PB95-963801
                            EPA/ROD/R02-95/244
                            July 1995
EPA  Superfund
       Record of Decision:
       GCL Tie & Treating, Inc.
       OU2, Sidney, Delaware County, NY
       3/31/95

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             RECORD OF DECISION
              DECISION SUMMARY
               Operable Unit 2

             GCL Tie & Treating

      Sidney,  Delaware County,  New York
United States Environmental Protection Agency
                  Region II
              New York,  New York
                  March  1995

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             DECLARATION FOR THE RECORD OF DECISION
SITE NAME AND LOCATION

GCL Tie & Treating
Sidney, Delaware County, New York


STATEMENT OF BASIS AND PURPOSE

This Record of Decision  (ROD) documents the U.S. Environmental
Protection Agency's  (EPA's) selection of the remedial action for
the GCL Tie & Treating site  (the Site) in accordance with the
requirements of the  Comprehensive Environmental Response,
Compensation and Liability Act of 1980, as amended  (CERCLA), 42
U.S.C. §§9601-9675 and the National Oil and Hazardous Substances
Pollution Contingency Plan  (NCP), 40 CFR Part 300.  An
administrative record for the Site, established pursuant to the
NCP, 40 CFR 300.800, contains the documents that form the basis
for EPA's selection  of the remedial action  (see Appendix III).

The New York State Department of Environmental Conservation
(NYSDEC) has been consulted on the planned remedial .action in
accordance with section  121(f) of.CERCLA, 42 U.S.C. §9621(f), and
concurs with the selected remedy (see Appendix IV)  contingent
upon further concurrence based on any changes made  to the
selected remedy during the remedial design.


ASSESSMENT OF THE SITE

Actual or threatened releases of hazardous substances from the
Site,  if not addressed by implementing the response action
selected in this ROD, may present an imminent and substantial
endangerment to public- health, welfare, or the environment.


DESCRIPTION OF THE SELECTED REMEDY

The selected remedy  pertains to the last of two operable units
for the Site and addresses the non-GCL property soils,
contaminated groundwater, and surface-water sediments located at
the GCL Site.  The first operable unit addressed the
contamination in the GCL-property soils.

The major components of  the selected remedy include:

•    Extraction, collection, and on-site treatment  of groundwater
     contaminated with organic compounds; discharge of treated
     groundwater to  the  surface water.  The selected remedy
     provides two options for primary treatment of  organics:
     carbon adsorption or biological treatment.

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     Information will be obtained during the remedial design to
     reassess the time frame and technical practicability of
     achieving State and Federal drinking water standards in the
     aquifer.  Should the remedial design data indicate that
     groundwater restoration through extraction and treatment is
     feasible and practical, additional work will be conducted to
     determine which groundwater treatment option (carbon
     adsorption or biological treatment) is more appropriate and
     cost-effective.  If groundwater restoration is not feasible
     or practical, the remedy will focus on containing the
     groundwater contamination within the GCL-property boundaries
     in which case chemical-specific ARARs may be waived for all
     or some portions of the aquifer based on the technical
     impacticability of achieving further contamination reduction
     within a reasonable time frame.  Under such a scenario, it
     may be determined that natural attenuation or enhanced
     biodegradation  (e.g.. introduction of air to increase the
     rate of biodegradation) would be able to reduce the
     concentration of contaminants in the aquifer groundwater to
     levels which are similar to those achievable under
     extraction and treatment, but at a lower cost.  Such
     information would be utilized during the remedial design to
     maximize the effectiveness and efficiency of the system;
     and,

•    Excavating and treating contaminated sediments on-site
     through a thermal desorption process along with the GCL-
     property soils.  The selected remedy will also provide for
     the mitigation of damages to the aquatic environment which
     may occur during implementation (i.e.. revegetation).

In addition, EPA will recommend to local agencies that
institutional control measures be undertaken to ensure that
future land use of the property continues to be
industrial/commercial, and precludes the use of Site groundwater
for human consumption until drinking water quality is restored in
the aquifer.
DECLARATION OF STATUTORY DETERMINATIONS

The selected remedy meets the requirements for remedial actions
set forth in Section 121 of CERCLA, 42 U.S.C. §9621 as:   (1) it
is protective of human health and the environment; (2) it attains
a level or standard of control of the hazardous substances,
pollutants and contaminants, which at least attains the legally
applicable or relevant and appropriate requirements (ARARs) under
State and Federal laws; (3) it is cost-effective;  (4)  it utilizes
permanent solutions and alternative treatment (or resource
recovery) technologies to the maximum extent practicable; and (5)
it satisfies the statutory preference for remedies that employ
treatment to reduce the toxicity, mobility, or volume of the
hazardous substances, pollutants or contaminants at a site.

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A review of the remedial action pursuant to CERCLA §121(c), 42
U.S.C. §9621(c), will be conducted five years after the
commencement of the remedial action to ensure that the remedy
continues to provide adequate protection to human health and the
environment, because this remedy will result in hazardous
substances remaining on-site above health-based levels.
Jeanne
Regiona
M. Jfox.   s^
L/Adminj^^ra
                 rator

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             RECORD OF DECISION
              DECISION SUMMARY
               Operable Unit 2

             GCL Tie  & Treating

      Sidney, Delaware County, New York
United States Environmental Protection Agency
                  Region II
              New York,  New York
                  March  1995

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                          LIST OF TABLES
 TABLE 1


 TABLE 2

 TABLE 3


 TABLE 4

 TABLE 5


 TABLE 6

 TABLE 7


 TABLE 8

.TABLE 9

 TABLE 10
SUMMARY OF NON-GCL PROPERTY SOIL ANALYTICAL
RESULTS

SUMMARY OF SURFACE WATER ANALYTICAL RESULTS

SUMMARY OF SURFACE-WATER SEDIMENTS ANALYTICAL
RESULTS

SUMMARY OF GROUNDWATER ANALYTICAL RESULTS

CONTAMINANTS OF POTENTIAL CONCERN USED IN THE RISK
ASSESSMENT

RISK ASSESSMENT EXPOSURE PATHWAYS

TOXICITY DATA FOR CARCINOGENIC AND NONCARCINOGENIC
RISK EVALUATION

CARCINOGENIC AND NONCARCINOGENIC RISK LEVELS

LIST OF ARARs AND TBCs

BREAKDOWN OF COSTS ASSOCIATED WITH THE SELECTED
REMEDY
                                IV

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SITE NAME, LOCATION AND DESCRIPTION

The GCL Tie and Treating site (the Site) occupies approximately
60 acres in an industrial/commercial area of Delaware County,  New
York (see Figure 1).  According to an analysis of historical
photographs conducted by the U.S. Environmental Protection Agency
(EPA) and accounts by local residents, wood-preserving activities
at the Site date as far back as the 1940's.

The Site is bordered on the north by a railroad line.  A
warehouse and a municipal airport are located to the north of the
railroad line.  Route 8 and Delaware Avenue delineate the eastern
and southern borders of the Site, respectively.  A drainage ditch
(Unalam Tributary) and woodland area lie between Delaware Avenue
and the Site.  The western portion of the property abuts a small
impoundment and wetlands area.  The Site eventually drains via
overland flow to the Susquehanna River, which is located within
one mile of the Site.

The Site includes two major areas, generally referred to as the
"GCL property" and "non-GCL property"  (see Figure 2).  The 26-
acre GCL property housed a wood-treating facility called GCL Tie
& Treating, and includes four structures.  The primary building
housed the wood pressure treatment operations including two
treatment vessels  (50 feet in length,by 7 feet in diameter), an
office, and a small laboratory.  Wood  (mostly railroad ties) and
creosote were introduced into the vessels which were subsequently
pressurized in order to treat the wood.  The remaining three
structures housed a sawmill and storage space.  The non-GCL
portion of the Site includes two active light manufacturing
companies  (which did not conduct wood treatment operations)
located on a parcel of land adjacent to the GCL property.

Approximately 1,100 people are employed in a nearby industrial
area.  About 5,000 people live within 2 miles of the Site and
depend on groundwater as their potable water supply.  The nearest
residential well is within 0.5 mile of the Site.  Two municipal
wells, supplying the Village of Sidney, are located within 1.25
miles of the Site.  A shopping plaza consisting of fast-food
restaurants and several stores is located approximately 300 feet
south of the Site.  Other facilities  (i.e.f a hospital, public
schools, senior citizen housing, and child care centers) are
located within 2 miles of the Site.

SITE HISTORY AND ENFORCEMENT ACTIVITIES

The Site first came to the attention of the New York State
Department of Environmental Conservation (NYSDEC) in 1986, after
one of the pressure vessels used at the ,GCL facility
malfunctioned, causing a release of an estimated 30,000 gallons
of creosote.  GCL personnel excavated the contaminated surface
soil and placed it in a mound; no further action was undertaken

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at the time.

In September 1990, NYSDEC requested EPA to conduct a removal
assessment at the Site.  Consequently,  EPA conducted sampling of
the GCL Tie and Treating facility in October 1990.  As a result
of the data and information that were obtained as part of the
assessment, a Removal Action was initiated by EPA in March 1991.

Activities conducted as part of the removal effort included: site
stabilization (e.g..  run-off and dust control),  delineation of
surface contamination, installation of a chain-link fence,
identification and disposal of containerized  (e.g..  tanks, drums)
and uncontainerized hazardous wastes (e.g.. wastes in sumps);
preparation of approximately 6,000 cubic yards (cy)  of
contaminated soil and wood debris for disposal;  and a pilot study
to determine the effectiveness of composting for bioremediation
of creosote-contaminated soils.

The Site was proposed for inclusion on the National Priorities
List  (NPL) in February 1994 and was added to the NPL in May 1994.
In September 1994, EPA signed a Record of Decision (ROD) for the
first operable unit which called for the excavation and on-site
treatment of approximately 36,100 cubic yards of contaminated
soil and debris by a thermal desorption process.

EPA has been conducting a search for potentially responsible
parties (PRPs).  To date, only one PRP has been identified and
notified of his potential liability under CERCLA; however, this
PRP was not considered to be a viable candidate to undertake the
necessary response actions.  If EPA determines that there are one
or more viable PRPs,  EPA will take appropriate enforcement
actions to recover its response costs pursuant to CERCLA, 42
U.S.C. § 9601 - 9675.

HIGHLIGHTS OP COMMUNITY PARTICIPATION

The Remedial Investigation (RI) report and the Proposed Plan for
the Site were released to the public for comment on March 1,
1995.  These documents were made available to the public in the
administrative record file at the EPA Docket Room in Region II,
in New York City and the information repository at the Sidney
Memorial Library in Sidney, NY.  The notice of availability of
the above-referenced documents was published  in the Oneonta Daily
Star on March 1, 1995.  The public comment period on these
documents was held from March 1, 1995 to March 30, 1995.

On March 8, 1995, EPA and NYSDEC conducted a public meeting at
the Civic Center in Sidney, NY to inform local officials and
interested citizens about the Superfund.process, to review
current and planned remedial activities at the site, and to
respond to any questions from area residents and other attendees.

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Responses to the comments received at the public meeting and in
writing during the public comment period are included in the
Responsiveness Summary (see Appendix V) .

SCOPE AND ROLE OF OPERABLE UNIT

The GCL Tie & Treating site was selected as a pilot project for
the Superfund Accelerated Cleanup Model (SACM) initiative.  The
purpose of SACM is to make Superfund cleanups more timely and
efficient.  Under this pilot, activities which would normally
have been performed sequentially (e.g.f site assessment, NPL
placement, removal assessment) were performed concurrently.  In
June 1993, while attempting to determine if the Site would score
high enough for inclusion on the NPL, EPA initiated RI/FS
activities to delineate further the nature and extent of
contamination at the Site.  These activities would not typically
have been initiated until after the Site had been proposed for
the NPL.

Site remediation activities are sometimes segregated into
different phases, or operable units, so that remediation of
different environmental media or areas of a site can proceed
separately, resulting in an expeditious remediation of the entire
site.  EPA has designated two operable units for the GCL Tie &
Treating site as described below. .

   »•  Operable unit 1 addresses the remediation of contaminated
soils found on the GCL-property portion of the Site via thermal
desorption.  This operable unit is currently in the remedial
design phase.

   >•  Operable unit 2 addresses the contamination in the soils on
the remainder of the Site  (non-GCL property), and in the
groundwater, surface water, and surface-water sediments.  This is
the final operable unit planned for this Site and the subject of
this ROD.

SUMMARY OF SITE CHARACTERISTICS

The nature and extent of contamination found at the Site were
assessed through a comprehensive sampling of soil, groundwater,
surface water, and surface-water sediment.  Sampling was
conducted during the Fall/Winter of 1993.  The investigation
focussed on contaminants typically associated with the creosote
wood-preserving process.  Creosote contaminants typically found
included numerous polyaromatic hydrocarbons (PAHs) such as
benzo[a]anthracene, chrysene, benzo[b]fluoranthene, benzo
[k]fluoranthene, benzo[a]pyrene, indeno[l,2,3-c,d] pyrene and
dibenzo[a,h]anthracene.

The following paragraphs discuss the characterization of
contamination in the operable unit 2 study area, namely, in the

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groundwater, surface water, surface-water sediments, and non-GCL
property soils.

Soils

Approximately 130 soil samples were collected from monitoring-
well and soil borings drilled on the GCL property and on the non-
GCL property.  Samples also were collected at off-site locations
to provide information on background conditions.  Table 1
summarizes the analytical results for the soil samples collected
on the non-GCL property.  In general, relatively low levels of
contaminants were detected with total PAHs ranging up to 24 parts
per million  (ppm).  Generally, the concentrations of metals
detected ori-site were not significantly above background
concentration ranges with the exception of beryllium (up to 3.2
ppm), copper (up to 176 ppm) and lead (up to 46 ppm), which were
above their representative background concentrations of 0.6 ppm,
26.2 ppm and 11.2 ppm, respectively.

Surface Water

Surface water samples and sediments were collected at 7 locations
along the drainage ditch and the impoundment.  Table 3 summarizes
the analytical results.  Of the 14 inorganics detected in the
surface water samples, only arsenic  (up to 11.4 parts per billion
[ppb]), copper (up to 35.2 ppb) and nickel (up to 19.6 ppb)
significantly exceeded State or Federal ambient water quality  .
standards.  The only organic contaminant detected was
chloroethane at a level of 12 ppb.

Surface-Water Sediments

Elevated PAH concentrations were detected at 3 of the 7 sediment
sampling locations along the drainage ditch and the impoundment
along the western side of the Site.  Table 2 summarizes the
analytical results.  The extent of contamination (see Figure 3)
is approximately 2,850 feet in length, 1.5 feet in width and 0.5
feet in depth in the tributary, as well as a 5-foot wide strip
along the edge of the impoundment.  PAHs were detected in these
areas with total concentrations ranging up to 23,850 ppb.  The
PAH contamination detected in the unconsolidated sediments is
most likely attributed to runoff from the Site soils.  Arsenic
(up to 16,400 ppb), copper  (up to 51,900 ppb), lead  (up to 70,200
ppb), manganese  (up to 547,000 ppb), mercury  (up to 690 ppb),
nickel (up to 43,600 ppb), and zinc  (up to 173,000) were detected
in concentrations which exceeded their respective sediment
criteria values.  However, arsenic, copper, manganese, nickel,
and zinc were detected at concentrations relatively equivalent to
their respective background levels.  The relatively elevated
concentrations of these metals could be attributed to regional
background variations or from off-site sources, as these
contaminants are not typically associated with the wood-

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preserving operations conducted at the Site.

Groundwater

Site-specific geology within the GCL property is characterized by
a layer of fill approximately 5 feet thick on the western portion
of the Site which gradually decreases to approximately 2 to 3
feet on the eastern section of the GCL property.  The fill
consists predominantly of silt and clay with significant amounts
of wood and assorted debris.  The fill is underlain by silt and
clay type soils.

There are two hydrogeologic systems consisting of the overburden
and bedrock units.  The overburden unit can be further divided
into shallow (approximately 5 to 16 feet in depth) and
intermediate (approx. 11 to 25 feet in depth) groundwater zones.
Groundwater is first encountered at depths ranging from 5 to 8
feet below grade around the Site.  As a general rule, groundwater
flow in the overburden aquifer appears to be in a north-
northwesterly direction; groundwater movement in the bedrock
appears to be in a northerly direction.  Permeability of the
overburden and bedrock soils is relatively low; groundwater flow
through the bedrock aquifer occurs primarily through fractures.

Six previously existing groundwater monitoring wells and 14 new
wells were sampled during the RI.  Two rounds of samples were
collected and analyzed for a full range of organic and inorganic
constituents.  Table 4 summarizes the analytical results.  The
data in Table 4 indicate the contaminants associated with the GCL
site wells influenced by the Route 8 Landfill contamination
 (column 3 of the table) and the GCL Site wells not influenced by
the Route 8 Landfill contamination  (column 4 of the table).  Two
main groups of organic compounds were found  in the groundwater
above drinking water standards, namely, PAHs and volatile organic
compounds  (VOCs).  Referring to column 4, PAHs, including
benzo[b]fluoranthene  (up to 3 ppb - drinking water standard of
0.2 ppb), benzo[a]pyrene  (up to 2 ppb - drinking water standard
of 0.2 ppb), chrysene  (up to.4 ppb - drinking water standard of
0.2 ppb) and benzene  (220 ppb - drinking water standard of 5 ppb)
significantly exceeded drinking water standards, and are the same
type of contaminants as those found in high  concentrations in the
Site soils.  Referring to column 3, chlorinated VOCs such as
vinyl chloride  (up to 4,700 ppb - drinking water standard of 2
ppb), 1,1-dichloroethane  (up to 1,200 ppb -  drinking water
standard of 5 ppb), cis-l,2-dichloroethene  (up to 4,300 ppb -
drinking water standard of 70 ppb), and trichloroethene  (up to
1,000 ppb - drinking water standard of 5 ppb) were also found at
concentrations exceeding the drinking water  standards, however,
they are most likely not related to the .activities that took
place at the GCL site.  It is likely that these chlorinated VOCs
originated from the Route 8 Landfill, located across from
Delaware Avenue and hydraulically upgradient from the GCL Site.

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The data obtained during the RI suggest that the contaminant
plume originating at the Route 8 Landfill extends beneath much of
the GCL Site.  Currently, the Route 8 site is being remediated
under the New York State hazardous waste remediation program; a
groundwater collection and treatment system designed to address
the groundwater contamination was constructed and recently
started operation.

Aluminum (up to 6,210 ppb), iron (up to 37,600 ppb), manganese
(up to 17,300), antimony  (up to 44.3 ppb), chromium (up to 166
ppb), and nickel  (up to 131 ppb) were detected in groundwater
samples in concentrations significantly above drinking water
standards.  However, the presence of most of these metals at
elevated concentrations in background and off-site wells is
potentially indicative of background levels and/or off-site
sources.

It is estimated that the GCL contaminant plume extends over an
area of approximately 173,500 square feet (see Figure 4) with a
thickness of approximately 45 feet.  The volume of contaminated
water which exceeds drinking water standards is estimated at 10
million gallons.

During the RI, a  creosote product layer (referred as dense
nonaqueous phase  liquid  [DNAPL]) was discovered in the shallow
groundwater, in a localized area near the wood treatment/process
buildings.  DNAPLs are heavier than water, and have a tendency to
sink.  PAH compounds, which are the principal components of
creosote, are extremely immobile and tend to attach to the
aquifer soil particles rather than move with the groundwater.
The DNAPL appears to be perched on many thin soil layers rather
than in a single well-defined pool.  It is estimated that the
DNAPL.layer ranged from 1 to 2 feet in thickness, and contained
concentrations of PAHs in excess of 8,000 ppm.  The volume of the
DNAPL layer is estimated at 10,000 to 30,000 gallons.  The data
suggest that the  DNAPL layer is contained within the property
boundaries.  DNAPLs constitute a highly significant source of
soil and groundwater contamination at the Site.

SUMMARY OF SITE RISKS

Based upon the results of the RI, a baseline risk assessment was
conducted to estimate the risks associated with current and
future Site conditions.  The baseline risk assessment estimates
the human health and ecological risk which could result from the
contamination at the Site, if no remedial action were taken.

Human Health Risk Assessment

A four-step process is utilized for assessing site-related human
health risks for a reasonable maximum exposure scenario:  Hazard
Identification—identifies the contaminants of concern at the

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site based on several factors such as toxicity, frequency of
occurrence, and concentration.  Exposure Assessment—estimates -
the magnitude of actual and/or potential human exposures, the
frequency and duration of these exposures, and the pathways
(e_._g. , ingesting contaminated soil) by which humans are
potentially exposed.  Toxicitv Assessment—determines the types
of adverse health effects associated with chemical exposures, and
the relationship between magnitude of exposure (dose) and
severity of adverse effects  (response).  Risk Characterization—
summarizes and combines outputs of the exposure and toxicity
assessments to provide a quantitative assessment of site-related
risks.

EPA conducted a baseline risk assessment to evaluate the
potential risks to human health and the environment associated
with the GCL property in its current state.  The Risk Assessment
focused on contaminants in the soil, surface water, surface-water
sediments, and groundwater which are likely to pose significant
risks to human health and the environment.  A summary of the
contaminants of potential concern in sampled matrices is listed
in Table 5.

