIVE
COATING OVEN-GENERAL
TSDF-SURFACE IMPOUND.
TSDF-HASTE PILES
TSDF-LAND TREATMENT
TSDF-CONTAINERS
LBS/YEAR
TONS COAT.
TONS COAT.
TONS COAT.
TONS COAT.
TONS COAT.
TONS COAT.
TONS COAT.
103 FEET
LBS/YEAR
LBS/YEAR
LBS/YEAR
LBS/YEAR
APPLIED
APPLIED
APPLIED
APPLIED
APPLIED
APPLIED
APPLIED
PROCESS UNIT-YEAR
TONii COAT. MIX APPLIED
TQNJi COAT. MIX APPLIED
TONJi COAT. MIX APPLIED
TONS! COAT. MIX APPLIED
TONS! COAT. MIX APPLIES
TONS! COAT. MIX APPLIED
TONii COAT. MIX APPLIED
10* FEET OF OVEN
103 SAL THRUPUT
ACRE OF STORAGE PILES
ACRI:
103 CONTAINERS STORED
ACTION
SCC
DESCRIPTION
REASON
FOR
CHANGE
DELETE SCCs
DELETE SCC
DELETE SCC
DELETE SCC
DELETE SCC
DELETE SCC
DELETE SCC
DELETE SCC
DELETE SCC
DELETE SCC
DELETE SCC
DELETE SCC
DELETE SCC
DELETE SCC
DELETE SCC
DELETE SCC
DELETE SCC
DELETE SCC
DELETE SCC
DELETE SCC
DELETE SCC
DELETE SCC
DELETE SCC
DELETE SCC
DELETE SCC
DELETE SCC
DELETE SCC
DELETE SCC
DELETE SCC
#*«900*»
30201914
30201915
30901601
30901602
30901603
33000201
33000202
33000203
40701607
40701608
40717201
40717202
40717203
40717204
40717605
40717606
40718001
40718002
40718003
40718004
40718005
40718006
40718007
40718008
40718009
40718010
40718097
40718098
OIL FIRED FLARES NO LONGER USED IN THE U.S.
VEGE. OIL-FUGITIVES REPLACED BY NEW SCC
VEGE. OIL- SOLVENT STORA6E REPLACED BY NEW SCC
METAL PIPE COAT. -ASPHALT DIP REPLACED BY NEW SCC
METAL PIPE COAT. -PIPE SPINNING REPLACED BY NEW SCC
METAL PIPE COAT. -PIPE WRAPPING REPLACED BY NEW SCC
RUBBERIZED FABRIC-IMPREGNATION REPLACED BY NEW SCC
RUBBERIZED FABRIC-WET COATING REPLACED BY NEW SCC
RUBBERIZED FABRIC-HOT MELT COAT. REPLACED BY NEW SCC
FIXED ROOF STOR. ISOPENTANE MUST BE STORED IN PRESSURE TANKS
FIXED ROOF STOR. ISOPENTANE MUST BE STORED IN PRESSURE TANKS
FLOAT ROOF STOR. ACETALDEHYDE MUST BE STORED IN PRESSURE TANKS
FLOAT ROOF STOR. ACETALDEHYDE MUST BE STORED IN PRESSURE TANKS
FLOAT. ROOF STOR. ACROLEIN MUST BE STORED IN PRESSURE TANKS
FLOAT. ROOF STOR. ACROLEIN MUST BE STORED IN PRESSURE TANKS
FLOAT. ROOF STOR. N-PENTANE MUST BE STORED IN PRESSURE TANKS
FLOAT. ROOF STOR. N-PENTANE MUST BE STORED IN PRESSURE TANKS
FLOAT. ROOF STOR. ISOPRENE MUST BE STORED IN PRESSURE TANKS
FLOAT. ROOF STOR. ISOPRENE MUST BE STORED IN PRESSURE TANKS
FLOAT ROOF STOR, METHYLALLENE MUST BE STORED IN PRESSURE TANKS
FLOAT ROOF STOR. METHYLALLENE MUST BE STORED IN PRESSURE TANKS
FLOAT. ROOF STOR. 1-PENTENE MUST BE STORED IN PRESSURE TANKS
FLOAT. ROOF STOR. 1-PENTENE MUST BE STORED IN PRESSURE TANKS
FLOAT. ROOF STOR. PIPERYLENE MUST BE STORED IN PRESSURE TANKS
FLOAT. ROOF STOR. PIPERYLENE MUST BE STORED IN PRESSURE TANKS
FLOAT ROOF STOR. CYCLOPENTENE MUST BE STORED IN PRESSURE TANKS
FLOAT ROOF STOR. CYCLOPENTENE MUST BE STORED IN PRESSURE TANKS
FLOAT. ROOF STOR. OTHER ALKENES MUST BE STORED IN PRESSURE TANKS
FLOAT. ROOF STOR. OTHER ALKENES MUST BE STORED IN PRESSURE TANKS
208
-------
TABLE E-l. CHANGES TO THE SCC LISTING SINCE
THE 1985 NEDS REPORT (Continued)
ACTION
SCC
DESCRIPTION
UNITS
ADD SCC 10200213 EXT. COMBUSTION-WET SLURRY
ADD SCC 20100702 COMBUSTION-PROCESS GAS, RECIP.