An exposure assessment was conducted for reasonable maximum
exposures to estimate the magnitude, frequency, and duration of
actual and/or potential exposures to the contaminants of
potential concern present in the sampled media.  Reasonable
maximum exposure is defined as the highest exposure that is
reasonably expected to occur at the Site for individual and
combined pathways.  The baseline risk assessment evaluated the
current health effects which could potentially result from
ingestion, inhalation, and dermal contact of soils, and ingestion
and dermal contact of surface water and surface-water sediments
by Site trespassers; ingestion, inhalation and dermal contact of
groundwater by off-site residents; the ingestion and inhalation
of soils by.off-site residents; and ingestion, dermal contact,
and inhalation of soils by workers  (see Table 6).  These exposure
pathways were evaluated separately for adults and children.  The
future-use scenario evaluated the same scenarios and also
evaluated the potential health impacts resulting from ingestion,
inhalation and direct contact to soil by future on-site workers.
Site-related and nonsite related fe.g.. Route 8 Landfill)
potential health threats were evaluated.  The property is
currently zoned for industrial/commercial use only.  Input from
the community and local officials, indicated that
industrial/commercial use of the property would be the preferred
use of the property in the future.  Therefore, it was assumed
that future land uses of the property would continue to be
industrial/commercial.

Under current EPA guidelines, the likelihood of carcinogenic
(cancer-causing)  and noncarcinogenic effects due to exposure to
site chemicals are considered separately.  It was assumed that

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the toxic effects of the site-related chemicals would be
additive.  Thus, carcinogenic and noncarcinogenic risks
associated with exposures to individual compounds of concern were
summed to indicate the potential risks associated with mixtures
of potential carcinogens and noncarcinogens, respectively.

Potential carcinogenic risks were evaluated using the cancer
slope factors developed by EPA for the contaminants of concern.
Cancer slope factors (SFs) have been developed by EPA's
Carcinogenic Risk Assessment Verification Endeavor for estimating
excess lifetime cancer risks associated with exposure to
potentially carcinogenic chemicals.  SFs, which are expressed in
units of (mg/kg-day)"1,  are multiplied by the estimated intake of
a potential carcinogen, in mg/kg-day, to generate an upper-bound
estimate of the excess lifetime cancer risk associated with
exposure to the compound at that intake level.  The term "upper
bound" reflects the conservative estimate of the risks calculated
from the SF.  Use of this approach makes the underestimation of
the risk highly unlikely.  The SFs for the compounds of concern
are presented in Table 7.

For known or suspected carcinogens, EPA considers excess upper-
bound individual lifetime cancer risks of between 1CT4 to 10"6 to
be acceptable.  This level indicates that an individual has not
greater than a one in ten thousand to one in a million chance of
developing cancer as a result of site-related exposure to a
carcinogen over a 70-year lifetime under the specific exposure
conditions at the Site.  The total potential current and future
carcinogenic health risks for all pathways are summarized in
Table 8.  The total potential current and future carcinogenic
health risks from exposure to non-GCL property soil are: 9.2 x
10"6 for off-site children residents,  3.9 x 10"6 for off-site adult
residents, 1.4 x 10"5 for on-site workers, 4 x 10"6 for children
trespassers, and 4.2 x 10"6 for adult trespassers.  The potential
carcinogenic health risks from exposure to surface water is 3.5 x
10"6 and 1.7 x 10"5  for children and  adult trespassers,
respectively.  For surface-water sediments, the risk is 1 x 1CT5
for both children and adult trespassers.  The site groundwater is
not currently being used for human consumption, however, under a
hypothetical future use scenario the potential carcinogenic
health risk due to exposure to contaminated groundwater was
calculated.  For future children and adult residents the total
potential risk  (from site-related and upgradient contaminant
sources) is 1.1 x 10'1  and 1.4 x 10'1,  respectively.   For site-
related groundwater contamination only, the potential risks for
future children and adult residents are 2.8 x 1CT4 and 2.4 x 1CT3.
These risk numbers mean that approximately three persons out of
ten thousand and two persons out of one thousand respectively,
would potentially be at risk of developing cancer if exposed to
site-related contaminated groundwater over a lifetime.

Noncarcinogenic risks were assessed using a hazard index (HI)

                                8

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approach, based on a comparison of expected contaminant intakes
and safe levels of intake (Reference Doses).   Reference doses
(RfDs) have been developed by EPA for indicating the potential
for adverse health effects.   RfDs, which are expressed in units
of milligrams/kilogram-day (mg/kg-day),  are estimates, of daily
exposure levels for humans which are thought to be safe over a
lifetime (including sensitive individuals).  The reference doses
for the compounds of concern at the Site are presented in Table
7.  Estimated intakes of chemicals from environmental media
(e.g., the amount of a chemical ingested from contaminated
drinking water) are compared to the RfD to derive the hazard
quotient for the contaminant in the particular medium.  The HI is
obtained by adding the hazard quotients for all compounds across
all media that impact a particular receptor population.  An HI
greater than 1.0 indicates that the potential exists for
noncarcinogenic health effects to occur as a result of site-
related exposures.  The HI provides a useful reference point for
gauging the potential significance of multiple contaminant
exposures within a single medium or across media.

It can be seen from Table 8 that the His for noncarcinogenic
effects from ingestion, inhalation, and dermal contact to all
media (reasonable maximum exposure) are less than 1.0 for all
receptors, except for exposure to groundwater  (up to HI=497) and
exposure to surface water under current and future uses  (up to
HI=6).

Ecological Risk Assessment

A four-step process is utilized for assessing  site-related
ecological risks for a reasonable maximum  exposure scenario:
Problem  Formulation - a qualitative evaluation of contaminant
release, migration, and fate; identification of contaminants of
concern, receptors, exposure pathways, and known ecological
effects  of the contaminants; and  selection of  endpoints  for
further  study.  Exposure Assessment—a quantitative evaluation of
contaminant release, migration, and fate;  characterization of
exposure pathways and receptors;  and measurement or estimation of
exposure point concentrations.  Ecological Effects Assessment—
literature reviews, field studies, and toxicity tests, linking
contaminant concentrations to effects on ecological receptors.
Risk Characterization—measurement or estimation of both current
and  future adverse effects.

The  ecological risk assessment began with  evaluating the contami-
nants associated with the Site in conjunction  with the site-
specific biological species/habitat information.  Principal
ecological communities at the Site consist of  a deciduous wetland
area within the southern portion  of the -Site  (Unalam tributary),
and  an emergent wetland/open water complex (impoundment) to the
west of  the Site  (see Figure 2).  The wetland  areas support a
wide array of animal species, including 5  mammal species, 3 frog

                               . 9

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species, and 17 bird species.

This risk assessment evaluated the Site ecological communities
and their responses to toxicological exposures.   The threat of
lethal accumulations of contaminants in plant and animal
populations was evaluated.  The results of the ecological risk
assessment indicate the potential for ecological impacts due to
the presence of PAH contamination in the surface water and
sediments of the Unalam Tributary, drainage ditches, wetlands and
pond.  Since both aquatic plants and invertebrates form a portion
of the diets of wading birds and waterfowl, their diet poses a
potential exposure route.  Although adult mallard ducks subjected
to dietary exposure of levels similar to those found on Site
displayed no toxic effects, studies have shown significant
mortality and deformities in mallard embryos and ducklings
following exposure to similar levels of PAHs.  Therefore,
ingestion by breeding adult waterfowl may affect nesting success
in the wetland habitats present on and adjacent to the Site.

Uncertainties

The procedures and inputs used to assess risks in this
evaluation, as in all such assessments, are subject to a wide
variety of uncertainties.  In general, the main sources of
uncertainty include:

   environmental chemistry sampling and analysis
   environmental parameter .measurement
   fate and transport modeling
   exposure parameter estimation
   toxicological data

Uncertainty in environmental sampling arises in part from the
potentially uneven distribution of chemicals in the media
sampled.  Consequently, there is significant uncertainty as to
the actual levels present.  Environmental chemistry-analysis
error can stem from several sources including the errors inherent
in the analytical methods and characteristics of the matrix being
sampled.

Uncertainties in the exposure assessment are related to estimates
of how often an individual would actually come in contact with
the chemicals of concern, the period of time over which such
exposure would occur, and in the models used to estimate the
concentrations of the chemicals of concern at the point of
exposure.

Uncertainties in toxicological data occur in extrapolating both
from animals to humans and from high to.low doses of exposure, as
well as from the difficulties in assessing the toxicity of a
mixture of chemicals.  These uncertainties are addressed by
making conservative assumptions concerning risk and exposure

                               . 10

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parameters throughout the assessment.  As a result, the Risk
Assessment provides upper-bound estimates of the risks to
populations near the Site, and is highly unlikely to
underestimate actual risks related to the Site.

More specific information concerning public health risks,
including a quantitative evaluation of the degree of risk
associated with various exposure pathways, is presented in the
Risk Assessment Report.

Actual or threatened releases of hazardous substances from this
Site, if not addressed by implementing the response action
selected in the ROD, may present an imminent and substantial
endangerment to the public health, welfare, or the environment.

REMEDIAL ACTION OBJECTIVES

Remedial action objectives are specific goals to protect human
health and the environment.  These objectives are based on
available information and standards such as applicable or
relevant and appropriate requirements  (ARARs) and risk-based
levels established in the risk assessment.

The following remedial action objectives were established:

   >•  Prevent public and biotic exposure to contaminant sources
that present a significant threat  (contaminated groundwater and
surface-water sediments); and,

   *•'  Reduce the concentrations of contaminants in the groundwater
to levels which are protective of human health and the
environment  (e.g.. wildlife).

   > Prevent further migration of groundwater contamination.

DESCRIPTION OF REMEDIAL ALTERNATIVES

Section 121(b)(l) of CERCLA,.42 U.S.C. §9621(b)(l), mandates that
a  remedial action must be protective of human health and the
environment, be cost-effective, and utilize permanent solutions
and alternative treatment technologies or resource recovery
technologies to the maximum  extent practicable.  Section
121(b)(1) also establishes a preference for remedial actions
which employ, as a principal element, treatment to permanently
and significantly reduce the volume, toxicity, or mobility of the
hazardous substances, pollutants, and contaminants at a site.
Section 121(d) of CERCLA 42, U.S.C.  §9621(d), further specifies
that a remedial action must  attain a level or standard of control
of the hazardous substances, pollutants, and contaminants, which
at least attains ARARs under State and Federal laws, unless a
waiver can be justified pursuant to Section 121(d)(4) of CERCLA,
42 U.S.C. §9621(d)(4).

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In the spirit of the SACM initiative and relying on the Agency's
technology selection guidance for wood-treating sites,  EPA
considered technologies which have been consistently selected at
wood-preserving sites with similar characteristics (e.g..  types
of contaminants present, types of disposal practices,
environmental media affected) during the development of remedial
alternatives.  As referenced below, the time to implement a
remedial alternative reflects only the time required to construct
or implement the remedy and does not include the time required to
design the remedy, negotiate with responsible parties,  procure
contracts for design and construction, or conduct operation and
maintenance at the Site.

The alternatives developed for groundwater (GW) are discussed
below.

Alternative 1: No Action

Capital Cost:            Not Applicable
O & M Cost:              $27,200 for biannual monitoring
                         $20,000 each five-year review
Present Worth Cost:      $380,700 (over 30 years)
Implementation Time:     Not Applicable

The Superfund program requires that the No Action alternative be
considered as a baseline for comparison with other alternatives.
The No Action alternative for the contaminated groundwater would
only include a long-term monitoring program.  The contaminated
groundwater and DNAPL present in the subsurface would be left to
naturally attenuate without any treatment.  The long-term
monitoring program would consist of semiannual sampling for PAHs
at existing wells on-site and around the Site.  A 30-year
monitoring period was assumed for estimating the cost of this
alternative.  A total of six existing monitoring wells would be
utilized to sample the groundwater to determine whether the
concentrations of the contaminants of concern have been lowered
to cleanup levels through natural attenuation and to monitor the
migration of contaminants and free-phase DNAPL in areas
surrounding the Site.

Because this alternative would result in contaminants being left
on-site above health based levels, the Site would have to be
reviewed every five years for a period of 30 years per the
requirements of CERCLA.  These five-year reviews would include
the reassessment of human health and environmental risks due to
the contaminated material left on-site, using data obtained from
the monitoring program.
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Alternative GW-2, Option A: Extraction, on-site treatment via
activated carbon adsorption, and discharge to surface water

Capital Cost:            $1,883,100
0 & M Cost:              $603,300 per year
Present Worth Cost:      $9,369,400
Implementation Time:     24 months

The major features of this alternative are groundwater
extraction, collection, treatment, and discharge of treated
groundwater.  The treatment system would consist of an oil/water
separator, followed by pretreatment for manganese removal
(necessary to eliminate its potential interferences with
subsequent treatment processes) and removal of organic
contaminants by activated carbon adsorption.  The treated
groundwater would be discharged to the small unnamed stream
adjacent to the Site.  Although it is likely to take considerably
longer than 30 years to achieve remediation goals, the treatment
plant design and cost estimate is based on an operating period of
30 years.

The extraction/collection system would ,include a combination of a
collection trench for shallow groundwater and an extraction well
for the intermediate groundwater.  The trench would be
approximately. 700 feet long and would be located at the
northwestern  (downgradient) boundary of the Site.  It is
estimated that approximately 0.4 gallons per minute  (gpm) of
groundwater would be pumped from the collection trench, and
.approximately 26.4 gpm would be pumped from the extraction well
to the on-site treatment system.

In addition to groundwater extraction, if the DNAPL were  found to
be pumpable, DNAPL extraction wellpoints would be installed in
areas of suspected DNAPL.  It is envisioned that four wellpoints
would be installed in the shallow overburden and would have low
sustainable pumping rates  (less than 1 gpm in total).  Total flow
to the on-site treatment system would be approximately 30 gpm.
All pumping rates and numbers of wells would be refined during
the design phase based on pumping tests.  Extracted groundwater
would be delivered to a collection tank before treatment.

Because of the nature of the creosote contaminants and the
observation of DNAPL during field activities, oily product is
likely to be present with the extracted groundwater.  Heavy or
light product would be separated using an oil/water separator.
Solids and/or heavy product would settle by gravity into  the
separator's sludge hopper and would be removed periodically for
disposal to a permitted treatment facility.  Lighter product
would float to the surface and be removed by a skimmer for
disposal/reuse at a licensed off-site treatment/recycling
facility.
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The pretreatment system would consist of an individual treatment
train designed for the removal of manganese.  Manganese would be
removed through pH adjustment, oxidation, precipitation,
coagulation, clarification, neutralization, and filtration steps
with the addition of caustic, acid, and polymer.  Sludges
produced during this step would be stored in drums or rolloffs,
and sent out to an approved disposal facility.  Filtration may be
required to further pretreat the.effluent.

After pretreatment, groundwater would be pumped to a carbon
adsorption system consisting of two carbon beds connected in
series.  Organic contaminants (PAHs) would be removed by the
carbon adsorption units to target groundwater cleanup levels.
The spent carbon would be collected and shipped for off-site
disposal or regeneration and reuse.

Treated groundwater would be discharged via a culvert to the
small unnamed stream located on the southern border of the Site.
This stream in turn discharges to an unnamed tributary to Unalam
Creek, which eventually discharges to the Susguehanna River.  The
discharge structure would include appropriate erosion control
devices such as rip rap and energy dissipation features.  The
discharge would comply with the New York State Pollutant
Discharge Elimination System  (NYSPDES) requirements.  All waste
residuals generated from the treatment process would be
transported off-site to a permitted treatment and disposal
facility, or (in the case of carbon) to a recycling facility.

The goal of this alternative is to restore groundwater to
drinking water quality.  However, due to the characteristics of
creosote (e.q...., it is extremely viscous and difficult to pump)
and the complex hydrogeological setting, it is unlikely that this
goal would be achieved within a reasonable time frame for areas
containing the creosote layer (e.g.. shallow groundwater).
Current estimates of shallow groundwater remediation are on the
order of several hundred years.  As such, it is likely that
chemical-specific ARARs would be waived for those portions of the
aquifer based on the technical impracticability of achieving
further contamination reduction within a reasonable time frame.
If groundwater restoration were not feasible or practical, the
alternative may then focus on containing the extent of
groundwater. contamination within the Site boundaries.
Restoration of the groundwater outside the DNAPL source areas
fe.g.. intermediate groundwater) is likely to be feasible, since
it is mostly contaminated with mobile organic contaminants  (e.g.,
benzene).

During design or operation of the system, it may also be
determined that natural attenuation or enhanced biodegradation
(e.g.. introduction of air to increase the rate of
biodegradation) would be able to achieve a similar level of
contaminant removal and containment as groundwater extraction and

                                14

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treatment, but at a lower cost.  Such information would be
utilized during the remedial design to maximize the effectiveness
and efficiency of the system.  The information would also be used
to reassess the time frame and technical practicability of
achieving cleanup standards.

Alternative GW-2, Option B:  Extraction, on-site treatment via
biological treatment, and discharge to surface water

Capital Cost:            $2,058,600
0 & M Cost:              $626,500
Present Worth Cost:      $9,832,800
Implementation Time:     24 months

This option is virtually identical to Alternative 2, option A.
The only difference is that, following pretreatment, the
remaining contaminants in the groundwater would be pumped to an
aerobic biological reactor for treatment.  This reactor would
contain bacterial cultures capable of degrading the contaminants
in the groundwater.  Wastes  (e.g.. sludges) generated during the
treatment process would be disposed off-site at a permitted
disposal/treatment facility.

Alternative GW-3:  Extraction, on-site pretreatment, discharge to
publicly owned treatment works  (POTW) for final treatment

Capital Cost:            $1,904,000
O '& M Cost:              $6.13,.600
Present Worth Cost:      $9,518,200
Implementation Time:     24 months

The major features of this alternative are groundwater
extraction, collection, pretreatment and discharge to the local
POTW.  In order to comply with POTW influent requirements,
manganese would have to be removed from the groundwater.  This
would be accomplished by using conventional pretreatment methods
for manganese removal such as the treatment train described under
Alternative GW-2.  The extraction/collection system and
pretreatment for this alternative would also be the same as that
discussed for Alternative GW-2.  Therefore, only those operations
that differ from previous alternatives are discussed below.

Treatment of organic contaminants would be accomplished by the
Village of Sidney POTW utilizing a conventional sanitary
wastewater treatment process consisting mainly of aerobic
biodegradation.  The facility was designed for a maximum
wastewater treatment capacity of 1.7 million gallons per day
(MGD), and currently operates at an average capacity of 0.6 to
0.7 MGD.  Effluent from the pretreatment system would be
discharged to the sanitary sewer line via a metered control
manhole, which would record flow to the POTW.  The nearest
sanitary sewer is located parallel to Delaware Avenue,

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approximately 80 feet south of the roadway.

Groundwater would have to meet pretreatment requirements prior to
discharge to the POTW.  The Village of Sidney Municipal Code
governs sewer use within the Village and regulates the discharge
of wastes into the POTW.  The Village has indicated that final
acceptance of the pretreated GCL wastewater would not be
available until a detailed application is submitted.

As described under Alternative GW-2, due to the characteristics
of creosote and the complex hydrogeological setting, it is
unlikely that groundwater restoration would be achieved within a
reasonable time frame for areas containing the creosote layer
(e.g.. shallow groundwater).  The discussion of waiving chemical-
specific ARARs for a portion of the aquifer and/or containing the
groundwater contamination described for Alternative GW-2, would
similarly apply for GW-3.

The remedial alternatives developed for surface-water sediments
(SD) are discussed below.

Alternative SD-1:  No Action

Capital Cost:            $0
O & M Cost:              $18,900 for biannual monitoring
                         $20,000 for each five-year review
Present Worth Cost:      $277,700
Implementation Time:     6 months

The No Action alternative for the sediments at the GCL Site would
consist of a long-term monitoring program.  For cost-estimation
purposes, it is assumed that sediments would be monitored
semiannually and that eight sediment samples would be collected
and analyzed.

Because this alternative does not include contaminant removal,
the Site will have to be reviewed every five years for a period
of 30 years per the requirements of CERCLA, as amended.  These
five-year reviews would include the reassessment of human health
and environmental risks due to the contaminated material left on-
site, using data obtained from the monitoring program.

Alternative SD-2:  Excavation, treatment, and disposal with GCL-
property soils

Capital Cost:            $298,400
O & M Cost:              $0
Present Worth Cost:      $298,400
Implementation Time:     12 months

The contaminated sediments would be excavated during periods of


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no or low flow using conventional earth moving equipment such as
backhoes, bulldozers, etc.  Excavation would be performed under
moistened conditions to minimize the generation of fugitive dust.
Erosion and sediment control measures such as silt curtains would
be provided during excavation to control migration of
contaminated sediment.  Adjacent wetlands would be protected by
erosion and sediment control measures.

The sediments would be treated via thermal desorption along with
the GCL property soils as specified in the Record of Decision
dated September 30, 1994 for the Site.  A typical thermal
desorption process consists of a feed system, thermal.processor,
and gas treatment system (consisting of an afterburner and
scrubber or a carbon adsorption system).  Screened sediments are
placed in the thermal processor feed hopper.  Nitrogen or steam
may be used as a transfer medium for the vaporized PAHs to
minimize the potential for fire.  The gas would be heated and
then injected into the thermal processor which would operate at a
temperature of 700°F to 1000"F.  PAH contaminants of concern and
moisture in the contaminated sediments would be volatilized into
gases, then treated in the off-gas treatment system.  Treatment
options for the off-gas include burning in an afterburner
(operated to ensure complete destruction of the PAHs), adsorbing
contaminants onto activated carbon, or collection through
condensation followed by off-site disposal.  Thermal desorption
achieves approximately 98 to 99 percent reduction of PAHs in
soil.  If an afterburner were used, the treated off-gas would be
treated further in the scrubber for particulate and acid gas
removal.  A post-treatment sampling and analysis program would be
instituted in order to ensure that contamination in the
soil/sediment had been reduced to below cleanup levels.  The
treated sediment would be redeposited along with treated soils in
excavated areas on the GCL property.