ADD SCC 30101949 PLASTICS PROD-ABS RESIN
ADD SCC 30101970 POLYETHER RESIN PROD.-REACTOR
ADD SCC 30101971 POLYETHER RESIN PROD.-BLOW. FREON
ADD SCC 30101972 POLYETHER RESIN PROD.-MISCELL.
ADD SCC 30101990 POLYURETHANE-REACTOR
ADD SCC 30101891 POLYURETHANE-BLOWIN6 AGENT-FREQN
ADD SCC 30101992 POLYURETHANE-BLOWING AGENT-MC
ADD SCC 30101983 POLYURETHANE-TRANS/CONVEY/STORAGE
ADD SCC 30101994 POLYURETHANE-PACKAGING/SHIPPING
ADD SCC 30101885 POLYURETHANE-SPECIFY IN COMMENTS
ADD SCC 30103311 AGRIC. PESTICIDE PROD. GENL.
ADD SCC 30103312 AGRIC. PESTICIDE PROD. GENL.
ADD SCC 30106011 PHARMACEUTICALS-COATING PROC.
ADD SCC 30106012 PHARMACEUTICALS-GRANULATION PROC.
ADD SCC 30111201 ELEMENTAL PHOSPHORUS-CALCINER
ADD SCC 30112202 ELEMENTAL PHOSPHORUS-FURNACE
ADD SCC 30112299 ELEMENTAL PHOSPHORUS-SPEC. IN COM.
ADD SCC 30112720 FLUOROCARBONS PROD. CF 12/11
ADD SCC 30112730 FLUOROCARBONS PROD. CF 23/22
ADD SCC 30112740 FLUOROCARBONS PROD. CF 113/114
ADD SCC 30113701 ESTERS PROD.-ETHYL ACRYLATE
ADD SCC 30113710 ESTERS PROD.-BUTYL ACRYLATE
ADD SCC 30200512 GRAIN PROC. COUNTRY ELEVATORS
ADD SCC 30200611 GRAIN PROC. COUNTRY ELEVATORS
ADD SCC 30201906 VEGE. OIL PROD.-CORN OIL
ADD SCC 30201907 VEGE. OIL PROD.-COTTONSEED OIL
ADD SCC 30201909 VEGE. OIL PROD.-SOYBEAN OIL
ADD SCC 30201909 VEGE. OIL PROD.-PEANUT OIL
ADD SCC 30201916 VEGE. OIL PROD.-OIL EXTRACTION
ADD SCC 30201917 VESE. OIL PROD.-MEAL PREPARATION
ADD SCC 30201918 VEGE. OIL PROD.-OIL REFINING
ADD SCC 30201919 VEGE. OIL PROD.-FUGITIVES
ADD SCC 30201920 VEGE. OIL PROD.-SOLVENT STORAGE
ADD SCC 30202101 POULTRY PROD.-MANURE HAND./DRY
ADD SCC 30202102 POULTRY PROD.-MANURE HAND./DRY
ADD SCC 30202105 POULTRY PROD.-MANURE HAND./MET
ADD SCC 30202106 POULTRY PROD.-MANURE HAND./WET
ADD SCC 30203801 ANIMAL/POULTRY RENDERING-GENL
ADD SCC 30300211 RUBBERIZED FABRIC-IMPREGNATION
ADD SCC 30300212 RUBBERIZED FABRIC-WET COATING
ADD SCC 30300213 RUBBERIZED FABRIC-HOT MELT COATING
ADD SCC 30300214 RUBBERIZED FABRIC-WET COAT MIXING
ADD SCC 30400114 SEC, ALUMINUM-POUR t CASTINS
ADD SCC 30400513 LEAD BATTERY MANF.-BARTON PROCESS