Remedial activities will be conducted in a manner to minimize
impact to wetlands to the extent feasible.  The excavated areas
of the intermittent stream and wetlands edge would be backfilled
with clean material and restored to pre-excavation conditions.  A
wetland restoration plan will be prepared for any wetlands
impacted or disturbed.  The restoration would take place as soon
as practicable after the sediments have been excavated, in order
to minimize the period of impact to the stream and wetland.  All
applicable wetlands management guidelines would be followed.

The total volume of sediments to be excavated is estimated to be
125 cy.  Further delineation of the extent of contamination will
be conducted during the remedial design phase.
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Alternative SD-3:  Excavation and off-site disposal

Capital Cost:            $820,300
O & M Cost:              $0
Present Worth Cost:      $820,300
Implementation Time:     6 months

This alternative consists of excavation of 125 cy contaminated
sediment as described in Alternative SD-2 and transportation of
all contaminated materials to an off-site RCRA permitted facility
for treatment and disposal.  One hundred twenty-five cy of clean
fill would be used to restore excavated areas.  Wetlands would be
restored as discussed in Alternative SD-2.

SUMMARY OF COMPARATIVE ANALYSIS OF ALTERNATIVES

In selecting a remedy, EPA considered the factors set out in
section 121 of CERCLA, 42 U.S.C. §9621, by conducting a detailed
analysis of the viable remedial alternatives pursuant to the NCP,
40 CFR §300.430(e)(9) and OSWER Directive 9355.3-01.  The
detailed analysis consisted of an assessment of the alternatives
against each of nine evaluation criteria and a comparative
analysis focusing upon the relative performance of each
alternative against those criteria.

The following "threshold" criteria must be satisfied by any
alternative in order to be eligible for selection:

1.   Overall protection of human health and the environment
     addresses whether or not a remedy provides adeguate
     protection and describes how risks posed through each
     exposure pathway (based on a reasonable maximum exposure
     scenario) are eliminated, reduced, or controlled through
     treatment, engineering controls, or institutional controls.

2.   Compliance with ARARs addresses whether or not a remedy
     would meet all of the applicable  (promulgated by a State or
     Federal authority), or relevant and appropriate requirements
     (that pertain to situations sufficiently similar to those
     encountered at a Superfund site such that their use is well
     suited to the site) of State and Federal environmental
     statutes or provide grounds for invoking a waiver.

The following "primary balancing" criteria are used to make
comparisons and to identify the major trade-offs between
alternatives:

3.   Long-term effectiveness and permanence refers to the ability
     of a remedy to maintain reliable protection of human health
     and the environment over time, once cleanup goals have been
     met.  It also addresses the magnitude and effectiveness of
     the measures that may be required to manage the risk posed

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     by treatment residuals and/or untreated wastes.

4.    Reduction of toxicity, mobility,  or volume through treatment
     refers to a remedial technology's expected ability to reduce
     the toxicity, mobility, or volume of hazardous substances,
     pollutants, or contaminants at the site.

5.    Short-term effectiveness addresses the period of time needed
     to achieve protection and any adverse impacts on human
     health and the environment that may be posed during the
     construction and implementation periods until cleanup goals
     are achieved.

6.    Implementabi 1 itv refers to the technical and administrative
     feasibility of a remedy, including the availability of
     materials and services needed.

7.    Cost includes estimated capital, operation and maintenance
     costs, and the present-worth costs.

The following "modifying" criteria are considered fully after the
formal public comment period on the Proposed Plan is complete:

8.    State acceptance indicates whether, based on its review of
     the RI/FS and the Proposed Plan, the State supports,
     opposes, and/or has identified any reservations with the
     preferred alternative.

9.    Community acceptance refers to the public's general response
     to the alternatives described in the Proposed Plan and the
     RI/FS reports.  Community acceptance factors to be discussed
     below include support, reservation, and opposition by the
     community.

A comparative analysis of the remedial alternatives based upon
the evaluation criteria noted above follows.

Groundwater

  •>  Overall Protection of Human Health and the Environment

Over time, Alternative GW-1 would provide some limited protection
of human health and the environment since contaminants would be
attenuated through natural processes  (e.g.. biodegradation,
dispersion).  However, it is unlikely that full restoration of
groundwater resources would be achieved.  Alternatives GW-2 and
GW-3 would be protective of human health and the environment,
since they would actively reduce the toxicity, mobility, and
volume of contaminants in the groundwater, and would protect
groundwater surrounding the GCL site from further contamination.
Although GW-2 and GW-3 would result in significant reduction in
the mass of contaminants present in the aquifer, it is unlikely

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that full restoration of groundwater resources would be achieved
within a reasonable time frame.

  +  Compliance with ARARs

Alternative GW-1 would not comply with Federal or State drinking
water standards or criteria or those ARARs required for
protection of groundwater.  Alternatives GW-2 and GW-3 would be
designed to treat the aquifer to chemical-specific ARARs
associated with State and Federal groundwater and drinking water
standards.  Extracted groundwater would be treated to achieve
NYSPDES requirements under Alternative GW-2; under Alternative
GW-3 the extracted groundwater would be treated to local
pretreatment standards prior to discharge to the POTW.  Each of
these alternatives would be capable of removing a significant
mass of contaminants in the groundwater.  The goal of these
alternatives is to restore groundwater to drinking water
standards.  However, due to the characteristics of creosote and
the complex hydrogeological setting, it is unlikely that this
goal will be achieved within a reasonable time frame for areas
containing the creosote layer  (e.g.. shallow groundwater).
Current estimates of DNAPL remediation are on the order of
several hundred years.  As such, it is likely that chemical-
specific ARARs will be waived for those portions of the aquifer
based on the technical impracticability of achieving further
contamination reduction within a reasonable time frame.

  *•' Lona-Term Effectiveness and Permanence

Alternative GW-1 would not provide  for active treatment and would
rely on natural attenuation processes to restore the contaminated
aquifer.  Therefore, this alternative would not be an effective
long-term remedy.

Alternatives GW-2 and GW-3 would reduce the potential risk
associated with contaminated groundwater by extracting and
treating the groundwater to remove  a significant mass of
contaminants from the aquifer.  The time to achieve these risk
reductions is limited by the effective extraction rates from the
aquifer.  However, it is unlikely that DNAPL contamination
present in the shallow aquifer can  be completely remediated due
to the tendency of DNAPLs to attach to the aquifer.  Although
none of the alternatives would be able to clean the aquifer to
drinking water standards in a short period of time, the treatment
alternatives would protect surrounding groundwater from further
contamination.

  *•  Reduction in Toxicity. Mobility, or Volume Through Treatment

Alternative GW-1 would not involve  any removal or active
treatment of the contaminants in the aquifer; therefore, would
not be effective in reducing the mobility, toxicity, or volume of

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contaminants.  However, over time, natural attenuation processes
would provide some reduction of the toxicity and volume of
contaminants.

Alternatives GW-2 and GW-3 would reduce the toxicity, mobility
and volume of contaminants in the aquifer to a larger extent than
GW-1, since extraction and treatment of groundwater are provided.

  »•  Short-Term Effectiveness

The implementation of Alternative GW-1 would result in no
additional risk to the community during remedial activities,
since no construction or remediation activities would be
conducted.  Workers  involved in periodic sampling of site soils
would be exposed to  minimal risks because appropriate health and
safety protocols would be followed for this activity.  For
purposes of  this analysis, monitoring of the Site would occur for
30 years.

Alternatives GW-2 and GW-3 involve construction and operation of
an on^-site treatment plant.  Procedures for proper handling of
the treatment reagents would be followed for all treatment
alternatives.  Any process residuals generated would be properly
handled and  disposed off-site.  The risk to workers involved in
the remediation also would be minimized by establishing
appropriate  health and safety procedures and preventive measures
to avoid direct contact with contaminated materials and
ingestion/inhalation of fugitive  dust.  All site workers would be
OSHA-certified and would be instructed to follow OSHA protocols.

It is estimated that the treatment alternatives would take well
over 30 years to achieve the remedial action objectives.
However, a 30-year period was used for cost estimation.
Operation of the treatment plant  would be stopped when remedial
objectives are achieved i.e.. levels of contaminants in the
aquifer are  reduced  to State and  Federal drinking water
standards, unless it is determined that ARARs would be waived in
portions of  the aquifer.

  *•  Impl ementabil itv

Alternative  1 would  not involve any major site activities other
than monitoring and  performing five-year reviews.  These
activities are easily  implemented.

The treatment components of Alternatives GW-2 and GW-3 would be
easily implemented,  as the technologies are proven and readily
available.   The carbon adsorption technology proposed for use in
Alternative  GW-2A is a proven and efficient method for removal of
organic contaminants.  Biological treatment, specified in
Alternatives GW-2B and GW-3, has  been used successfully for
groundwater  contaminated with creosote wastes.  The manganese

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removal pretreatment technology required under Alternatives GW-2
and GW-3 is proven and readily available.  Sufficient space is
available on-site for a treatment plant.

Alternatives GW-2 and GW-3 would require institutional management
of the operation and maintenance of the treated groundwater
discharge system.  Off-site disposal facilities are available for
the disposal of the oil/water separator sludge and skimmings
generated from Alternatives GW-2 and GW-3.  Disposal (or recycle)
facilities are also available for recovered DNAPL and the other
residues generated from those alternatives.

Alternatives GW-2A and GW-2B both provide for discharge to the
small stream located at the Site's southern border.  Based on the
review of the treated groundwater discharge requirements for the
Route 8 Landfill site and the successful operation of the
groundwater remediation system at this site, discharge to the
stream is expected to be readily implementable for Alternative
GW-2.

The Village of Sidney expressed its interest in having the
pretreated groundwater transmitted to the local POTW as described
under Alternative GW-3.  There is a degree of uncertainty,
however, as to whether final approval would be granted which
would be contingent upon factors such, as available capacity,
waste characteristics, and POTW permit requirements concerning
effluent and sludge quality.  Due to this uncertainty, this
alternative is considered less implementable than Alternative
GW-2.                                        '

  >  Cost

GW-1 is the least expensive of all alternatives but would not
involve treatment.  Alternative 1 has a present worth cost of
$380,700 which is associated with conducting a sampling and
analysis program and five-year reviews over a 30-year period.

Alternative GW-2A would be the most expensive treatment
alternative followed by GW-3 and GW-2B.  However, the cost
differences between GW-2A, GW-2B and GW-3 would be so small as to
not be significant.

  >  State Acceptance

The New York State has concurred with the selected remedy.

  *•  Community Acceptance

No objections by the community were raised concerning the
selected remedy.  The Village of Sidney has requested that EPA
select Alternative GW-3 which includes discharge of the
pretreated groundwater to the local POTW.  A responsiveness

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summary which addresses all comments received during the public
comment period is attached as Appendix IV.

Sediments

  »•  Overall Protection of Human Health and the Environment

Alternative SD-1 would not meet any of the remedial objectives
and thus would not be protective of the environment.
Contaminated sediments would remain on-site and would continue to
pose a risk to the biota.  Natural flushing would reduce
contaminants in the  sediments somewhat, especially after the
contaminated soils on the GCL-property are remediated.

Alternative SD-2, involving on-site sediment treatment and
Alternative SD-3 involving off-site treatment/disposal of
sediments, would remove contamination and eliminate any
environmental threats posed by the sediments.  Therefore, these
alternatives would meet remedial objectives. .

  >  Compliance with ARARs

There are no chemical-specific ARARs for the contaminated
sediments.  Alternative SD-1 would comply with appropriate
requirements such as New York State Technical and Administrative
Guidance Memoranda.

Alternatives SD-2 and SD-3 would be designed and implemented to
.satisfy all. appropriate requirements and location-specific ARARs
identified for the Site.  Excavation activities would be
conducted in compliance with the OSHA standards, soil erosion,
sediment control and wetland protection requirements.
Alternative SD-2 also would comply with ARARs related to on-site
treatment  (e^g^., disposal of treatment residuals, stormwater
discharge requirements and air pollution control regulations
pertaining to fugitive emissions and air quality standards).
Under Alternative SD-3, excavated sediments would be sent to an
appropriate treatment/disposal facility in accordance with
applicable ARARs.

  +  Long-Term Effectiveness

Alternative SD-1 would monitor contamination in the sediments and
would not remove and/or treat contaminants.  Therefore, this
alternative would not reduce the long-term risks to the
environment associated with the sediments.

Alternative SD-2 calls for on-site sediment treatment along the
GCL-property soils.  The soil treatment.system would reduce the
levels of PAH contaminants in sediments by 98 to 99 percent.

Alternative SD-3 would provide long-term protection by removing

                                23

-------
the contaminated sediments which would be sent to an approved
disposal facility.  Soil cover and revegetation would provide
protection against erosion.  No long-term monitoring would be
required.

  »•  Reduction of Toxicity. Mobility, or Volume Through Treatment

Alternative SD-1 would not provide immediate reduction in
toxicity, mobility, or volume of contaminants because treatment
is not included as part of this alternative.  Some reduction may
be realized after the GCL-property soils have been remediated
through natural attenuation processes.

Alternatives SD-2 and SD-3 would reduce the toxicity, mobility,
and volume of contaminants by removal and on-site treatment
(Alternative SD-2) or off-site disposal (Alternative SD-3).

  >•  Short-Term Effectiveness

The implementation of Alternative SD-1 would not pose any
additional risks to the community, since this alternative does
not involve any construction or remediation.  Workers involved in
periodic sampling of sediments would be exposed to minimal risks
because appropriate health and safety protocols would be followed
for this activity.

Alternatives SD-2 and SD-3 include activities such as excavation,
screening, shredding, and handling of contaminated sediments
which could result in potential exposure of workers and residents
to fugitive dust, and possible suspension of sediments.  In order
to minimize potential short-term impacts, the area would be
secured and access would be restricted to authorized personnel
only..  In addition, dust control measures such as wind screens
and water sprays would be used to minimize fugitive dust
emissions from material handling.  The risk to workers involved
in the remediation would also be minimized by establishing
appropriate health and safety procedures and preventive measures,
(e.g.. enclosed cabs on backhoes and proper personal protection
equipment) to prevent direct contact with contaminated materials
and ingestion/inhalation of fugitive dust.  All site workers
would be OSHA certified and would be instructed to follow OSHA
protocols.  Some increase in traffic and noise pollution would be
expected from site activities.  Short-term impacts may be
experienced for about a six-month period which is the estimated
time for construction and remedial activities.

Under Alternatives SD-2 and SD-3, short-term impacts on the
environment from removal of vegetation and destruction of habitat
could occur.  A plan would be prepared and implemented to
minimize and restore (i.e.. revegetate) any damage to the
environment.  Erosion and sediment control measures such as silt
curtains and berms would be provided during material handling

                                24

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activities to control migration of contaminants.

  »•  Implementabilitv

Alternative SD-1 would not involve any major site activities
except monitoring and sampling.  These activities would be easily
implementable.

Alternative SD-2 would be easily implemented, as the technology
is proven and readily available.  The thermal desorption
component of this alternative has been shown to be effective for
destruction of PAHs, and is commercially available.  Sufficient
land is available at the Site for operation of a mobile thermal
desorption system and supporting facilities.  Alternative SD-3
involves pff.-site disposal.  Capacity for the small volume of
sediment should be available at a permitted facility.
Implementation of Alternatives SD-2 and SD-3 would require
restriction of access to the Site during the remediation process.
Coordination with state and local agencies would also be required
during remediation.

  *•  Cost

Alternative SD-1 is the less expensive alternative, but does not
provide treatment of contaminated sediments..  Alternative SD-1
has a present worth cost of $277,700 which  is associated with
conducting a sampling and analyses program and  five-year reviews
over a 30-year period.

Alternative SD-2 is the least expensive of the  treatment
alternatives and has a present worth cost of $298,000.  The most
expensive Alternative is SD-3 with a present worth cost of
$820,300.

  >  State Acceptance

The New York State has concurred with the selected remedy.

  *•  Community Acceptance

No objections from the community were raised regarding the
selected surface-water sediment portion of the  remedy.

SELECTED REMEDY

EPA and NYSDEC have determined, after reviewing the alternatives
and public comments, that Alternatives GW-2 and SD-2 are the
appropriate remedies for the Site, because they best satisfy the
requirements of Section 121 of CERCLA, 42 U.S.C. §9621, and the
NCP's nine evaluation criteria for remedial alternatives, 40 CFR
§300.430(e)(9).  The total capital costs of the groundwater
portion of the remedy are $1.9 million for GW-2A and $2.1 million

                                25

-------
for GW-2B; the operation and maintenance cost is $0.6 million a
year for both GW-2A and GW-2B; the present worth cost are $9.4
million for GW-2A and $9.8 million for GW-2B.  The total capital
cost of the surface-water sediment portion of the remedy is $0.3
million; no l.ong-term operation and maintenance costs are
expected.

The major components of the selected remedy are as follows:

•    Extraction, collection, and on-site treatment of groundwater
     contaminated with organic compounds; discharge of treated
     groundwater to the surface water.  The selected remedy
     provides two options for primary treatment of organics:
     carbon adsorption or biological treatment.

     Information will be obtained during the remedial design to
     reassess the time frame and technical practicability of
     achieving State and Federal drinking water standards in the
     aquifer.  Should the remedial design data indicate that
     groundwater .restoration through extraction and treatment is
     feasible and practical, additional work will be conducted to
     determine which groundwater treatment option (carbon
     adsorption or biological treatment) is more appropriate and
     cost-effective.  If groundwater restoration is not feasible
     or practical, the remedy will then focus on containing the
     groundwater contamination within the GCL property boundaries
     in which case chemical-specific ARARs may be waived for all
     or some portions of the aquifer based on the technical
     impacticability of achieving further contamination reduction
     within a reasonable time frame.  Under such a scenario, it
     may be determined that natural attenuation or enhanced
     biodegradation  (e.g.. introduction of air to increase the
     rate of biodegradation) would be able to reduce the
     concentration of contaminants in the aquifer groundwater to
     levels which are similar to those achievable under
     extraction and treatment, but at a lower cost.  Such
     information would be utilized during the remedial design to
     maximize the effectiveness and efficiency of the system;
     and,

•    Excavating and treating contaminated sediments on-site
     through a thermal desorption process along with the GCL-
     propefty soils.  The selected remedy will also provide for
     the mitigation of damages to the aquatic environment which
     may occur during implementation  (i.e.. revegetation).

In addition, EPA will recommend to local agencies that
institutional control measures be undertaken to ensure that
future land use of the property continues to be
industrial/commercial, and precludes the use of Site groundwater
for human consumption until drinking water quality is restored in
the aquifer.

                                26

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Remedial Goal

The goal of the groundwater portion of the remedy is to restore
groundwater to drinking water quality.  However, due to the
characteristics of creosote (e.g.,  extremely viscous and
difficult to pump) and the complex hydrogeological setting, it is
unlikely that this goal will be achieved within a reasonable time
frame for areas containing the creosote layer (e.q_,._, shallow
groundwater).  Current estimates of shallow groundwater
remediation are on the order of several hundred years.  As such,
it is likely that chemical-specific ARARs will be waived for
those portions of the aquifer based on the technical
impracticability of achieving further contamination reduction
within a reasonable time frame.  If groundwater restoration is
not feasible or practical, the alternative may then focus on
containing the extent of groundwater contamination within the
site boundaries.  Restoration of the groundwater outside the
DNAPL source areas  (e.g.. intermediate groundwater) is likely to
be feasible, since it is mostly contaminated with mobile organic
contaminants (e.g.. benzene).  The treated effluent will meet
NYSPDES requirements.

During design or operation of the system, it may also be
determined that natural attenuation or enhanced biodegradation
(e.g.. introduction of air to increase the rate of
biodegradation) would be able to achieve a similar level of
contaminant removal and containment as groundwater extraction and
treatment, but at a lower cost.  Such information would be
utilized during the remedial design to maximize the effectiveness
and efficiency of the system.  The information would also be used
to reassess the time frame and technical practicability of
achieving cleanup standards.

The goal of the sediment excavation and treatment  is to
eliminated potential threats to the aquatic environment due to
the presence of elevated concentrations of organic contaminants.

STATUTORY DETERMINATIONS

As previously noted, Section 121(b)(1) of CERCLA,  42 U.S.C.
§9621(b)(l), mandates that a remedial action must be protective
of human health and the environment, be cost-effective, and
utilize permanent solutions and alternative treatment
technologies or resource recovery technologies to the maximum
extent practicable.  Section 121(b)(1) also establishes a
preference for remedial actions which employ treatment to
permanently and significantly reduce the volume, toxicity, or
mobility of the hazardous substances, pollutants, or contaminants
at a site.  Section 121(d) of CERCLA, 42 U.S.C. §9621(d),  further
specifies that a remedial action must attain a degree of cleanup
that satisfies ARARs under State and Federal laws, unless a
waiver can be justified pursuant to section 121(d)(4) of CERCLA,

                                27

-------
42 U.S.C. §9621(d)(4).  As discussed below, EPA has determined
that the selected remedy meets the requirements of -section 121 of
CERCLA, 42 U.S.C. §9621.

Protection of Human Health and the Environment

The selected remedy is considered fully protective of human
health and the environment.  Extraction and treatment of
groundwater through the implementation of Alternative GW-2 will
reduce the toxicity, mobility, or volume of contaminants in the
groundwater and result in overall protection of human health and
the environment.  If groundwater restoration is not feasible or
practical, and the selected remedy focusses on containing the
extent of groundwater contamination, the remedy will reduce the
mobility of contaminants in groundwater and result in overall
protection of human health and the environment.  Prior to
discharge, the groundwater will meet all state (e.g.. NYSPDES)
and/or federal discharge standards.  Alternative SD-2, the
excavation and treatment of the contaminated surface-water
sediments through a thermal desorption process, will remove the
organic contaminants from the surface-water sediments.  Treatment
of the surface-water sediments will result in the elimination of
the ecological threats posed by these sediments.

Compliance with ARARs

The selected groundwater remedy, Alternative GW-2, may not be
able to comply with associated chemical-specific ARARs for at
least some portions of the aquifer  (e.g..  shallow aquifer) within
a reasonable time frame.  Therefore, it is likely that chemical
specific-ARARs will be waived for those porions of the aquifer
based in technical impracticability.  However, the treatment
system with meet other ARARs, including:

Action-Specific ARARs:

•    RCRA - Land Disposal Restrictions

•    RCRA - Standards Applicable to Transport of Hazardous Waste

•    RCRA - Standards for Owners/Operators of Permitted Hazardous
     Waste Facilities

•    RCRA - Preparedness and Prevention

•    RCRA - Contingency Plan and Emergency Procedures

•    DOT - Rules for Transportation of Hazardous Materials

•    New York State Hazardous Waste Manifest System Rules

•    New York State Hazardous Waste Treatment Storage and

                               .28

-------
     Disposal facility Permitting Requirements
•    New York State Pollutant Discharge Elimination System
     Requirements
•    OSHA - Safety and Health Standards
•    OSHA - Record-keeping, Reporting and Related Regulations
Chemical-Specific ARARs:
•    New York State Groundwater Standards
Location-Specific ARARs:
•    Clean Water Act - Wetland Protection
The selected surface-water sediment remedy, Alternative SD-2,
will meet all ARARs, including:
Action-Specific ARARs:
•    RCRA - Land Disposal Restrictions
•    RCRA - Standards Applicable to Transport of Hazardous Waste
•    RCRA - Standards for Owners/Operators of Permitted Hazardous
     Waste Facilities
•    DOT - Rules for Transportation of Hazardous Materials
•    New York State Hazardous Waste Manifest System Rules
•    New York State Hazardous Waste Treatment Storage and
     Disposal facility Permitting Requirements
•    New York State Pollutant Discharge Elimination System
     Requirements
•    OSHA - Safety and Health Standards
•    OSHA - Record keeping, Reporting and related Regulations
•    Clean Water Act - Wetland Protection
Chemical-Specific ARARs:
•    None
Location-Specific ARARs:
•    Clean Water Act - Wetland Protection
                                29

-------
A full list of ARARs and TBCs (e.g., advisories, criteria, and
guidance) being utilized is provided in Table 9.

Cost-Effectiveness

The selected remedy is cost-effective in that it provides overall
effectiveness proportional to its cost.  The total capital costs
of the groundwater portion of the remedy are $1.9 million for GW-
2A and $2.1 million for GW-2B; the operation and maintenance cost
is $0.6 million a year for both GW-2A and GW-2B; the present
worth cost are $9.4 million for GW-2A and $9.8 million for GW-2B.
The total capital cost of the surface-water sediment portion of
the remedy is $0.3 million; no long-term operation and
maintenance costs are expected.  A breakdown of the costs
associated with the selected remedy is provided in Table 10.

Utilization of Permanent Solutions and Alternative Treatment (or
Resource Recovery) Technologies to the Maximum Extent Practicable

The selected remedy utilizes permanent solutions and treatment
technologies to the maximum extent practicable.  The groundwater
portion of the selected remedy will reduce the toxicity,
mobility, and volume of contaminants in the groundwater
underlying the Site and prevent further degradation of the area
groundwater.  The selected remedy employs permanent treatment of
the PAH-contaminated surface-water sediments on the Site through
excavation, treatment and disposal with GCL-property soils.  The
potential for direct and indirect threats to human health and the
environment will be eliminated.  The selected remedy represents
the best balance of trade-offs among the alternatives with
respect to the evaluation criteria.

Preference for Treatment as a Principal Element

In keeping with the statutory preference for treatment as a
principal element of the remedy, the remedy provides for the
treatment of contaminated groundwater and surface-water sediments
which constitute the remaining threats known to exist at the
Site.

DOCUMENTATION OF SIGNIFICANT CHANGES

There are no significant changes from the preferred alternative
presented in the Proposed Plan.
                               . 30

-------
APPENDIX I




 FIGURES

-------
Figure 1.  GCL Tie & Treating She Location M£=




-------
lluii:
iila I «yoi4 MI^I nn Aiitfinl 100.1 iwAilpl'"l'MI'"l>l1 Hhl«*!i»»
                                           lUUil. Ililuhei 111115,
   ai IOM,U»/ turr M
                         i lon;i.
                                                                                                          u.s.  F.Nviin)NMri-irAi.
                                                                                                                     GCI.  in:  .v  i HI.A i IMC.  :,iu
                                                     II     «liO    000 I;T.
                                                        lAI'I'IIOX.)
                                                                                                                       IIIS'IOI^ICAI.  I.AHD l-ril.

                                                                                                                          Sill!  I.AVOHI  MAI'

-------
            Figure 3. ••  1'utcnClul  lixtent  of Jjurfaco-w.itei: Sediment  Cont;im:l.ii;itJon
            "••	   	"	      "           	"	~	.""t	   ;              	   .""
                                                                                                    f| M
                                                                                                      Mt
 t
. f U
•(I,.
   '

                                                                 IO     II
                                                                                                      It     17     It      |>

-------
lr Igure 4      PuleullaJ.  ijxU^'i
      .
                                               ol  Groinulwalei' ('on Lc'imina lion
             m
       /
                                                                                                                    n n< ir*»mi w4> uitwi c
                                                      5i~~"^'-V.'Ur~-^°'J~=s"~r^—•• _^y=^-~j=a
I
                                                                                                                                                 OCI Iff • TMAIIM
                                                                                                                                               UI>T> nincta tM^o
                                                                                                                                                  -j~.:.a
                                                                                                                                                        IE

-------
APPENDIX II




  TABLES

-------
TABLE 1: SUMMARY OF NON-GCL PROPERTY SOILS ANALYTICAL RESULTS
(All values in parts per million [ppm])
CONTAMINANT
Volatile Organics
Tricaloroethene
Toluene
Total Volatiles
HIGHEST CONCENTRATION

0.01
0.024
0.042
Polyaroniatic Hydrocarbons
Fluoranthene
Pyrene
Benzo[a]anthracene
Chrvsene
Benzo[b]fi.uoranthene
Benzo[k]fluoranthene
Benzo[a]pyrene
Total PAHs
9.5
6.3
1.5-
2.7
3.2
3.2
2.9
24
Metals
AltTmTmm
Arsenic
Beryllium.
Cadmium
Chromium
Copper
Lead
Nickel
Zinc .
14.300
10.4
3.2
0.91
20.8
176
46
29.6
78.9
 Benchmark levels for comparison are NYSDEC soil cleanup objectives (VOCs only), background levels (metals
 only), and risk-based cleanup levels for industrial use (PAHs only, consistent with Record of Decision for
 Operable Unit 1).

-------
TABLE 2: SUMMARY OF SURFACE WATER ANALYTICAL RESULTS
(All values in parts per billion [ppb])
CONTAMINANT
Arsenic
Copper
Maneanese
Nickel •
Zinc
BENCHMARK LEVEL FOR
COMPARISON
0.018
12
Not available
6.1
110
HIGHEST .
CONCENTRATION
11.4
35.2
8.710
19.6
116
Benchmark levels for comparison are the lower value for that contaminant from either USEPA water quality
criteria or NYSDEC ambient water standards.

-------
TABLE 3: SUMMARY OF SURFACE-WATER SEDIMENT ANALYTICAL RESULTS
(All values in parts per billion [ppb])
CONTAMINANT
BENCHMARK LEVEL
FOR COMPARISON
HIGHEST
CONCENTRATION
Polvaromatic Hydrocarbons
Benzo[a]anthracene
Chrvsene
Benzo[b]fluoranthene
Benzo[k]fluoranthene
Benzo[a]pyrene
Indeno[1.2,3-cd]pyrene
Total PAH
20.8
20.8
20.8
20.8
20.8
8.8 •'
Not available
2.200
4.000
4.300
3,100
1.700
1,100
23.850
Metals
Arsenic
Chromium
Copper
Lead
Manganese
Mercury
Nickel
Zinc
5,000
26,000
19,000
27,000
428,000
110
22,000
85,000
16,400 :
32,000
51,900
70,200
547,000
690
43,600
173;000
 Benchmark levels for comparison are the lower value for that contaminant from either USEPA criteria for
 aquatic sediments (human health basis criteria) or NYSDEC sediment criteria.

-------
TABLE 4:  SUMMARY OF GROUNDWATER ANALYTICAL RESULTS
(All values in parts per billion [ppb])
CONTAMINANT
Volatile Organics
Vinyl chloride
Chloroethane
Methvlene chloride
1,1-Dichloroethene
1, 1-Dichloroethane
cis-1.2-Dichloroethene
Trichloroethene
Benzene
BENCHMARK LEVEL
FOR COMPARISON

2
5
5
7
5
70
5
5
WELLS INFLUENCED
BY ROUTE 5 LANDFILL
CONTAMINATION
[Highest Concentration]
ALL SAMPLES EXCEPT
WELLS INFLUENCED BY
ROUTE 8 LANDFILL
CONTAMINATION
[Highest Concentration]

4,700
19
25
17
1,200
4,300
1.000
9



8
15
36
48 :
220 :
Polyaromatic Hydrocarbons
Benzo[a]anthracene
Chrysene
Benzo [b]fluoranthene
Benzo[k]fluoranthene
Benzo [alpyrene
Indeno[l,2,3-cd]pyrene
0.1
.0.2
0.2
0.2
0.2
0.4






6
4 :..
3
2
2
0.7
Metals
Alurp'i'nuTi
Antimony
Arsenic
Chromium
Iron.
Manganese
Nickel
50
6
50
100
50
50
100
6,210
10
51.1 .
166
15,400
3,360
131
2.230
44.3
7.8
40.7
37,600
17,600
74.2
 Benchmark levels for comparison are taken from USEPA and NYSDOH drinking water MCLs. Blank spaces
 denote a value below Analytical detection limit.

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Table 5: Chemicals of Potential Concern
Croundwater

Acetone
Benzene
2-Butanone
Carbon tetrachloride"
Chlorobenzene*
Chloroform
Chloroethane"
•1,2 Dichlorobenzene
1,1 Dichloroethane
1,2 Dichloroethane"
1,1-Dichloroethene
cis-1,2 Dichloroethene
trans-1,2 Dichloroethene"
Ethyl benzene
Methylene chloride*
4-Methyl-2-pentanone
Styrene
Tetrachloroethene"
Toluene
 1,1,1-Trichloroethane
 1,1,2-Trichloroethane"
Trichloroethene
Vinyl chloride
 Xylenes
 Acenaphthene
 Anthracene
 Benzo(a)anthracene
 Benzo(b)flouranthene
 Bis(2-ethylhexyl)phthalate
 Chrysene
 Fluoranthene
 Fluorene
 2-Methy I naphtha lene"
 2-Methylphenol
 4-Methylphenol
  Naphthalene
  Phenol
  Pyrene.
 Aldrin
  Alpha BHC
  beta BHC-
  gamma BHC
  Chlordane
  ODD*
  DDE
  Dieldrin
  Endrin
  Heptachlor epoxide
Antimony
Arsenic"
Barium*
Chromium
Copper
Manganese
Nickel
Selenium
Silver
Vanadium
Zinc
Soil

Acenaphthene
Anthracene
Benzene
Benzo(a)anthracene
Benzo(a)pyrene
Benzo(b)f 1 uoranthene
Benzo(k)f I uoranthene
Bis(2-ethylhexyl)phthalate
Chrysene.
DDT
 Dibenz(a,h)anthracene
Ethylbenzene
 Flouranthene
 Fluorene
 Indeno (1,2,3-cd)pyrene
 Methoxychlor
 4-Methylphenol
 Naphthalene
 PCBs
 Pyrene
 Styrene
 Toluene
 Xylenes
Surface Water

Arsenic
Barium
Chloroethane
Chromium
Copper
Manganese
Nickel
Selenium
Zinc
Sediment

Acenaphthene
Aldrin
Anthracene
Benzo(a)anthracene
Benzo(a)pyrene
Benzo(b)f I uoranthene
Benzo(k)f j uoranthene
Bis(2-ethylhexyl)phthalate
Chlordane
4-Chloro-3-Methylphenol
2-Chlorophenol
Chrysene
DDT
2,4-Dinitrotoluene
Endosulfan
Fluoranthene
Indenod ,2,3-cd)pyrene
Methylene Chloride
PCBs
Pentachlorophenol
 Phenol
 Pyrene
  * Not a contaminant of concern when Route 8 Landfill wells are excluded.

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                                                                     Table  6
                         GCL Tic & Treating Itl/FS Risk Assessment Potential Kxposurc Pathways
  PRIMARY SOURCE     SECONDARY SOURCE
   act
PRODUCTION —^- SPILL/  -
 ACTIVITIES   DISCHARGE
                          SOIL
                          WATER
                                                    TERTIARY SOURCE
                                   STORM WATER
                                     RUN-OFF
                                            •>- SEDIMENT -3
                                   PERCOLATION/
                                   INFILTRATION
                                                                        SOIL
                                                                       SURFACE WATER
                                                                   ->• SEDIMENT
                                                         INFILT RATION f
                                                         PERCOLATION
                                                                       GROUNDWATER
 INGESTION
 DERMAL
 INHALATION
INGESTION
DERMAL
INGESTION
DERMAL
                                                                                       INGESTION
                                                                                       DERMAL
                                                                                       INHALATION
                                                                                                                     CURRENT/FUTURE USE RECEPTORS
                                                                                                            nESIDitilS        WDI1KEBS     SITEUlESPASSEnS
                                                                                                              YC    A           A           OC     A
                                                                                                              •    •           •           •      •
    Notes:
    YC - Young Children
    A  - Adults
    OC - OlUdf Children
                                                                                                                                   ni'A?ll/M4n/!M(>

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                                                                                                 Sheet I of 5
                                                     Table  7
                                         TOXICITY DATA FOR NONCARCINOGENIC
                                         AND CARCINOGENIC RISK ['VALUATION
Chemical Name
VnTalllcs








.-

'










1
Aceltrtle
lleiwcne
2-Hiitaiionc
Coilum leliaclilntide
Clilorj>l>eiizene
Oiloioclltnne
Uilmoform
1,1 Dichloroeihonc
1,2 Diciiloruelhane
1,1 Dichlorociliene
tij - 1,2 - Dichlnroeiliene
Irani - 1,2 - Dichloruefhciic
l'lliyll>i-(M
2.1X)I:-02
,
I.(X)H-02
I.(KII--OI
_
9.001-03
I.UUI--02
2.(X)li-()2 .
I.OOI--OI
6.(X)li-02
5.00I--02
2.(XII:OI
I.(X)IM)2
2.00I--OI
.
•I.IXIIMH
.
.
2.(K)l;i()0
.
.
i.ooEion
.
2.00H-02
I.UORiOl
•
5.00U-OI
.
,
. . •
.
I.OOIUOO
3.00I-+00 .
-•
I,(X)IUO(>
.
4.00I--OI
I.OORfOO
l.tXIHiOl
-

-
.
.
2.8fili-()l
-
_
.
.
I.43I--OI
.
.
-
.
2.861- -01

-
2.8r,i;-oi
.
f.MR-OI.
2.8
-------
                                                   Table 7
                                        TOXICITY DATA FOR NONCARCINOOENIC
                                         AND CARCINOGENIC RISK EVALUATION
                                                                                               Sheet 2 of 5
Chemical Niune
Scinl-Volallles






















Aceiia'plillicne
Aniline
Anthracene
l)cnzo(a)aitlliraccne
Benzo'(a)pyiene
l)cnzu(l))(luoraitlliene
llenzo(glii)|>cryleiie
l)eiizo(k)niioranllienc
iti9(2-cfhylhexyl)|ihlhalale
llulyl benzyl phllialale
Cnilmrolc
•1 CMoroanitine
4 Cliloto-3 inctliylpheiiol
2-Cliluroplicii()l
1 >il>eii'/,(a,h)i>"ll» acetie
Chiysenc
l,2-l>ichloruucn/.cnc
l,4-l)iclilorol>cii7.cnc
Dielhyl |4illtalale
2,4-Dimelliyiphcnul
|)i n-lnilyl plilhnlate
l)i-n ottylplillmlnte
2,'l-l)inilr(iloliieiic
NoiicarcinoRtn Reference Dose
Rfl) RfC R(l)l
(oral) Inhalalion (inlinlnlion)
(mg/Kg-day) (nig/Cu.m) (ing/Kg-day)
6.00I--02

3.(K)li-OI
-
-
-
-
.
2.00K-02
2.
-------
                                                      Table  7
                                                                                                   Sliccl 3 ui 5
                                          TOXICITY DATA FOR NONCARCINOdliNIC
                                           AND CARCINOGENIC RISK EVALUATION
1
Chemical Nainc












re.sllcldi-n









1
I'lumene
Iliioiaiitlivnc
Iiideiio(l23-cd)|iyrene
2 Mclliylnaplillialene
2-Mcdiyl|Jicm>l
heiu>l
Naphthalene
4-Nilro|>henol
I'eiilacliloruplrenol
Hieiioiillirene
Ilieiiul
I'yrene
AMiin
alplm DIIC
IKIB IIIIC
delta lillC
gnmma IIIIC
Clilordmie
1)1)11
DDK
DDT
I)il)cii7.(ifur(in
Uiehliin
Noncarcinocen Reference Dose
KID KfC Kf|)l
(oral) Inhalation (inhalation)
(nig/Kg-day) (ing/Cu.ni) (ing/Kg-ilay)
4.00H-02
•ux)iM«
-
.
S.OOIi-OZ
5.(X)li-03
4.00B-02
-
3.(X)I!-02
-
r,.(K)l; 01
3.00I!.()2
3.(K)li-05
.
.
-
3.(X)I:-M
6.00I;-05
.
-
5.(XII;-0-I
-
5.IMII'. 
-------
           Table 7
TOXICITY DATA POR NONCARCINOGIiNIC
 AND CARCINOGENIC RISK EVALUATION
                                                       Sheet 4 of 5
Chemical Nome









Inorganic.*













l-iidniulfan
Pmlcuulfoii siilfnlc
l-jidrin
linJrin aldehyde
lindrin kelune
lle|ilaclilur
lleplachlor epoxide
Melhoxychlor
(•CIJi (Aroclor 1016)
Anlinioiiy
Arsenic
llaiiuni
Dcryllhim
Chromium III
Cliruiniuin VI
Colrall
Copper
Uail
Manganese
Mercury
Nickel (Kefineiy Dust)
Selenium
Silver
NoncarcinnRen Refcicnce Dose
IUI) IUC RIDI
(oral) Inhalation (inhalation)
(ing/Kg-day) (mg/Cu.in) (mg/Kg-day)
6.0012-03

3.0012-04
-
.
5.00I--04
1.3012-05
5.00I!-03
7.00E-05
4.0012-04
3.00IMH
7.00I2-CI2
5.0012-03
I.OUlH(ll)
5.00I--03
-
3.7IE-02*

5.(Xlli-H3
3.(X)li-W
2.(Xlli-02
S.(X)Ii-(l3
5.(X)I: 03
.
-
.
-
.

.
-
-
-
.
s.oon-w
-
-
-
-
.-
I.SOIi-03**
5.0im-05
3.0012-04
-
-

.
-
-
-
-
.
.

-
-
.
.
-
-
-
.
-• -
.
-
-
.
-
-
CnrcinoRcn Slope Paclor
.SI' Weigh! Unit Kisk SIM Weight
(Oral) of (Inhalation) (Inhalntinn) 
-------
                                                                                   Table  7
Sheet 5 ui' 5
                                                                TOXICITY DATA FOR  NONCARC1NOGENIC
                                                                 AND CARCINOGENIC RISK EVALUATION
Chemical Nninc



'Iliallilnn
Vaiiniiinii)
Zinc
Noncarcinogen Reference Dose
KID RfC RfDI
(uinl) Inhalation (inlmlnlinn)
(ing/Kg-dny) (nig/Cu.m) (ing/Kg cloy)
.
7.00K-03
3.(X)I;-OI
.
-
-,
•.
.

Carcinogen Slope Factor
SI' Weight Unit Risk - SIM Weight
(Oral) of (Inhalntimi) (Inhalation) of
(mg/Kg-Jay)- 1 Hvidence (iig/C'ii.in)- 1 (mg/Kg-«lay)-l Evidence
.
.