ADD SCC 30400521 LEAD BATTERY MANF.-OVERALL PROCESS
ADD SCC 30400522 LEAD BATTERY MANF.-GRID CASTING
ADD SCC 30400523 LEAD BATTERY MANF.-PASTE MIXING
TONS BURNED
10 CUBIC FEET BURNED
TONS PRODUCED
TONS PRODUCT
TONS PRODUCT
TONS PRODUCT
TONS PRODUCT
TONS AGENT USED
TONS AGENT USED
TONS PRODUCT
TONS PRODUCT
TONS PRODUCT
GALLONS STORED
POUNDS STORED
TONS SOLVENT IN COATING
TONS SOLVENT CONSUMED
TONS PROCESSED
TONS PROCESSED
TONS PRODUCT
TONS PRODUCED
TONS PRODUCED
TONS PRODUCED
TONS PRODUCED
TONS PRODUCED
TONS GRAIN SHIPPED OR RECVD.
TONS GRAIN SHIPPED OR RECVD.
TONS EXTRACTOR FEEDCAKE
TONS EXTRACTOR FEEDCAKE
TONS EXTRACTOR FEEDCAKE
TONS EXTRACTOR FEEDCAKE
TONS EXTRACTOR FEEDCAKE
TONS EXTRACTOR FEEDCAKE
TONS EXTRACTOR FEEDCAKE
TONS EXTRACTOR FEEDCAKE
TONS RAW SEED PROCESSED
NUMBER OF CHICKENS CAPACITY
NUMBER OF CHICKENS THRUPUT
NUMBER OF CHICKENS CAPACITY
NUMBER OF CHICKENS THRUPUT
TONS PROCESSED
TONS COATING APPLIED
TONS COATING APPLIED
TONS COATING APPLIED
TONS COATING APPLIED
TONS METAL CHARGED
TONS PROCESSED
TONS PROCESSED
TONS PROCESSED
TONS PROCESSED
209
-------
TABLE E-l. CHANGES TO THE SCC LISTING SINCE
THE 1985 NEDS REPORT (Continued)
ACTION
SCC
DESCRIPTION
UNITS
ADD SCC
ADD SCC
ADD SCC
ADD SCC
ADD SCC
ADD SCC
ADD SCC
ADD SCC
ADD SCC
ADD SCC
ADD SCC
ADD SCC
ADO SCC
ADD SCC
ADD SCC
ADD SCC
ADD SCC
ADD SCC
ADD SCC
ADD SCC
ADD SCC
ADD SCC
ADD SCC
ADD SCC
ADD SCC
ADD SCC
ADD SCC
ADD SCC
ADD SCC
ADD SCC
ADO SCC
ADD SCC
ADD SCC
ADD SCC
ADD SCC
ADD SCC
ADD SCC
ADD SCC
ADD SCC
ADD SCC
ADD SCC
ADD SCC
ADD SCC
ADD SCC
ADD SCC
ADD SCC
ADD SCC
ADD SCC
ADD SCC
30400524
30400525
30400526
30400527
30400528
30401002
30401004
30401005
30401006
30401007
30401008
30401010
30401011
30515001
30515002
30515003
30515004
30515005
30701097
30901605
30901606
30901607
30903005
30903006
31000207
39999993
39999994
40100208
40100227
40100228
40299995
40299996
40500413
40704421
40704422
40704423
40704424
40706813
40706814
40781201
40781202
40781606
40781607
40782007
40782008
40782009
40782010
40782011
40799997
NICKEL PROD.
NICKEL PROD.
NICKEL PROD.
NICKEL PROD.
NICKEL PROD.