.
.
1)

.
•
.
.
-
.
.
-
             lil'A Weight at Evidence classifications are as follows:                       .       -

             tiiuu|> A:     Iliunan Carcinogen. Sufficient evidence from epidciniologic studies lo 3ii|ip»il a cniual association between eX|H)9lire aild cancer.
             (iroup III:    I'rohalile Iliunan Carcinogen.  Limilcd evidence  C:     I'onible Iliunan Carcinogen. Limited evidence of carcinogcnicity in animals.
              iroup I):     Not classified. Inadequate evidence of cntcinogenicily in animals.
             vlotc:  -      No data/Not available.
                          I'or Adults Only.
                          NAAQS
                          KfC/IUI) and Unit ((isk/SI' inhalation dnln cunvcrsiiiii for C(K's only in snil nml giimndwnlrr ns per IIHA.ST.
IW507.LYN

-------
                                                      Table  8
                                SITE WORKER RISK LEVELS AND HAZARD INDEX VALUES
                                        SUMMARY ACROSS EXPOSURE PATHWAYS
                                            PRESENT/FUTURE USE SCENARIOS
                                                                                                            Shed I of I
 Present/Future Use Scenarios:
                                                  Carcinogenic Risk Levels                Noncarcinogcnic Hazard Index Values
 Exposure to non-GCL Property Soil                Reasonable Maximum Exposure                Reasonable Maximum Exposure

 Silc Worker

 "l) Inhalation                                            8.90E-I2                                  l.2fiE-<)9
 2) IngcsUon                                            I.40E-05                                  2.OIE-U1
 3) Dennal Contact                                       6.88E-08                                  3.57E-04


 Total Health Risk = Soil Inhalation + Soil Ingestioii + Soil Dermal Contact

 Summation Results - Site Worker:

              Carcinogenic Health Effccls = 1.40E-05         Noncarcinogcnic Hcallh Effects = 2.4UE-03
DO.   ' N

-------
                                                        Table  8
                              OFF-SITE RESIDENT RISK LEVELS AND HAZARD INDEX VALUES
                                         SUMMARY ACROSS EXPOSURE PATHWAYS
                                             PRESENT/FUTURE USE SCENARIOS
                                                                                                               Shed  I (if 2
 Present/Future Use Scenarios:
 Exposure to Non-GCL Property Suil

 Off-Site Resident Adults

 I) Inhalation
 2) Ingcslion

 Off-Site Resident Young Children

 1) Inhalation
 2) Ingcslion
  Carcinogenic Risk Levels
Reasonable Maximum Exposure
         I.49E-I2
         3.92E-06
         2.0GE-11
         9.1GI>06
Noncai'cinngcuic lla/.aul Index Values
   Reasonable Maximum Exposure
           2.201 j-W
           5.95E-04
           I.54E-09
           5.50E-U3
 Exposure to Groundwater (including R8 wells)

 Off-Site Resident Adults

 1)  Inhalation
 2)  Ingcstion
 3)  Dcnnal Contact

 Off-Site Resident Young Children

 1)  Inhalation
 2)  Ingcslion
 3)  Dcnnal Contact
        2.98E-02
        1.05E-01
        2.48E-03
        2.78E-02
        9.80E-02
        9.-24E-05
          4.8SE-OI
           1.17EIO2
          9.95 E+00
           2.27EMH)
           5.45IMG
           l.85F-i(M)
IJ«567.LYN
          6-44

-------
                                                          Table  8

                                                                                                                   SIlCCl ?, of 2

                               OFF-SITE RESIDENT RISK LEVELS AND HAZARD INDEX VALUES
                                          SUMMARY ACROSS EXPOSURE PATHWAYS
                                              PRESENT/FUTURE USE SCENARIOS


                                                    Carcinogenic Risk Levels                  Noneaieinogcnic Hazard Index Values
 Exposure to Groundwatcr (excluding R8 wells)        Reasonable Maximum Exposure                Reasonable Maximum Exposure

 Off-Site Resident Adults

 I) Inhalation'                                             6.99E-U5                                    0.1711-0?.
 2) Ingcslion                                               2.38E-04                                    l.()f»Ei()2
 3) DcnnaJ Contact                                         2.15E-03                                    I.72EMH

 Off-Site Resident Young Children

 1) Inhalation                                               6.54E-05                                    2.88E-OI
 2) Ingcstion                                                I.33E-U4                                    4.9vclls) - Off-Site Ucsidcnt Children;

              Carcinogenic Health EITccls =  I.26E-OI          Noncarcinogenic llcallh liliccls = 5.49EKI2

 Suiiiinatioii Results (excluding R8 wells) - Off-Site Resident Adults:

              Carcinogenic Health Effects = 2.4GE-03      -    Noncarcinogenic llcallh Effects = 1.23EI-02

 Suiiiinatioii Results (cxcludinu U8 wells) - Uff-Silc Resident Children:

              Carcinogenic Health EITccls = 2.88E-04         . Nonqarcinogcnic llcallh Effects = 4.98E+02
IXJ567.LYN                                                      6-45

-------
                                                         Table 8


                                                                                                                .Slicel  I of 2

                               SITE TRESPASSER RISK LEVELS AND HAZARD INDEX VALUES
                                         SUMMARY ACROSS EXPOSURE PATHWAYS
                                             PRESENT/FUTURE USE SCENARIOS

 Present/Future Use Scenarios:
                                                   Carcinogenic Risk Levels                 Noncardnogcnic Hazard Index Values
 Exposure tu non-OCL Property Soil                  Reasonable Maximum Exposure                Reasonable Maximum Exposure

 Adull Trespassers

 1) Inhalation                                              1.20E-il                                    l.7f>E-()9
 2) Ingcslion                                              3.92E-06                                    5.95E-04
 3) Dermal Conlacl                                         3.35E-07                                    l.45P,-()3

 Older Child Trespassers

 1) InluQalion                                             ' 3.74E-12                                    2.20E-09
 2) Ingcsticm                                               3.92E-Of»                    '                2.3Xli-()3
 3) Dermal Contact                                         9.24E-OH                                    2.UOP.-03

 Exposure to Surface  Water

 Adull Trespassers

 1)  Iiigestion                                               1.52E-05                                   3.I8E-I-00
 2)  Dcnnal Contact                                        2.15E-06                                   9.32E-03

 Older Child Trespassers

 1)  Ingcslion                                              3.05E-06                                   6.3f)E-MK)
 2)  Dermal Contact                                        4.87E-07                                   3.78H-03

 Exposure tu Sediment                                    •

 Adult Trespassers

 1)  Ingestion                                               1.08E-05                                   2.7()ri-()3
2)  Dermal Conl.'ict                                         2.I5E-Ofi                                   9.32I--03
     VN

-------
                                                        Table 8
                               SITE TRESPASSER RISK LEVELS AND HAZARD INDEX VALUES
                                        SUMMARY ACROSS EXPOSURE PATHWAYS
                                            PRESENT/RJTURE USE SCENARIOS
                                                                                                              Sheet 2 of 2
 Exposure to Sediment  (Conl'd)

 Older Child Trespassers

 I) Ingcslion
 2) Dermal Contact
  Carcinogenic Risk Levels
Reasonable Maximum Exposure
         S.fiOE-Ofi
         5.94E-U7
Noncarcinogcnic Hazard Index Values
   Reasonable Maximum Exposure
           I.OKE-07.
 Total Health Risk = Soil Inhalation + Soil Ingeslion + Soil Dermal Contact i Surface Water Iii|>eslion  i Surface Wafer Dvnnal Contact
 + Sediment Ingeslion + Sediment Dermal Contact
 Summation Results • Adult Trespassers:

              Carcinogenic Health Effects = 3.41E-05

 Summation Results - Older Child Trespassers:

              Carcinogenic Health Effects = 1.66E-05
        Noncarcinogcnic Health Effects = 3.I9Ei()0



        Noncarcinogcnic Health Effects = 6.38E+00
I»567.LYN
          6-47

-------
Table 9. List of Applicable or Relevant and Appropriate Requirements (ARAfis) and To-Be-Considered (TBC) for the Selected Remedy
REGULATION
STATUS
REGULATORY
LEVEL
DESCRIPTION
RATIONALE
ACTION-SPECIFIC
RCRA- Land Disposal Restrictions
(40 CFR 268)
RCRA- Standards Applicable to Transport
of Hazardous Waste (CFR 263.11, 263.20-21 And
263.30-31)
RCRA- Standards for Owners/Operators of Permitted
Hazardous Waste Facilities (40 CFR 264.10-264.18)
DOT- Rules for Transportation of Hazardous Materials
(49 CFR Parts 107, 171.1-172.558)
New York State Hazardous Waste Manifest System
Rules (6NYCRR 372)
New York Hazardous Waste Treatment Storage and
Disposal Facility Permitting Requirements
(6 NYCRR 370 and 373)
OSHA- Safety and Health Standards (29 CFR 1926)
OSHA- Record keeping, Reporting and related
Regulations (29 CFR 1904)
ARAR
ARAR
ARAR
ARAR
ARAR
ARAR
TBC
TBC
Federal
Federal
Federal
Federal
NY State
NY State
Federal
Federal
Regulates Land Disposal of
Hazardous Wastes
Regulates Transport of
Hazardous Waste
Regulates Hazardous Waste
Treatment, Storage or Disposal
Facilities
Regulates Transport of
Hazardous Waste
Regulates the Manifesting of
Hazardous Wastes
Regulates Hazardous Waste
Treatment, Storage or Disposal
Facilities
Regulates Occupational
Exposure/Protection
Regulates Record Keeping and
Reporting Requirements
Off-site Disposal of Treatment
Residues
Off-site Disposal of Treatment
Residues
Off-site Disposal of Treatment
Residues
Off-site Disposal of Treatment
Residues
Off-site Disposal of Treatment
Residues
Off-site Disposal of Treatment
Residues
Workers Health and Safety
Workers Health and Safety
CHEMICAL-SPECIFIC
National Ambient Air Quality
Standards (NAAQS) (40 CFR 50)
Safe Drinking Water Act
(40 CFR 141)
New York State Air Criteria Requirements
6 NYCRR 200-212)
New York State Pollution Discharge Eliminantion
System (SPDES) (6 NYCRR 750)
New York State Surface and Groundwater Quality
Standards (6NYCRR Part 703)
TBC
ARAR
TBC
TBC
ARAR
Federal
Federal
NY State
NY State
NY State
Regulates Air Emissions
Regulates Standards for
Drinking Water Protection
Regulates Air Emission
Requirements
Regulates Discharges to Surface
Waters
Regulates Surface and
Groundwater Quality
Operation of Thermal Desorption
System
Groundwater Treatment
Operation of Thermal Desorption
System
Groundwater Treatment
Groundwater Treatment

-------
REGULATION
STATUS
REGULATORY
LEVEL
DESCRIPTION
LOCATION-SPECIFIC
New York State Wetland Protection Regulations
(6 NYCRR 661)
New York State Floodplain Management Regulations
(6 NYCRR 500)
National Historic Preservation Act
Executive Orders on Floodplain Management and
Wetland Protection #11988 and 11990
ARAR
ARAR
TBC
TBC
NY State
NY State
Federal
Federal
Regulates Disturbance of
Freshwater Wetlands
Regulates Disturbances to
Floodplain Areas
Regulates Protection of Historic
and Cultural Resources
Requires Assessment of Impacts
to Floodplains and Wetlands
RATIONALE

Surface-water Sediment Remediation
Surface-water Sediment Remediation
Surface-water Sediment Remediation
Surface-water Sediment Remediation

-------
                                                               Table 10                                                     .Shed I of .1
                                                          Alternative GW-2A
        TREATMENTOITION I: EXTRACTION/PHASE SEPARATION/PRETKEATMENT/CARIJON ADSORPTION/ DISCHARGE TO SURFACE WATER
 FACIIJTY/CON.STRUC'TION
  I.     SOCURITV SYSTEM
        I.     Waining Signs
        2.     Fence Completion
        3.     E<|iiipmenl Piirking mul Storage Area
 If.    SUPPORT FACILITIES
       i.     Office Trailer
       2.     Dccuiiliiininalion Trailer

 III.    GROUNDWATER EXTRACTION
       I.     Trenches
       2.     Pumps
       3.     Piping
       4.     Extraction Well
       5.     Pumps
       (•>.      Piping
       7.      Hot Spol Extraction Wells
       8.      Pumps
       9.      Piping

 IV.    COLLECTION
       I.      Collection Tank
       2.      Pumps
       3.      Piping

 V.    PHASE SEPARATION

 VI.    OFF-SITE DNAPL RECYCLE/DISPOSAL
       I.     Tank
       2.     Contractor
                                                CAPITAL COST ESTIMATES (IVA*) DOLLARS)
MATERIAL
ESTIMATED
QUANTITIES
31
1 ,200 II
2.500 sy
1
1
1
2
i.ooon.
i
2
5(X) ft
4
8
1,00011.
1
2
5(X) II.
1
1
125 Ions
(30,0(X) gal)
UNIT
PRICE
80
18
8
I4.3IX)
42,900
59.400
2,000
r»
7,000
1,500
6
• 2,000
1 ,000
6
5,000
2.000
6
I5.IKX)
5,000
I.KOO


COST
2,500
21, MX)
20.IMX)
I4.3IX)
42,90

                                                                                                             DIRECT CONSTRUCTION
DIN2.I.YN

-------
                                                                 Table  10
                                                                                                                                  Shod '2 til 3
                                                             Alternative  GW-2A
        TREATMENT OPTION I:  I-XTK ACTION/PI I ASE SliPARATION/PRF.TREATMENT/CARHON AIXSORPTION/DISCIIAUCiE TO SURFACE WATER
 FACILITY/CONS'! RUCTION

 VII.   CHEMICAL PRECIPITATION SYSTEM
       1.      Rapid Mix Tank
       2.      Flocculator
       3.      Claiificr
       4.      Causlic feed tank
      • 5.      Caustic feed pumps
       6.      Polymer feed lank
       7.      Polymer feed pumps
      • 8.      Acid feed tank
       9.      Acid feed pumps
       10.      Process piping

 VIII.   FILTRATION SYSTKM
       I.      Filter feed water sump
       2.      Filler feed pumps
       3.      Process piping
       4.      Dual media pressure filters

 IX.   SLUDGE HANDLING SYSTEM
  X.
       1.
       2.
       3.
       Sludge pumps
       Filler press
       Filiniie pumps
                                                  CAPITAL COST ESTIMATES (1995 DOLLARS)
                                         ESTIMATED
                                         QUANTITIES
                                         I
                                         I
                                         I
                                         I
                                         2
                                         I
                                         2
                                         I
                                         2
                                         15011
                                         I
                                         2
                                         15011
                                         2
2
I
2
ACTIVATED CARBON ADSORPTION SYSTEM
I.      Activated carbon adsorber       •      2
2.      Treated water lank                   I
3.      Treated water pumps                 2
4.      Process Piping                   •   5(X)
  All niimlieis arc rounded (o nearest hundred.
                     MATERIAL
                  UNIT
                  PRICE       COST
                  5,000        5,0(f()
                  Included in Clarificr Unit
                           INSTALLATION
                         UNIT
                         PRICE      COST
                         3,000
                       3,000
  750
50.0IX)
 1,500
 1,500
50.0IX)
 3,001)
 1.001)
25,000
 1,250
 2,000
25.000
 2,500
                          DIRECT CONSTRUCTION

                          COST*


                          R.OOO
35.0IX)
1,000
500
9,000
500
9,000
500
15
35,000
1,000
1,000
9,000
1,000
9,000
1,000
2,300
5,000
300
1,000
2,500
1.000
2,500
1,000
50
5,000
300
2,000
2.500
2.000
2,500
2,000
7,500
40.000
1,300
3,000
11,500
3.000
11,500
3,000
9. 800
9,000
1,800
15
50,000
9,000
3,000
2,300
IOO,(XJ()
2.500
2,000
50
4,000
2.500
4,000
7,500
8,000
11.500
7,fioo
9,800
108.000
 3.500
75.000
 5,500
li).o(X)
5,000
2,000
6
20,000
5,001)'
4,000
3,000
5,000
3,000
2,000
15
IO.O(X)
3.000
4.000
7.500
30.000
8,000
R.OOO
I(),5(XI
DIMM.YN

-------
                                                            Table 10                                                 Sheet 11 ol
                                                       Alternative GW-2A
        TREATMENT OPTION I: HXTU ACTION/I'M ASH SIMRATION/PRIZTRIiATMENT/CARBON ADSORITION/DISCIIAROli TO SURFACE WATER

                                             CAPITAL COST ESTIMATES (1995 DOLLARS)
 FACILITY/CONSTRUCTION

  xi.   TREATED"WATER DISCHARGE
       I.     Pi|)clhic
       2.     Outfall structure

 XII.   OFFICE AND CONTROL UUILDINC!

 XIII.   BLGCTKICALS

 XIV.   INSTRUMENTATION AND CONTROLS

 XV.   PROCESS WATIiR SUPPLY

 XVI.   FOUNDATIONS AND PADS

 XVII.   HEALTH AND SAFETY

 XVIII.  TREATABILITY STUDY

 XIX.   MOBILIZATION/DEMOBILIZATION

ESTIMATED
QUANTITIES
1 ,000 II
LS
LS
LS
LS
LS
LS
LS
LS
LS


MATERIAL
UNIT
PRICE COST
6 - 6,000
5,000 5.000
40.0IX) 40,000
Included in installation
Included in installation
1,200 1,200
5,000 5,000
Included in installation
Included in installation
Included in installation
Total Direct Construction
Contingency @ 20% of '1
1NSTAL
UNIT
PRICE
15

50,()(X)
KX).(X)I)
fiO.IHX)
1,1(00
7,500
50.0IX)
r>o,o(X)
50,(HX)
Cosl (TDCC)
•DCC
LATION

COST
I5.IMX)
Included
50.0IX)
lOO.IXK)
60,0(X)
t,HOO
7,500
50.000
60,(I(X)
50,01 X)


Engineering® 10% ofTDCC

Legal and Administrative
@ 5% ol TDCC

Toial ('oiisliiKlinii Cosl
DIRECI

COST*
21,01X1
5,000
90.1 WH)
I(X).(X)0
fiO.O(X)
:t.ooo
I2.51X)
50.01X)
r,o,o,x»
SO.OIX)
1.394.900
279,(X)0
139,500
r)9.7(X)
I.HK:I,IOO
* All iMiinlicis arc rounded to nenrcsl hundred.
1)1142 I.VN

-------
                                                         Table  10                                                Sheet I ol 4
                                                    Alternative GW-2B
      TREATMENT OITION 3: EXTRACTION/PHASE SEI'ARATION/PRETREATMENT/lHOLOCilCAL TREATMENT/DISCHARGE TO SURFACE WATER

                                           CAPITAL COST ESTIMATES (1995 DOLLARS)
MATERIAL
FACILITY/CONSTRUCTION
1.



11.


III.









IV.



SECURITY SYSTEM
1.
2.
3.
Winning Signs
Fence Completion
Equipment Parking and Storage Area
ESTIMATED
QUANTITIES

31
1.200 If
2,500 sy
UNIT
PRICE

80
18
8
COST

2,500
21,600
20,000
INSTALLATION
UNIT
PRICE

20
8
4
COST

600
9,600
10,01X1
DIRF.C
COST*

3.100
31,200
30,01X1
SUPPORT FACILITIES
1.
2.
Office Trailer
Decontamination Trailer
1
1
14,300
42,900
14,300
42,9
5.000
4,000
3,000
3,000
2,000
15
3,000
4,200
7,500
8,000
8.000
I0.5(X»
                                                                                                    DIRECT CONSTRUCriON
  V.  PHASE SEPARATION
I5.0IX)
15,01 X)
Included
I5.0IX)
DIH2.I.YN

-------
                                                                  Table  JO
                                                             A:i.tcni,-iE:l.vc CW-2U
       TRHATMENT-OITION 1: EXTRACTION/PHASE .SEIVWATION/PIUiTKGATMt»NT/mOLO(.ilCAL TREATMENT/DISCHARGE TO SURFACE WATER

                                                  CAPITAL COST ESTIMATES (1995 DOLLARS)
                                                                                                                                  Shi-el 2 i)l 'I
 FACILITY/CONSTRUCI'ION

   VI.  OFF-SITE DNAI'L RECYCLE/DISPOSAL
        I.      Tank
        2.      Contractor
   VII.  CHEMICAL PRECIPITATION SYSTEM
        I.      Rapid Mix Tank
      .  2.      Flocciilalor
        3.      Cl;iril1cr
       •4.      Caustic Iced lank
      ,  5.      Caustic Teed pinnp.s

        6.      Polyiner Teed tank
        7.      Polyincr Iced pumps
        8.      Acid Iced lank
       9.     Acid Iced pinups
        10.     Process piping

 VIII.   FILTRATION SYSTEM
        1.     Filler feed walcr sump
       2.     Filler feed pumps
       3.     Process piping
       4.     Dual media pressure fillers

  IX.   SLUDGE HANDLING SYSTEM
                                  ESTIMATED
                                  QUANTITIES.
                                        I
                                  125 Ions
                                  (30,000 g
       1.
       2,
       3.
Sludge pumps
Filler press
Pillralo pumps
   MATERIAL
 UNIT
 PRICE       COST
 5 ,<)<)()
 1,800
  5,000
225.1XH)
                INSTALLATION
             UNIT
             PRICE     COST
  .«.()()(>      3.0(10
     Included
750
50,000
1,500
 1,500
50,000
 3.001)
 1.01)1)
25.0IX)
 1.250
 2,000
25.000
 2,500
                          DIRECT CONSTRUCTION

                          COST*
                K.OOO
              225.000
1
1
1
1
2
1
2
1
2
150)1
, 5,000
Included in
35,000
1.000 .
500
4,000
500
9,000
500
15
5,000
Clarillcr Unit
35,0(X)
1,000
1,000
4,000
1 ,000
9,000
1,000
2,300
3,000

5,000
3(X)
1,000
2.500
1,000
2,500
1.000
50
3.000

5,000
3(X)
2.000
6.500
2,000
2.500
2,000
7,500
8,000

40.0IX)
1.300
3,000
11.500
3,000
II.5IM)
3,000
9.KOO
1
2
150 11
2
9,000
1 ,800
15
50,000
9,000
3,fiOO
2,300
100,000
2,500
2,000 .
50
4,000
2,500
4,000
7,500
8,000
II.5(X)
7/100
9,800
I08.(X)0
 3,500
75.0IX)
 5.500
1)1142.I.YN

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                                                          Table  10                                                  Shed 3 of
                                                       Alternative GW-2R
      TREATMENT OITION 3: EXTRACTION/PHASE SI-PARATION/PRETREATMENT/IJIOLOCilCAL TREATMENT/DISCHARGE TO SURFACE WATER

                                              CAPITAL COST ESTIMATES (199-5 DOLLARS)
                                            ESTIMATED
 FACILITY/CONSTRUCTION                      QUANTITIES

  X.    BIOLOGICAL TREATMENT
       I.     Bioliealnieiil Unil                  I
       2.     Treated Water Tank                 I
       3.     Treated Water Pumps               2
       4.     Process Piping                     5(K) It.

  XL   TRIiATIil) WATER DISCHARGE
       I.     Pipeline                          1,000
       2.     Outrall Structure                   LS

 XII.    OFFICE AND CONTROL BUILDING .        LS

 XIII.    ELliCTRICALS                          LS

 XIV.   INSTRUMENTATION AND CONTROLS      LS

 XV.   PROCESS WATER SUPPLY               LS

 XVI.   FOUNDATIONS AND PADS               LS

 XVII.   TRHATAHIUTY STUDY                  LS
MATERIAL
UNIT
PRICE COST
Included
5.000
2,000
6
6
5,000
40,000
Included
Included
1,200
5,000
Included
in installation
5.000
4,000
3,000
6,000
5.000
40.000
in installation
in installation
1.2(10
5.000
in installation
INSTALLATION
UNIT
PRICE
MO.tXIO
3,000
2,000
15
15
50.000
IOO,(X)0
80.0W
1,801)
7,500
60,01X1
COST
I4(),(X)0
3,000
4.000
7,500
I5.0IX)
Included
50,0(X)
100,000
80.000
I.XOO
7,500
r>o,()(X)
DIRECI
COST*
MO.(X)0
8.000
8.000
10.500
21.000
5.000
90.0W
I(X),(X)0
80.0(X)
3,000
I2,5(XI
r>o.oix)
DIMZ1.YN

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                                                               Table 10                                 .
                                                           Alternative GW-2B
       TREATMENT OITION .1: EXTRACTION/PHASE SI-PARATION/PRETREATMIiNT/mOLO(!ICAL TIlfiATMIiNT/DISCIIARCJIi TO SIJRI'ACIi WATI-R
                                                                                                                                 4 ol 'I
 FACILITY/CONSTRUCTION

 XVIII.  HEALTH AND SAFETY

  XIX.  MOBILIZATION/DEMOBILIZATION
                                                 CAPITAL COST ESTIMATES (I"-"S DOLLARS)
                                                                  MATERIAL
INSTALLATION
   DIRliCT CONSTRUCTION
JiSTI MATED
QUANTITIES
I.S
LS
UNIT
PRICE
. Included in
Included in
COST
installation
installation
UNIT
PRICE
50,()(X)
COST
50.0IX)
50,0(X)
COST'
5«MMX)
50,0(X)
                                                               Tolal Direct Conslriiclkin Cost (TDCC)
                                                               Contingency @ 20% of TDCC
                                                               Engineering @ 10% of TDCC
                                                               Legal and Ailininislralivc @ 5% of TDCC

                                                                           Tolal Construction Cost
1,524,900
  3<)5,(XX)
  152,500
  7r).2(X)

2,05K,fiOO
 *  All numbers are rounded lo nearest hundred.
DII42.I.YN

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                                                          Table. 10
                  ALTERNATIVE SD-2: EXCAVATION/DEW ATERING/TREATMENT AND DISPOSAL WITH GCL PROPERTY SOILS

                                             CAPITAL COST ESTIMATES (1995 DOLLARS)
 FACILITY/CONSTRUCTION

  1.    SITE PREPARATION

  II.    SUPPORT FACILITIES

 III.    CLEARING AND GRUBBING

  IV.   CONTAMINATED SEDIMENT EXCAVATION 125 cy

  V.   DEWATERING

  VI.   ON-SITE THERMAL DESOR1TION

 VII.   DISPOSAL

VIII.   STREAM/WETLAND RESTORATION

 IX.   HEALTH AND SAFETY

  X.   MOBILIZATION/DEMOBILIZATION
ESTIMATED
QUANTITIES
Shared with GCL
Shared wilh GCL
I.fi8«sf
1 125 cy
125 cy
125 cy
125 cy
125 cy
LS
LS
MATERIAL INSTALLATION
UNIT UNIT
PRICE COST PRICE COST
properly soils action.
properly soils action.
Included in installation 0.15 3(X)
Included in installation 25 3,100
400 50,000 Included
2(X) 25,000 Included
I0: 1,300 Included
40 5.000 10 1.300
KXI.OOO UX).(XK) included
35.01X) 35.01X) .Included
Total Direct Construction Cost (TDCC)
Contingency @ 20% TDCC
Engineering @ 10% TDCC
Legal and Administrative @ 5% TDCC
DIREC
COSI

3(X)
3.100
50.000
25.0(X)
1,300
6,300
100.000
35.000
221. (KM)
44.2IX)
22.IIXI
II, MX)
                                                                    Total Construction Co.sl
                                                                                                      DIRECT CONSTRUCTION
2W/100
  All numbers rounded to the nearest hundred.
DIU2.I.YN

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         APPENDIX III




ADMINISTRATIVE RECORD INDEX

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                     6CL TIE & TREATING SITE
                        OPERABLE UNIT TWO
                   ADMINISTRATIVE RECORD FILE
                        INDEX  OF DOCUMENTS

3.0  REMEDIAL INVESTIGATION

3.4  Remedial Investigation Reports

P.   300001-   Report:  Final Remedial Investigation Report. GCL
     300936    Tie & Treating Site. Sidney. New York. Volume I of
               II. prepared by Mr. Howard Lazarus, P.E., Site
               Manager, Ebasco Services Incorporated, January
               1995.

P.   300937-   Report:  Final Remedial Investigation Report. GCL
     300959    Tie & Treating Site. Sidney. New York. Volume II
               of II, prepared by Mr. Howard Lazarus, P.E.,  Site
               Manager, Ebasco Services Incorporated, January
               1995.

4.0  FEASIBILITY STUDY

4.3  Feasibility Study Reports

P.   400001-   Report:  Final Feasibility Study Report. GCL Tie
     400511    & Treating Site. Sidney. New York, prepared by   .
               Mr. Howard Lazarus, P.E., Site Manager, Ebasco
               Services Incorporated, January 1995.

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        APPENDIX IV




STATE LETTER OF CONCURRENCE

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-DIRECTOR'S OFFICE  '  . Fax:518-485-8*04



  New York State Department f Environ me
  50 Woff Road, Albany, New York 12233-7010
                                              Mar 29 "'95  1&=50     P. 01/02
                                          Post-It1" brand fax transmilla! memo 7671 f of page* >

                                                               CO.
                                          Dtpt.
Ms. Kathleen C.  Callahan

Director                         _.  . .
Emergency & Remedial Response Div.s.on
United States Environmental Protection Agency

Region II
290 Broadway,  1 9th Floor
New York,  NY  10007-1866
                                                                     ^
                                                                     5/5
                                                        MAR  30 i3S5
                                                                    Commissioner
   Dear Ms. Callahan:
                                 GCL Tie & Treating Site ID # 413011
                                 Draft Record of Decision, Operable Unit 2
    following:
        SD-2 Sediment
                          excavation, treatment, and disposal with GCL property soils.
           2.
            3.
            4.
              the site;

               Post-treatment sampling and analysis to ensure attainment of

               established cleanup levels;






               pre-excavation conditions;









                        and vegetation plans; and site security and access.

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DIRECTOR'S OFFICE     Fax:518-485-8404 '         Mar 29  '95   16:50    P.'02/02


Ms. Kathleen C.  Callahan                                         Page 2


      GW-2, Groundwater extraction and treatment.

      1.     Ground walKi and DNAPL extraction through 3 combination of
            collection trenches and extraction wells;

      2.     On-5ite treatment to ARAR levels;

      3.     Remedial design to include: plume and DNAPL area delineation;
            investigation of current aquifer conditions and hvdrologic parameters;
            evaluation of additional groundwater treatment alternatives; plans,
            operating specifications, and performance parameters for on-site
            groundwater treatment; engineering controls and mitigation options for
            discharges.and other residual wastes generated during the remedial
            action; off-site disposal options for unbeatable residues; sampling and
            analytical protocols; and maintenance, site security and access.

      The NYSDEC and NYSDOH concur with the selected remedies for Operable
Unit 2.  Our concurrence is conditioned on the completion of a Remedial Design
which further evaluates the feasibility and practicability of groundwater treatment.
It-is understood that the results of the  additional investigations of the plume and
D'NAPL areas will be used to develop a detailed evaluation of the actual scope of
the groundwater remedial program. Alternatives to the full scale program outlined
in the ROD might include enhanced bioremediation or DNAPL removal only,
alternatives which would represent significant capital and O&M cost savings and
yet be equally protective.  The operation and maintenance (subject to the
90%/10% federal/State split) of  any system will be the responsibility of USEPA for
a period  of ten (10) years.

      It  is also understood that EPA may seek technology-based chemical-specific
waivers  of ARARs for the  DNAPL areas of the site if it is determined from the
Remedial Design or through operation  of a groundwater treatment system that
contaminant reductions to standards are not feasible or cannot be achieved within
a reasonable time frame. The NYSDEC reserves concurrence on this issue.

       If you have any  questions, please contact Walter E. Demick,  P.E. at (518)
457-5637.

                                    Sincerely,
                                    Michael J. OToole, Jr.
                                    Director
                                    Div. of Hazardous Waste Remediation

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      APPENDIX V •




RESPONSIVENESS SUMMARY

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                           APPENDIX V

                      RESPONSIVENESS SUMMARY

                GCL TIE & TREATING SUPERFUND SITE
INTRODUCTION

A' responsiveness summary is required by the Superfund
legislation.  It provides a summary of citizens' comments and
concerns received during the public comment period, and the
United States Environmental Protection Agency  (EPA) and the New
York State Department of Environmental Conservation's  (NYSDEC's)
responses to those comments and concerns.  All comments
summarized in this.document have been considered in EPA and
NYSDEC's final decision for selection of a remedial alternative
for the GCL Tie & Treating site.

SUMMARY OF COMMUNITY RELATIONS ACTIVITIES

Community involvement at the site has been moderate.   EPA has
served as the lead Agency for community relations and  remedial
activities at the site.  EPA initiated its community relations
activities on August 19, 1993 with the conduct of community
interviews with local officials and residents.  Public meetings
were held on August 19, 1993 and August 5, 1994 to discuss
planned site activities and seek comments on the preferred remedy
for contaminated soils  (Operable Unit 1), respectively.

The remedial investigation and feasibility study  (RI/FS) reports.
and the Proposed Plan for Operable Unit  2 of the site  were
released to the public  for comment on March 1,  1995.   These
documents were made available to the public in the administrative
record file .at the EPA  Docket Room in Region II, New York City,
and in the  information  repository at the Sidney Memorial Library,
Main Street, Sidney, New York.  The notice of  availability for
the above-referenced documents was published in the Oneonta  Daily
Star on March  1, 1995.  The public comment period  on these
documents was held from March 1, 1995 to March 30, 1995.

On March' 8, 1995,  EPA conducted a public meeting at the Civic
Center "in Sidney,  New York to discuss remedial alternatives  for
the second  operable unit of site remediation,  namely,
contaminated groundwater and surface-water sediments,  to present
EPA's preferred remedial alternative, and to provide an
opportunity for the interested parties to present  oral comments
and guestions to EPA.

Attached to the Responsiveness Summary are the following
Appendices:

     Appendix A -  Proposed Plan

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     Appendix B - Public Notice

     Appendix C - March 8, 1995 Public Meeting Attendance Sheets

     Appendix D - March 8, 1995 Public Meeting Transcript

     Appendix E - Letters Submitted During the Public Comment
                  Period

 SUMMARY OF COMMENTS AND RESPONSES

 Comments expressed at the public meeting and written comments
 received from the Village of  Sidney and New York State Electric
 and  Gas Corporation during the public comment period have been
 categorized as follows:

     A.  Selected Remedy

     B.  Nature and Extent of Contamination

     C.  Health Effects

     D.  Land Use

     .E.  Impact of Cleanup Activities on the Local  Economy  and
          Job Market

 A summary of the comments and EPA's responses to the comments is
.provided below.

 A. Selected Remedy

 Comment #1: EPA received correspondence  from the Village of
 Sidney requesting that EPA consider selecting Alternative GW-3
 for  the groundwater  remedy.   The Village  indicated  that  the
 relatively low estimated pretreated groundwater effluent flow of
 approximately  30 gallons per minute generated under Alternative
 .GW-3 would not be expected to interfere with the treatment
 process at the publicly owned treatment works  (POTW).  Although
 the  Village could not presently commit  to  accepting the  waste
 stream, they expressed their desire and willingness to pursue
 this issue by  obtaining additional information  on the  impact of
 the  potential  discharge on the  POTW1s  effluent  and  sludge
 quality, and consulting with NYSDEC and Delaware County  on  these
 issues.

 Response fl:  Given  the information currently  available, and
 lacking a firmxcommitment  from  the Village of  Sidney,  EPA
 believes "that  Alternative  GW-2  is  the  best, choice  for  remediating
 groundwater at the  site.   EPA's main  concern  regarding
 Alternative GW-3  is  the uncertainty associated  with whether the
 Village would  be able to obtain the necessary  clearances (from

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local and State agencies) to accept the groundwater effluent.
Less uncertainty is associated with the implementation of
Alternative GW-2 since a similar groundwater pump and treat
system is being utilized for remediation of the Route 8 Landfill,
located just southeast of the site.  The treated effluent from
the Route 8 Landfill is discharged into the same drainage ditch
contemplated as a discharge point under Alternative GW-2.  The
Route 8 discharge has been able to meet all New York State
.Pollutant Discharge Elimination System  (NYSPDES) requirements.
The effluent generated under Alternative GW-2 would meet
standards similar to those required for the Route 8 Landfill
system.

Pending the results of the work to be conducted during the
remedial design phase, and pending further input from the Village
as to whether they will enter into a long-term commitment to
accept the; waste stream, EPA may re-evaluate  the feasibility  and
cost-effectiveness of utilizing the POTW.  If after evaluating
the additional  information EPA determines  that the Village  is
willing and able .to accept pretreated groundwater at the POTW and
that this  is the most cost-effective alternative, EPA may
consider modification of the groundwater remedy.

Comment #2:  Village representatives were  interested .in obtaining
information regarding the anticipated chemical  characteristics  of
the groundwater following separation and manganese pretreatment
which  could potentially  be discharged to the  POTW.

Response  #2:  A detailed characterization  of  the groundwater at
various stages  of treatment would  be available  during  the
remedial  design phase.

Comment #3;  Proposed Remedy, page 12.   The  "goal"  of  Alternative
GW-3,  referred  in the last paragraph of the  alternative
description, is not  stated.

Response  #3:  The "goal" of the  active  groundwater  restoration
alternatives was detailed  in the Alternative GW-2 description
summary.   The groundwater  remediation  goal is the  same for both
Alternatives GW-2 and GW-3, namely,  to  restore the  groundwater to
drinking,  water  quality.

Comment #4i:  Village officials  submitted additional  cost data,
 including information on likely  discharge  fees associated with
discharge of pretreated  effluent to  the POTW.

Response  f4:  EPA considered the revised estimate  and
acknowledges that this estimate  would  result in an  overall lower
cost  for'Alternative GW-3.  However,  as'noted above,  significant
uncertainty  exists  regarding the implementability  of Alternative
GW-3.  This  uncertainty, rather  than cost, was the  significant

-------
factor in selecting Alternative GW-2 rather than Alternative
GW-3.

Comment #5:  The Village also noted that although the closest
connection point to the public sewer system is on the south side
of Delaware Avenue, the most expedient connection point would be
to the public sewer on Unalam property which runs in a north-
south direction in the vicinity Of the Unalam water well.

Response 15:  This information will be considered during the
remedial design phase for any action which may require connection
to the sanitary sewer.

B. Nature and Extent of Contamination

Comment 11:  A commenter suggested that groundwater contaminant
boundaries in the shallow intermediate and deep zones had not
been established and was confirmed as indicated by contamination
found in perimeter wells.  It was also noted that since there are
residential groundwater users located northwesterly of the site,
the potential impact to these users due to offsite migration,
whether site or nonsite related, should be considered.

Response #1:  Contamination due to GCL site activities has been
established.  The .information obtained as part of EPA's RI
indicates that GCL-related groundwater contamination is limited
vertically to the shallow and intermediate deep zones, and
horizontally to a 'narrow portion of the aquifer beneath the GCL
•facility.  There is no evidence that suggests that the GCL
contaminant plume has moved beyond the GCL property boundaries.
Groundwater contamination, especially in the wells along the
northern perimeter, is attributed to the Route 8 Landfill.
Although additional information will be collected during the
remedial design phase  (including installation of new monitoring
wells, and sampling of existing and newly installed wells) to
refine further the extent of the GCL contaminant plume, it is
unlikely that private residential wells will be sampled unless
the data generated during the remedial design suggest that such
action is warranted.  The selected remedy will be designed to
contain the GCL groundwater contamination within the property
boundaries so that offsite wells  (including those located
northwesterly of the site) are not affected.  Individuals
concerned with the quality of their residential well water could
have their private wells tested by the New York State Department
of Health  (NYSDOH).

Non-GCL contamination associated with the Route 8 Landfill plume
is already being remediated under the NYSDEC's hazardous waste
remediation program; a groundwater collection and treatment
system designed to address the groundwater contamination was
constructed and recently started operation.  It is expected  that
operation of the Route 3 Landfill remediation system will

-------
significantly  reduce  or eliminate groundwater contamination from "
upgradient  sources.   EPA will work with New York State and the
responsible party  for the Route  8 Landfill site to evaluate the
effectiveness  of the  groundwater restoration system.

Comment #2: EPA should consider including monitoring of existing
downgradient wells in all alternatives  including "no build" for
reasons mentioned, above.

Response #2:  All  of  the groundwater remedial alternatives
evaluated in the Proposed Plan,  including the selected remedy,
include further delineation of  the  GCL  contaminant plume.
Although the exact location and number  of wells to be installed
and sampled will be determined'during the remedial design phase,
sampling of existing residential wells  will  be  conducted provided
it is deemed to be necessary for developing  the remedial design
 (see also comment  #1 above).

Comment #3:  It appears that there  is significant  groundwater
contamination  which is not  related  to the GCL site.   Since  the
 full extent of the non-GCL contamination was not addressed  in the
RI, is EPA planning to define other contaminant plumes,  even if
they are not related to the GCL site?

• Response f 3:  Two contaminant plumes were identified in the area.
 of study:  the GCL site plume and the Route 8 Landfill plume.   The
.Route 8 Landfill  plume is considerably deeper and larger in
 extent than the GCL plume,  and consists of some contaminants
 (e.g., PCBs) not found in the GCL contaminant plume.   The Route .8
 Landfill contamination is not related to the activities conducted
 at the GCL site;  remediation at the Route 8 Landfill.site is
 being undertaken by a private party under the supervision of
 NYSDEC.  One of the activities being conducted at the Route 8
 Landfill is the installation and sampling of numerous monitoring
 wells to define .the nature and extent of groundwater
 contamination.  Individuals interested in learning more about
 remedial activities at the Route 8 Landfill should contact NYSDEC
 Region 4 in Schenectady, NY., at (518)  357-2045.

 EPA's RI focussed on contamination which resulted from wood-
 preserving activities at the GCL site.   The contaminant plume
 originating at GCL appears to be limited to the
 shallow/intermediate portion of the aquifer and contained within
 the property boundaries.  However,  additional sampling of
 existing cind new monitoring wells will be conducted during the
 remedial design phase to further detail the extent of groundwater
 contamination and to .ensure that the contamination will not
 impact areas outside the GCL property.

-------
C.  Health and Environmental Effects

Comment #1:  Residents expressed concern about health threats
resulting from exposure to contaminated groundwater.

Response #1:  The results of the RI indicate that site-related
groundwater contamination is contained within the GCL property
boundaries.  No private or public drinking water supply wells
exist within the boundaries or immediately adjacent to the GCL
contaminant plume.  Therefore, there is no known current human
exposure to contaminated groundwater from the GCL site; the
groundwater remedy will prevent future exposure to contaminated
groundwater.  However, due to the existence of other potential
sources of groundwater contamination in the area such as the
Route 8 Landfill, households which have private wells should
consider having their water tested for drinking water parameters.
NYSDOH has recently sampled private wells in the Delaware County
area and should be contacted for additional information on
regional groundwater quality.

Comment #2:  A resident expressed concern about health and
environmental threats resulting from the discharge of treated
groundwater to the surface water.

Response #2:  The groundwater remedy provides.for discharge of
treated groundwater to the drainage ditch that runs along the
southern border of the site.  The treated groundwater would
comply with the NYSPDES requirements, which are designed to
protect both human health and the environment.  Therefore, no
significant impact to human health or the environment is expected
due to the discharge of treated GCL site groundwater to the
drainage ditch.

D.  Land Use

Comment #1:  Village officials and residents have expressed
concern about future land use of the site property.  They noted
that the site is zoned for industrial use, with no change in
zoning expected.

Response #1:  The remedy that EPA has selected for the site
soils, sediments and groundwater will allow for an
industrial/commercial use of the property in the future.  In
addition, EPA will recommend to local agencies that institutional
control measures be undertaken to ensure that future land use of
the property continues to be industrial/commercial, and precludes
the use of Site groundwater for human consumption until drinking
water quality is restored in the aquifer.
                                6

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E.  Impact of Cleanup Activities on the Local Economy and Job
    Market

Comment #1:  After the selected remedies for soil, surface-water
sediments and groundwater are implemented,  can the land be
utilized?