TONS PROCESSED
TONS PROCESSED
TONS PROCESSED
TONS PROCESSED
TONS PROCESSED
TONS PROCESSED
TONS PROCESSED
TONS PROCESSED
TONS PROCESSED
TONS THROUGHPUT
TONS THROUGHPUT
TONS THROUGHPUT
TONS THROUGHPUT
TONS THROUGHPUT
TONS MAKEUP
10J SQ FT PIPE PROCESSED
10"
LEAD BATTERY MANF.-LEAD OXIDE MILL TONS PROCESSED
LEAD BATTERY MANF.-STACK/PB BURN TONS PROCESSED
LEAD BATTERY MANF.-RECLAIMING FURN.TONS PROCESSED
LEAD BATTERY MANF.-SML. PARTS CAST TONS PROCESSED
LEAD BATTERY MANF.-FORMATION
-MIX/BLEND/GRIND
-HEAT TREAT. FURN.
NICKEL PROD.-INDUCTION FURN.(IN)
NICKEL PROD.-INDUCTION FURN.(VAC)
-EAF NX CARBON ELECT.
-EAF
-FININSHINGs PICKLING
NICKEL PROD.-FINISHING! GRINDING
CALCINING-RAH MATERIAL HAND.
CALCININ6-GENERAL
CALCININ6-6RINDINS/MILL ING
CALCINING-FINISHED PROD. HAND.
CftLCINING-MIXING
ELECTROPLATING-SPEC. IN COMM.
METAL PIPE COATING-ASPHALT DIPPING
METAL PIPE COATING-PIPE SPINNING
METAL PIPE COATING-PIPE WRAPPING
MACHINING OPER.-SAWING, SPEC. MAT.
MACHINING OPER.-HONING, SPEC. MAT.
NATL. GAS PROD.-VALVES (FUGITIVES)
INDUSTRIAL PROCESSES
INDUSTRIAL PROCESSES
DE6REASING-CHLOROSOLVE
SOLVENT-HEXYLENE 6LYCQL
SOLVENT-ETHYLENE OXIDE
SURFACE COATING-SPECIFY IN COMM.
SURFACE COATING-SPECIFY IN COMM.
LITH06RAPHIC-ISOPROPYL ALCOHOL
FIXED ROOF STOR.-N-PROPYL ACETATE
FIXED ROOF STOR.-N-PROPYL ACETATE
FIXED RF. STOR.-i-BUTYL-i-BUTYRATE 103GAL
FIXED RF. STOR.-i-BUTYL-i-BUTYRATE 10J6AL
FIXED ROOF STOR.-METHYLAMYL KETONE 103GAL
FIXED ROOF STOR.-METHYLAMYL KETONE
PRESSURE TANKS - ACETALDEHYDE
ACROLEIN
ISOPENTANE
N-PENTANE
ISOPRENE
METHYLALLENE
1-PENTENE
PIPERYLENE
CYCLOPENTENE
MISC.
MISC.
VAPOR
THIN.
THIN.
PRESSURE TANKS
PRESSURE TANKS
PRESSURE TANKS
PRESSURE TANKS
PRESSURE TANKS
PRESSURE TANKS
PRESSURE TANKS
PRESSURE TANKS
MISC. ORGANIC CHEMICAL STORAGE
SQ FT PIPE PROCESSED
103 SQ FT PIPE PROCESSED
TONS PROCESSED
TONS PROCESSED
PROCESS UNIT/YR
PARTS PROCESSED
POUNDS PROCESSED
TONS SOLVENT USED
TONS SOLVENT USED
TONS SOLVENT USED
TONS SOLVENT IN COATING
TONS SOLVENT
TON SOLVENT USED
lO^GAL. STOR. CAPACITY
THROUGHPUT
STOR. CAPACITY
THROUGHPUT
STOR. CAPACITY
THROUGHPUT
1000 GALLONS THROUGHPUT
1000 GALLONS THROUGHPUT
1000 GALLONS THROUGHPUT
1000 GALLONS THROUGHPUT
1000 GALLONS THROUGHPUT
1000 GALLONS THROUGHPUT
1000 GALLONS THROUGHPUT
1000 GALLONS THROUGHPUT
1000 GALLONS THROUGHPUT
10 GAL. STORAGE CAPACITY
103GAL.
103GAL.
210
------- |