Response #1:  Based upon input from community and local
officials, the selected soils, sediments and groundwater remedies
will be designed to allow for an industrial/commercial use of the
property in the future.  EPA shares the Village's interest of
returning the property to productive use as soon as possible.  To
achieve this, the most important step is completing the soil
remediation.  As no viable potentially responsible parties (PRPs)
have been identified to implement the site remedies, EPA would
utilize the Superfund to pay for the remedies.  It is expected
that EPA will complete the design and procurement of a contractor
to remediate the soils and surface-water sediments in
approximately 1.5 years.  In addition, the remedial action for
soils and surface-water sediments should be completed
approximately 1 year thereafter.  During this time, EPA will be
conducting the additional investigatory work needed to implement
the groundwater remedy.  Although a small portion of the property
may be required for the long-term operation of the groundwater
restoration system, the majority of the property could be
returned to productive use shortly after implementation of the
soil and sediment remedy.

Comment #2:  Representatives of local industries were generally
concerned about the job market.  They noted that manufacturing
jobs have decreased in the area and expressed their desire that
remediation activities not cause any further losses of jobs.
They asked whether local merchants and contractors will be
utilized or benefit from the remedial work to be conducted at the
site.

Response f 2:  EPA does not anticipate any negative impact to the
local economy as a'result of the remedial activities planned for
the GCL property.  It is EPA's intent to remediate the property
as quickly as possible, so that it can be returned to productive
use.

All cleanup activities to date have been funded by the Federal
government.  When hiring contractors to perform work at a site,
EPA must abide by federal procurement regulations.  The
regulations are intended to ensure fair, competitive bidding,
resulting in the hiring of responsible firms, capable of
performing the type of specialized work required at Superfund
sites.  EPA cannot assure that local contractors will be hired to
perform work at the site.  Conducting work at hazardous waste
sites requires certain level of worker health and safety
training, which is often difficult for small local companies to

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afford.   However, local contractors capable of performing
requisite Superfund site work are frequently utilized, since they
may have a competitive advantage over nonlocal contractors who
would incur expenses for travel, lodging, etc.  In addition, EPA
contractors often utilize local services and suppliers (e.g.,
lodging, food, and general supplies).

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 APPENDIX A
PROPOSED PLAN

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Superfund Proposed Plan

                           GCL  TIE  &  TREATING SITE
                                            Operable Unit 2
                                            Town of Sidney
                                      Delaware County, New York
 EPA
 Region 2
                               February 1995
PURPOSE OF PROPOSED PLAN

This Proposed Plan describes the remedial
alternatives considered for the contaminated
-grpunriwatgr »nH ynrfape-wgt-gf ggd'TifmtS located-	
• at the-GCL-Tie & Treating-site and identifies the
preferred remedial, alternative with the rationale
for this preference. The Proposed Plan was
developed by the U.Si Environmental Protection
Agency (EPA), as lead agency, with support from
the New York State Department of
Environmental Conservation (NYSDEC).  EPA is
issuing the Proposed Plan as part  of its public
participation responsibilities under Section 117(a)
 of the Comprehensive Environmental Response,
 Compensation, and Liability Act (CERCLA) of
 1980, as  amended, and Section 300.430(f) of the
 National Contingency Plan (NCP). The remedial -
 alternatives summarized here are described in the
 remedial investigation and feasibility study
 (RI/FS) reports which should be consulted for a
 more detailed description of all the alternatives.

 This Proposed Plan is being provided as a
 supplement to the RI/FS reports  to inform the
 public of EPA's and NYSDEC's preferred remedy
 and to solicit public comments pertaining to all
 the remedial alternatives evaluated, as well as the
 preferred alternative.

 The remedy described in this Proposed Plan is
 the preferred remedy for contaminated
 groundwater and surface-water sediments at the .
 site. Changes to the preferred remedy or a
 change from the preferred remedy to another
 remedy may be made, if public comments or
 additional data indicate that such a change will
 result in a more appropriate remedial action. The
final decision regarding the selected remedy will •
be made after EPA has taken into consideration
all public comments.  We are soliciting public
comment on all of the alternatives considered in
           smfllysis.sectio" oFt.ke FS because  ... .
              *
EPA and NYSDEC may select a remedy other
than the preferred remedy.

COMMUNITY ROLE IN SELECTION PROCESS

EPA and NYSDEC rely on public input to ensure
that the concerns of the community are
considered in selecting an effective remedy for
each Superfund site. To this end, the RI/FS
reports, Proposed Plan, and supporting
documentation have been made available to the
public for a public comment period which begins
on-Mareh 1st and ends on Masch-SOth, 1995.
   Dates to remember:
   MARK YOUR CALENDAR

   March 1st to March 30th, 1995
   Public comment period on RI/FS reports, Pro-
   posed Plan, and remedies considered

   March 8th, 1995
   Public meeting at the Civic Center, 21 Liberty
   Street. Sidney. NY
 A public meeting will be held during the public
 comment period at the Sidney Civic Center on
 March 8, 1995 at 7:00 p.m. to present the
 conclusions of the FS, to elaborate further on the
 reasons for recommending the preferred remedial
 alternative, and to receive public comments.     ;.

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Comments received at the public meeting, as well
as written comments, will be documented in the
Responsiveness Summary Section of the Record
of'Decision (ROD), the document which
formalizes the selection of the remedy.

All written comments should be addressed to:

Carlos R. Ramos, Remedial Project Manager
U.S. Environmental Protection Agency
290 Broadway, 20th Floor
New York, NY  10007-1866
  Copies of the Remedial Investigation'and
  feasibility StiudytReporfcl dated January *
  1995,^Proposed iPIan,' anbVsuppOrting ^ ..
  -»x«S~ ^s*^4>w*^^*••'''?' '••" ''''  -  ';   *  •••-•"
 ^^SOjBroadway^lB^tPlopr^/v/ ,\;;- ;
 SITE BACKGROUND^

 The GCL Tie and Treating site occupies
 approximately 60 acres in an
 industrial/commerdal area of Delaware County,
 New York (see Figure 1). According to an
 analysis of historical photographs conducted by
 EPA and accounts by local residents, wood-
 preserving activities at the site date as far back as
 tKe 1940's.

 The site is bordered on the north by a railroad
 line. A warehouse and a municipal airport are
 located-to the north of the railroad line. Route 8
 and Delaware Avenue delineate the eastern and
 southern borders of the site, respectively.  A
 drainage 'ditch (Unalam Tributary) and woodland
 area lie between Delaware Avenue and the site.
The western portion of the property abuts a small
impoundment and wetlands area. The site
eventually drains via overland flow to the
Susquehanna.River, which is located within.one
mile of the site..

The  site includes two major areas, generally
referred as the "GCL property" and "non-GCl/
property".  The 26-acre GCL property housed a
wood-treating facility called GCL Tie  & Treating,
and includes four structures.  The primary
building housed the wood pressure treatment
operations  including two treatment vessels (50
feet in length by 7 feet hi diameter),  an,office,
and a small laboratory. Wood (mostly railroad
ties) and creosote were introduced into the
vessels which were subsequently pressurized in
order to treat the wood. The remaining three
structures  housed a sawmill and storage space.
The non-GCL portion of the site includes two
active light manufacturing companies (which did
not conduct wood treatment operations) located
on a parcel of land adjacent to the GCL property.
 Approximately 1,100 p'eople are employed'uTa"""
 nearby industrial area. -About 5,000 people' live
 within 2 miles of the site and depend on
 groundwater as then: potable water supply.  The
 nearest residential well is within 0.5 mile of the.
 site.  Two municipal wells,  supplying the Village
 of Sidney, are located within 1.25 miles of the
 site.  A shopping plaza consisting of fast-food
 restaurants and several stores is located approxi-
 mately 300 feet south of the site. Other facilities
 (i.e.,  a hospital, public schools, senior citizen
 housing, and child care centers) are located within
-2.miles of .the site.                   	
                     -  •  • •          .•*•-•
 . ......   •  	•	    ••.   •   • ^=. •.
 The  site first came to the attention of the--  .
 NYSDEC in 1986, after one of the pressure
 vessels used at the GCL facility malfunctioned,
 causing a release of an  estimated 30,000-gallons of
 creosote. GCL representatives excavated the
 contaminated surface soil and placed it in a
 mound; no further action was undertaken at the
 time.

 In September 1990, NYSDEC requested EPA_to
 conduct a removal assessment at the site.
 Consequently, EPA conducted sampling of the
 GCL Tie and Treating  facility in December 1989
 October 1990, and August 1990.  As a result of
 the  data and information that were obtained as
 part of the assessment, a Removal Action was
 initiated by EPA in March 1991.     . .

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 Activities conducted as part of the removal effort
 included: site stabilization (e.g., run-off and dust
 control), delineation of surface contamination,
"installation of a chain-link fence, identification	 "
 and disposal of containerized (e.g., tanks, drums)
 and uncontainerized hazardous wastes (e.g.,
 wastes in sumps); preparation of approximately
 6,000 cubic yards (cy) of contaminated soil and
 wood debris for disposal; and a pilot study to
 determine the effectiveness of composting for
 biore'mediation of-creosote-contaminated soils.

 The site was proposed for inclusion on the
 National Priorities List (NPL) in February 1994
 and was added to the NPL in May 1994. In
 September 1994, EPA signed a Eecord of Decision
 for the first operable  unit which called for the
 excavation and on-site treatment of approximately
 36,100 cubic yards of contaminated soil and debris
 by a thermal desorption process.

 EPA has been conducting a search for potentially
 responsible parties (PRPs).- If EPA determines
 'thartHere~afe' ofiiS" or -ffiore viableTRPs, EPA-will—
 take appropriate enforcement actions to recover
 its response costs pursuant section 107(a) of
 CERCLA, 24 U.S.C. § 2907(A). To date, only one
 PRP has been identified and notified of his
 potential liability  under CERCLA; however, this
 PRP was not considered to be a viable candidate
 to undertake the necessary response actions.

 SCOPE AND ROLE  OF ACTION

 The GCL Tie & Treating site was selected as a
 pilot project for the Superfond Accelerated
 Cleahup:Model (SACM) initiative. The purpose of"
 SAGM is-to-make Superfund cleanups more
 timely and efficient.  Under this pilot, activities
 which would normally have been performed
 sequentially (e.g., site assessment, NPL
 placement, removal assessment) were performed
 concurrently." In  June 1993, while attempting to
 determine if the site would  score high enough for
 inclusion on the NPL, EPA initiated RI/FS
 activities to delineate further the nature and
 'extent of contamination at the site. These
 activities would not typically have been initiated
 until after the site had been proposed to the
  NPL."

  Site remediation activities are sometimes
  segregated into different phases, or operable
  units, so that remediation of different
  environmental media or areas of a site can
proceed separately, resulting in an expeditious
remediation of the entire site. EPA has
designated two operable units for the GCL Tie &
Treating site as described below.         •   -

  »•  Operable unit 1 addresses the remediation of
contaminated soils found on the GCL-property
portion of the site. This unit is currently in the
remedial design phase.

  >•  Operable unit 2 addresses the contamination
in the soils on the remainder of the site (non-
GCL property), and in the groundwater, surface
water, and surface-water sediments. This is the
final operable unit planned for this site and the
focus of this Proposed Plan.

REMEDIAL INVESTIGATION SUMMARY

The nature and extent of contamination found at
the GCL site was assessed through a
comprehensive sampling of soil, groundwater,
surface water, and surface-water sediment.
Sampling was-conduet«d-during-fefee-Fall/WiRter-—
 of  1993. The- investigation focussed on
 contaminants typically associated with the
 creosote wood-preserving process.  Creosote
 contaminants typically found included numerous
 polyaromatic hydrocarbons (PAHs) such as
 benzo[a]anthracene, chrysene,
 benzo[b]fluoranthene, benzo
 [k]fiuoranthene, benzo[a]pyrene, indeno[l,2,3-c,d]
 pyrene and dibenzo[a,h]anthracene.

 The following paragraphs discuss the
 characterization of contamination in the operable
 unit 2'study area, namely, in the non-GCL__
 property soils, groundwater, surface water, and
 surface-water sediments.

 Soils

  Soil samples were collected from monitoring wells
  and soil borings drilled on the GCL property and
  on the non-GCL property.  Samples were also
  collected at off-site  locations to provide
  information on background conditions. Table 1
  summarizes the analytical results for the soil
  sampling for the non-GCL property.  In general,
  relatively low levels of contaminants were
  detected with total PAHs ranging up to 24 parts
  per million (ppm).  Generally, the concentrations
  of metals detected  on-site were not significantly
  above background concentration ranges with the
  exception of beryllium (up to 3.2 ppm), copper (up

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to 176 ppm) and lead (up to 46 ppni), which were
above their representative background
concentrations of 0.6 ppm, 26.2 ppm and 11.2
ppm, respectively:

Table 1.  Summary of Non-GCL Property Soils
Analytical Results
(All values in parts per million [ppm])
Table 2.  Summary of Surface Water Analytical
Results
(All values in parts per billion [ppb])  :
CONTAMINANT
Volatile Organia
'richloroethene
oluene
Total Volatile;
BENCHMARK LEVEL FOR
COMPARISON

0.7
1.5
10
HIGHEST
CONCENTRATION

0.01
0.024
0.042
Polyaronatic Hydrocarbons
Fluoranthene
*yrene
Benzo(a|amhracene
Ihrysene
Oenzo(blfluoranthene
Genzo(klfluoranthene
!enzo(alpyrene
Total PAHs
Mcuk
Aluminum
Arsenic
Beryllium
Cadmium
Chromium 	
Copper
Lead
Nickel
Zinc
SO
50
78
7,840
678 -
78
8
500
9.5
6.3
1.5
2.7
3.2 •
3.2
2.9
24

11,300
8.5
0.6
i.o • •
16.2 "
26.2
11.2
24.4
S7.0
14,300
10.4
3.2


20.8
176
46
29.6
78.9
Benchmark levels lor comparison are NYSUtC soil cleanup objectives tVOCs only),
background levels (metals only), and risk-based cleanup levels for Industrial use
(PAHs only, consistent with Record of Decision for operable unit 1). •
 Surface Water and Surface-Water Sediments

 Surface water samples and sediments were
 collected along the Unalam tributary and the
 impoundment. Tables 2 and 3 summarize the  .
 analytical results.

CONTAMINANT
Arsenic
Copptr
Manganese
Nickel
Zinc

BENCHMARK LEVEL FOR
COMPARISON
0.018 '
12
Not available
6.1
110

HIGHEST
CONCENTRATION
11.4
35.2
8,710
19.6
116
                                                    benchmark; levels tor comparison are the low value lor that contaminant Horn
                                                    either USEPA water quality criteria or NYSDEC ambient water standards.
                                                    Table 3. Summary of Surface-Water Sediment
                                                    Analytical Results
                                                    (All values in parts per billion [ppb])
CONTAMINANT
Polyaranutic Hydrocarbon*
enzofalanthracene
Chrysene
Benzo|b]fluoranthene
ienzolklHuoranthene
Benzo(a]pyrene
lndeno( 1 ,2,3-cd|pyrene
Total PAH
BENCHMARK LEVEL FOR
COMPARISON

20.8 . '.
20.0
2O.8
20.8
20.8
8.8
Not available
HIGHEST
CONCENTRATION

2,200
4,000
4,300
3,100
1,700
1,100
23,850
Metati ..'-"• .
Arsenic" : ".
Chromium
Copper
Lead
Manganese
Mercury
Nickel
Zinc
5,000

26,000
19,000
27,000
428,000
110
22,000 . •
85,000 -~ ' • • -:
16,400.^ 	
32,000
51,900 -
70,200
547,000 •
690
43,600
173,000 ^i.
Benchmark levels tor comparison are the low .value tor that contaminant tram
either USEPA criteria for aquatic sediments (human health basis enteifa) or
NYSDEC sediment criteria. . " .
 Of the 14 inorganics detected in the surface water
 samples, only arsenic (up to 11.4 (parts per
 billion) ppb) and copper (up to 35.2 ppb)

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 significantly exceeded state or federal ambient
. water quality standards. Elevated PAH
 concentrations were, detected at 3 of the 7	
 sediment sampling locations. PAHs were detected
 in these areas with total concentrations ranging
 up to 23,850 ppb.  The PAH contamination
 detected in the sediments is most likely
 attributed to runoff from the site soils. Lead,
 chromium, and mercury were detected in
 concentrations above background levels which
 could be attributed to regional background
 variations or from off-site sources, as these
 contaminants are not typically associated with  the
 wood-preserving operations conducted at the site.
 The results of the sediment sampling indicate
 that unconsolidated sediments along the Unalam
 tributary and the impoundment along the western
 side of the site contain elevated levels of PAHs.
 The extent of contamination is approximately
 2,850 feet in length,  1.5 feet in width and 0.5 feet
. in depth in the  tributary, as well as a 5-foot wide
. strip along the.edge, of the. impoundment.     	

 Groundwater

 Site-specific geology within the GCL property is
 characterized by a layer of fill approximately 5
 feet thick in the western portion of the site which
 gradually decreases to approximately 2 to 3 feet in
 the eastern section of the GCL property.  The fill
 consists predominantly of silt and clay with
 significant amounts of wood and assorted debris
 on the GCL property.  The fill is underlain by silt
 and clay type soils.

 There are two hydrogeologic systems consisting of
 the  overburden and bedrock units.  The
 overburden unit can be further divided into
 shallow (approx. 5 to 16 feet in depth) und
 intermediate (approx. 11 to 25 feet in depth)
 groundwater zones.  Groundwater is first
 encountered at depths ranging from 5 to 8 feet
 below grade around the site.  As a general rule,
 groundwater flow in the overburden aquifer
 appears to be in a north-northwesterly direction;
 groundwater movement in the bedrock appears, to
 be in a northerly direction. Permeability of the
 overburden and bedrock soils is relatively low;
 groundwater flow through the bedrock aquifer
 occurs primarily through fractures.

 Six previously existing groundwater monitoring
 wells and 14 newly installed wells were sampled
during the RI. Samples were collected during two
separate rounds -of sampling, and analyzed-for a
full range of organic and inorganic constituents.
Table 4 summarizes the analytical results. .Two
main groups of organic compounds were found in
the groundwater above drinking water standards,
namely, volatile organic compounds (VOCs) and
PAHs. PAHs, including benzo[b]fluorantliene (up
to 3 ppb), benzo[a]pyrene (up to 2 ppb), chrysene
(up to 4 ppb) and benzene (220 ppb) significantly
exceeded drinking water standards, and are the
same type of contaminants as those found in high
concentrations in the site soils.  Chlorinated
VOCs such as vinyl chloride (up to 4,700 ppb),
1,1-Dichloroethane (up to  1,200 ppb), cis-1,2-
dichloroethene (up to 4,300 ppb), and
trichloroethene (up to 1,000 ppb) were also found
at concentrations exceeding drinking water      •
standards, however, they are most likely not
related to the activities that took place at the
GCL site. It is likely that the chlorinated VOCs
originated fi=om-the--former Route 8 Landfill*•  •••
located across from Delaware Avenue and
hydraulically upgradient from the GCL site. The
data obtained during the RI suggest that the
contaminant plume originating at the Route 8
Landfill  extends beneath much of the GCL site.
Currently, the Route 8 site is being remediated
under the New York State hazardous waste.
remediation program; a groundwater collection
 and treatment system designed to address the
 groundwater contamination was constructed and
 recently started operation.

 Aluminum, (up to 6,210 p'pb), iron (up to 37,600
. ppb), manganese (up to 17,300), antimony (up to
 44.3 ppb), chromium (up to 166 ppb),-and nickel
 (up to 131 ppb) were  detected in groundwater
 samples in concentrations significantly above
 drinking water standards.  However, the presence
 of most of these metals at elevated concentrations
 in background and off-site wells is potentially
 indicative of background levels and/or off-site
 sources.                  .           .

 It is estimated that the GCL cbntaminnpfc plume
 extends over an area of approximately 173,500
 square feet with a thickness of approximately 45
 feet.  The volume of water which exceeds
 drinking water standards is estimated at 10
 million gallons.

 During the  RI, a creosote product layer (referred

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 as dense nonaqueous phase liquid [DNAPL])
 wasdiscovered in the shallow groundwater, in a
 localized.area.near_the wood treatment/process
 buildings.  The DNAPL appears to be perched on
 many thin soil layers rather than in a single well-
 defined pool. It is estimated that the DNAPL
 layer ranged from 1 to 2 feet in thickness, and
 contained concentrations of PAHs in excess of
 8,000 ppm. The volume of the DNAPL kyer is
 estimated at 10,000 to 30,000 gallons. The data
 suggest that the DNAPL layer is contained within
 the property boundaries. DNAPLs are heavier
 than water, and have a tendency to sink. PAH
 compounds, which are the principal components
 of creosote, are extremely immobile and tend to
 sorb to the aquifer rather than move with the
 groundwater.  DNAPLs constitute  a highly
 significant source of soil and groundwater
 contamination at the site.

 SUMMARY OF SITE RISK

 Based upon the results of the investigations, a
 baseline risk assessment was conducted to
 estimate the risks associated with  current and
 future site conditions. The baseline risk
 assessment estimates the human health and
 ecological risk which could result from the
 contamination at the site, if no remedial action
 were taken.

 Human Health Risk Assessment

 A four-step process is utilized for assessing site-
 related human health risks for a reasonable
 maximum -exposure scenario:  Hazard
' Jdepri/lcaffpiri-identifies the contaminants of
 concern at the site based" on several factors such
 as toxicity, frequency of occurrence, dnd
 concentration. Exposure Assessment-estimates -
 the magnitude of actual and/or potential human
 exposures, the frequency and duration of these
 exposures, and the pathways (e.g., ingesting
 contaminated well-water) by which humans are
 potentially exposed. Toxicity Assessment-
 determines the types of adverse health effects
 associated with chemical exposures, and the
 relationship between magnitude of exposure
 (dose) and severity of adverse effects (response).
 Risk'Charocterization—svamnaiizes and combines
 outputs of the exposure and toxicity assessments
 to provide a quantitative assessment of site-
 related risks.
The baseline risk assessment began with selecting
contaminants of concern which would be
representative of site risks.. These contaminants
are summarized in Table 5, and include several
contaminants which are known to cause cancer in
laboratory animals and are suspected to be human
carcinogens. In addition, since the current land
use of the property is industrial, and based on
input from the community and local officials, it
was assumed that future land uses of the property
would continue to be industrial.

The baseline risk assessment evaluated the health
effects which could result from exposure to
contamination as a result of:

  > Ingestion and inhalation of soil by young
children and adult residents living off-site;

  •• Ingestion, inhalation and dermal contact with
soil by older children and adults trespassing on
the site;
 ~V Tngestion and dermal contact with surface
 water and sediments by older children and adults
 trespassing on the site;

  >• Ingestion, inhalation and dermal contact with
 groundwater by children and adults living in the
 vicinity of the site in the future; and

  >• Ingestion, inhalation and dermal contact with
 soil by on-site workers.

 Current federal guidelines for acceptable
 exposures are an individual lifetime excess
 cardnogemc risk m_the range of lO^-toJ-O"6 (e.g.,
 a one-in-ten-thousand to;a:one-m-a-miilion excess
 cancer risk) and a maximum health Hazard Index
 (which reflects noncarcinogenic effects for a
 human receptor) equal to 1.0.. A Hazard Index
 greater than 1.0 indicates a potential for
 noncarcinogenic health effects.

 The results of the baseline risk assessment
 indicate that of all pathway- scenarios evaluated,
 only one, future consumption of groundwater,
 poses a potential health threat  Although site
 groundwater is not currently being used for
 human consumption, under a hypothetical future
 use scenario, children and adults consuming
 contaminated groundwater in the vicinity of the
 site would be at risk. The total potential

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Table 4.  Summary of Groundwater Analytical Results
(All values in parts per billion tppbl)
CONTAMINANT
Volatile Otjanlct
Vinyl chloride
JhJoroctnmc
ficthyicnc cfuortdc
1.1-Ofchloroethene
1,1-Dichlonechane
cis-1 ,2-Olchloroethene
'richloroethene
ienzene
BENCHMARK LEVEL FOR
COMPARISON

2
5
S
7
S
70
5
5
GO. PROPERTY
HIGHEST CONCENTRATION


•

8
IS
36
•48
220
MON-Ca PROPERTY •
HIGHEST CONCENTRATION

4,700
19
25
17
1,200
4300
1,000
9
3FF-SITE
-UGHEST CONCENTRATION




3
13
29
30

Polyaromalic Hydrocarbon!
3enzo(a)anthracene
Chryiene
Denzo(b|fluorantliene
Benzolklfluoramhenc
Benzofalpyrene
lndeno(1,2,3-cdlpyrent
0.1
0.2
0.2
0.2
0.2
0.4
y
4
3
2
2
0.7












Mctali
Aluminum
Antimony
Arsenic
Cniuiuiutix . -
Iron • • •
Manganese
Nickel
SO
6
SO
100.
SO ....
so
100
2,230
44.3
7.8
40.7 — 	
37,600 	
17,600
74.2
6,210
10
51.1
166 ......
15,400'
3.360
131
827

5.4 '
177 "••
1,220 	
519
35.2
 wncnnunc levels lor comparison are taken trom UStPA and NYSLKJH drinking water MCLs. blank spaces denote a value below analytical detection limit.
carcinogenic health risk due to ingestion,
inhalation and dermal contact with contaminated
groundwater (from i»ite related-and upgradient
contaminant sources) by future children and adult
residents is 1.3 x 10"1. For site-related
groundwater contamination only, the total
potential carcinogenic health risk is 7.1 x 10"4.
These risk numbers mean that approximately one
person out of ten and one person out of ten-
thousand respectively, would be  at risk of
developing cancer, if the site were not
remediated.  The total potential carcinogenic
health risks (via exposure to surface water,
sediments, and soils) to tbTe-other potential
receptors were within EPA's acceptable range and
varied from liT6 to lO'12. The HI is less than 1.0
for all receptors, except for exposure to
groundwater under the future use scenario (up to
HI=387) and exposure to surface water under
current and future uses (up to HI=6).

-------
 Ecological Risk Assessment

 A four-step process is utilized for assessing ....
"site^related" ecological risks for a reasonable
 maximum exposure scenario: Problem Formula-
 tion - a qualitative evaluation of contaminant
 release, migration, and fate; identification of
 contaminants of concern, receptors, exposure
 pathways, and known ecological effects of the
 contaminants; and selection of endpoints for
 further study. Exposure Assessment—&
 quantitative evaluation of contaminant release,
 migration, and fate; characterization of exposure
 pathways and receptors; and measurement or
 estimation of exposure point concentrations.
 Ecological Effects Assessment-literature reviews,
 field studies, and toxicity tests, linking
 contaminant concentrations to effects on
 ecological receptors. Risk Characterization—
 measurement or estimation of both current and
 future adverse effects.

 The ecological risk assessment began with
• evaluating the-contaminants associated wifch-the
 site in conjunction with the site-specific biological
 species/habitat information,  Principal ecological
 communities at the site consist of a deciduous
 wetland area within the southern portion of the
 site (Unalam tributary), and an emergent
 wetland/open water complex (impoundment) to
 the west of the site (see Figure 1).  The wetland
 areas support a wide array of animal species,
 including 5 mammal species, 3 frog species, and
 17 bird species.

 This risk assessment evaluated the site ecological
• communities and their responses to toxicological
 exposures. The threat of lethal accumulations of
 contaminants in plant and «nimn1 populations was
 evaluated. The results of the ecological risk
 assessment indicate the potential for ecological
 impacts due  to the presence of PAH
 contamination in the surface water and sediments
 of the Unalam Tributary, drainage ditches,
 wetlands and pond. The invertebrate and plant
 communities present at the site appear to
 bioconcentrate PAHs. Since both aquatic plants
 and invertebrates form a portion of the diets of
 wading birds and waterfowl, their diet poses a
 potential-exposure route.  Although adult mallard
 ducks subjected to dietary exposure of levels
 similar to those found on site displayed no toxic
 effects, studies have shown significant mortality
and deformities in mallard embryos and ducklings
following exposure to similar levels of PAHs.
Therefore, ingestion by breeding adult waterfowl
may affect nesting success on the wetland
habitats present on  and adjacent to the site.

Actual or threatened releases of hazardous
substances from this site, if not addressed by the
preferred alternative or one of the other active
measures considered, may present a current or
potential threat to public health, welfare or the
environment.                     • .   ...  .

REMEDIAL ACTION OBJECTIVES

Remedial action objectives are  specific goals to
protect human health and the  environment.
These objectives are based on available
information and standards such as applicable or
relevant and appropriate  requirements (ARARs)
and risk-based levels established in the risk
assessment.

Organic contamination-has been detected at the — -
site at concentrations above levels determined to
be protective of human health and the
environment in groundwater and sediments,
respectively. Therefore, the following remedial
action objectives have been established for the
contaminated soil:                     •     •

  > Prevent public and biotic exposure to contami
nant sources that present a significant threat (con
taminated groundwater and surface-water
sediments); and,

  >• Reduce the concentrations of contaminants-in;
the groundwater to levels which are protective of.;
human health and  the environment (e.g.,
wildlife).

  »• Prevent further migration  of groundwater
contamination.

SUMMARY OF REMEDIAL ALTERNATIVES

 CERCLA requires that each selected site remedy
 be protective of human health and the   :  •;"-":
 environment, be cost-effective, comply with other
 statutory laws, and utilize permanent solutions   ".
 and alternative treatment technologies and
 resource recovery alternatives to the maximum
 extent practicable. In addition, the statute
                                                 8

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Table 5.  Chemicals of Potential Concern
        Croundwater

        / "etone
        Benzene
        2-Butanone
        Carbon tetrachloride
        Chlorobenzene*
        Chloroform •
        Chloroethane*
        1,2 Dichlorobenzene
        1,1 Dichloroethane
        1,2 Dichloroethane*
        1,1-Dichloroethene
        cis-1,2 Dichloroethene
        trans-1,2 Dichloroethene*
        Ethyibenzene
        Methylene chloride*
        4-Methyl^2-pentanone
        Styrene
        Tetrachloroethene*
        Toluene-		••  - •
        1,1,1 -Trichleroethane -
        1,1,2-Trichlioroethane*.
        Trichloroethene
        Vinyl chloride
        Xylenes
        Acenaphthene
        Anthracene   •
        Benzo(a)anthracene
        Benzo(b)flouranthene
         Bis(2-ethylhexyl)phthalate
        Chrysene
         Fluoranthene
         Fluorene
         2-MethylnaphthaIene*
         2-Methyiphenol        -
         4-Methyiphenoi
        . Naphthalene
         Phenol
         Pyrene
         Aldrin
         Alpha BHC
         beta BHC*
         gamma  BHC
         Chlordane
          ODD*
          DDE     •-_   .      .
          Dieldrin   ...     : .
          Endrin
          Heptachlor epcxide
  * Not a contaminant of concern when Route 8 wells are excluded.
Antimony
Arsenic*
Barium*
Chromium
Copper
Manganese
Nickel
Selenium
Silver
Vanadium
Zinc
 Soil

 Acenaphthene
 Anthracene
 Benzene
 Benzoia)anthpacene
 Benzo(a)pyrene
 Benzo(b)fluoranthene
 Benzo(k)fluoranthene
 Bis(2-ethylhexyl)phthalate
 Chrysene
 DDT
 Dibenz(a,h)anthracene
 Ethyibenzene
 Flouranthene
 Fluorene
 Indeno (1,2,3-cd)pyrene
 Methoxychlor
 4-Methylphenol
 Naphthalene-   •  --- --.
 PCBs
 Pyrene
 Styrene
 Toluene
 Xylenes
Surface'Water

Arsenic
Barium
Chloroethane
Chromium
Copper
Manganese
Nickel
Selenium
Zinc
 Sediment

 Acenaphthene
 Aldrin
 Anthracene
 Benzo(a)anthracene
 Benzo(a)pyrene
 Benzo(b)fluoranthene...  .
. Ben2o(k)fluoranthene
 Bis(2-ethylhexyl) phthalate
 Chlordane
 4-Chloro-3-Methylphenol
 2-Chlorophenol
 Chrysene
 DDT
 2,4-Dinitrotoluene
 Endosulfan
 Fluoranthene
 lndeno(1,2,3-cd)pyrene
 Methylene Chloride
 PCBs
 Pentachlorophenol
 Phenol  .:         .    .
 Pyrene

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includes a preference for the use of treatment as
a principal element for the reduction of toxicity,
mobility, or volume of the hazardous substances.
Implementation time includes time necessary to
contract and design the alternative.

In the spirit of the SAGM initiative and relying oil
the Agency's technology selection guidance for
wood-treating sites, EPA considered technologies
which have been consistently selected at wood-
preserving sites with similar characteristics (e.g.,
types of contaminants present, types of disposal
practices, environmental media affected) during
the development of remedial alternatives.

The alternatives developed for groundwater (GW)
are:
Alternative 1:  No Action
 Capital Cost:
 0 & M Cost:
 Present Worth Cost:

 Implementation Time:
  Not Applicable
  $27,200 for biannual
• • monitoring
 '$20,000 each five-year
  review ~
  $380,700 (over 30
  years)
  Not Applicable
 The Superfund program requires that the No
 Action alternative be considered as a baseline for
 comparison with other alternatives. The No
 Action alternative for the contaminated
 groundwater would only include a long-term
 monitoring program. The contaminated
 groundwater and DNAPL present in the
 .subsurface would be left to naturally attenuate
"without-any treatment. The long-term
 monitoring program would consist of semiannual
 sampling for PAHs at existing wells on-site and
 around the site. A 30-year monitoring period was
 assumed for estimating the cost of this
 alternative. A total of six existing monitoring
 wells would be utilized to sample the groundwater
 to determine whether the concentration of the
 contaminants of concern have been lowered to
 cleanup levels through natural attenuation and to
 monitor the migration of contaminants and free-
 phase DNAPL in areas surrounding the site.

 Because this alternative would result in
 contaminants being left on-site above health
 based levels, the site would have to be reviewed
                         every five years for a period of 30 years per the
                         requirements of CERCLA. These five-year
                         reviews would include the reassessment of human
                         health and environmental risks due'to the
                         contaminated material left on-site, using data
                         obtained from the monitoring program.

                         Alternative GW-2, Option A: Extraction, on-
                         site treatment via activated carbon
                         adsorption, and discharge to surface water
                          Capital Cost:
                          0 & M Cost:
                          Present Worth Cost:
                          Implementation Tune:
                         $1,883,100
                         $603,300 pen year
                         $9,369,400  •
                         24 months
The major features of this alternative are
groundwater extraction, collection, treatment and-
discharge of treated groundwater.  The treatment
system would consist of an oil/water separator for
phase separation, followed by pretreatment for
manganese removal (necessary to eliminate
potential interferences with subsequent treatment
processes) and removal of organic contaminants—
by activated carbon adsorption. The treated      ;.
groundwater would be discharged to the small
unnamed stream adjacent to the site. Although it
is likely to take considerable longer than 30 years
to achieve remediation goals, the treatment plant
design and cost estimate is based on an operating
period of 30 years.

The extraction/collection system would include a
combination of a collection trench for shallow
groundwater and an extraction wellfor the
intermediate groundwater.  The trench would be
approximately 700 feet long and would be located
at the northwestern (downgradient) boundary-of-
the site. It is estimated that approximately 0.4
gallons per minute (gpm) of groundwater would  -•
be pumped from the collection trench, and
approximately 26.4 gpm would be pumped from
the extraction well to the on-site treatment
system.

In addition to groundwater extraction, if the  	
DNAPL is found to be pumpable, DNAPL :
extraction wellpoints would be installed in areas
of suspected DNAPL. It is envisioned that four
wellpoints would be installed in the shallow
 overburden and would have low sustainable
pumping rates (less than 1 gpm in total).  Total
 flow to the on-site treatment system would be
                                                10

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approximately 30 gpm. All pumping rates would
be refilledduring the design phase based on
pumping tests. Extracted grbundwater would be"
delivered to a collection, tank before treatment.

Because of the nature of the  creosote
contaminants and the observation of DNAPL
during field activities, oily product is likely to be
present with the extracted groundwater. Heavy
or light product would be separated using an
oil/water separator. Solids and/or heavy product
would settle by gravity into the separator's sludge
hopper and would be removed periodically for
 disposal to a permitted treatment facility. Lighter
 product would float to the surface and be removed
 by a skimmer for disposal/reuse at a licensed off-
 site treatment/recycling facility.

 The pretreatment system would consist of an
 individual treatment train designed for  the
 removal of manganese.  Manganese would be
 removed" through pH adjustment,  oxidation,
 precipitation, coagiilatibn, clarification,	
 neutralization, and filtration steps with the
 addition of caustic, acid, and polymer. Sludges
 produced during this step would be stored in
 drums or rolloffs, and sent out to an approved
 disposal facility. Filtration may be required to
 further pretreat the effluent

 After pretreatment,  groundwater would be
 pumped to a carbon adsorption system consisting
 of two carbon beds connected in series. Organic
 contaminants (PAHs) would be removed by the
 carbon adsorption units to target groundwater
 cleanup levels." The spent carbon would be
 collected and shipped for off-site disposal or	
 regeneration and reuse.

  Treated groundwater would be discharged via a
  culvert to the small unnamed stream located on
  the southern border of the  site. This stream in
  turn discharges to an unnamed tributary to
.. Unalam Creek, which eventually discharges to the
  Susquehanna River. - The discharge structure
  would include appropriate., erosion control devices
  such as rip rap and energy  dissipation features.
  The  discharge would comply with the>  New York
  State Pollutant Discharge Elimination System
  (NYSPDES) requirements.  All. waste residuals
  generated from the treatment process would be
  transported off-site to a permitted treatment and
  disposal facility, or  (in the  case of carbon) to a
recycling facility.

The goal of this alternative is to restore  -
groundwater to .drinking water quality. However,
due to the characteristics of creosote (e.g.,
extremely viscous and difficult to pump) and the
 complex hydrogeological setting, it is unlikely
 that this goal will be achieved within a reasonable
 time frame for areas containing the creosote layer
 (e.g., shallow groundwater).' Current estimates of
 shallow ground water remediation are on the
 order of several hundred years.  As such", it is
 likely that chemical-specific ARARs will "be waived
 for those portions of the aquifer based on the
 technical impracticability of achieving further
 contamination reduction within a reasonable time
 frame.  If groundwater restoration is  not feasible
 or practical, the alternative may then focus on  •
 containing the extent of groundwater
 contamination within the site boundaries.
 Restoration of the groundwater outside the
 DNAPL source areas (e:g.; intermediate
 groundwater) is likely to be feasible,  sinceit is
 mostly contaminated with mobile organic
 contaminants (e.g., benzene). ..;..,..,  ;i

 During design or operation of the system, it may
  also be determined that natural attenuation or
  enhanced biodegradation (e.g., introduction of air
  to increase  the rate of biodegradation) would be
  able to achieve a similar level of contaminant
  removal and containment as groundwater
  extraction and treatment, but at a lower cost.
  Such  information would be utilized during the
  remedial design to maximize the effectiveness and
  efficiency of the system. ;-The imVma^'rm would
•• - also-be used to reassess the time frame .and.
  technical practicability of achieving cleanup
  standards.

  Alternative GW-2, Option B: Extraction, on-
   site treatment via biological treatment, and
   discharge to surface water   .

   Capital Cost:              $2,058$QO ' '
   O &  M Cost:              $626,500 . .      . .
   Present Worth Cost   —  $9,832,800 ^
 ; Implementation Time:     24..months -.

   This option is virtually identical to Alternative 2,
   option A.  The only difference is that, following
   pretreatment, the remaining contaminants in the
   groundwater would be pumped to an aerobic
                                                  11

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 biological reactor for treatment. This reactor
 would contain bacterial cultures capable of
_ degrading, the contaminants in the groundwater.
 Wastes (e.g., sludges) generated during the
 treatment process would be disposed off-site at a
 permitted disposal/treatment facility.

 Alternative GW-3: Extraction, cm-site
 pretreatment, discharge to publicly owned
 treatment works (POTW) for finpl treatment
Capital Cost:
O & M Cost:
Present Worth Cost:
Implementation Time:
                          $1,904,000
                          $613,600
                          $9,518,200
                          24 months
 The major features of this alternative are
 groundwater extraction, collection, pretreatment
 and discharge to the local POTW. In order to
 comply with POTW influent requirements,
 manganese would have to be removed from the
 groundwater. This would be accomplished by
 using conventional pretreatment methods for —
 manganese removal sucn'as the treatment' £fain
 described under Alternative GW-2. The
 extraction/collection system and pretreatment for
 this alternative would 'also be the same as that  :
 discussed for Alternative GW-2.  Therefore, only
 those operations that7 differ from previous
 alternatives are discussed below.

 Treatment of organic contaminants would be
 accomplished by the Village of Sidney POTW
 utilizing a conventional sanitary wastewater
 treatment process consisting mainly of aerobic
 biodegradation. The facility was designed for a   -
 maximum wastewater treatment capacity of 13 . .:.
 million gallons'per day (MGD),'and currently
 operates at an average capacity of 0.6 to 0.7 MGD.
 Effluent from the pretreatment system would be
 discharged to the sanitary sewer line via a
 metered control manhole, which would record
 flow to the POTW. The nearest sanitary sewer is
 located parallel to Delaware Avenue, .
 approximately 80 feet south of the roadway.

 Groundwater would have to meet pretreatment
 requirements prior to discharge to the POTW.
 The Village of Sidney Municipal Code governs
sewer use within the. Village and regulates the
discharge of wastes into the POTW. The Village
has indicated that final acceptance of the
pretreated GCL wastewater would not be available
until a detailed application is submitted.

It is noted, however, that due to the
characteristics of creosote (e.g., extremely viscous
and difficult to pump) and the complex
hydrogeological setting, it is unlikely that this
goal will be achieved within a reasonable time
frame for areas containing the creosote layer (e.g.,
shallow groundwater). Current estimates of
DNAPL remediation are on the order-of several
hundred years. As such, it is likely that chemical-
specific ARARs will be waived for those portions
of the aquifer based on the technical
impracticability of achieving further
contamination reduction within a reasonable
timeframe.

The alternatives developed for surface-water
sediments (SD) are:
                                                 Alternative SD-1:  No Action
                                                 Capital Cost:
                                                 O & M Cost:
                                                 Present Worth Cost:
                                                 Implementation Time:
                          $0
                          $18,900 for biannual
                          monitoring
                          $20,000 for each five-
                          year review
                          $277,700
                          6 months
                                                 The No Action alternative for the sediments at
                                                 the -GCL site would consist of a long-term
                                                 monitoring program.: For cost-estimating
                                                 •purposes, it is assumed that sediments" would be
                                                 monitored semiannually and that eightsediment
                                                 samples would be collected and analyzed. '

                                                 Because this alternative does not include contami
                                                 nant removal, the site will have to be reviewed
                                                 every five years for a period of 30 years per the
                                                 requirements of JCERCLA^ as^amended.^These
                                                : five-year Teviews would Jindude^tiie. reassessment
                                                 ofhuman health and^ envjujp^enj&alJrSk^due to
                                                 the contaminated maten^" left pn-|ite^ing data
                                                . obtained from the monitoring
                                                12

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 Alternative SD-2: Excavation, treatment and
 disposal with GCL- property soils

 Capital Cost:              $298,400
 0 & M Cost:              $0
 Present Worth Cost:      . $298,400
 Implementation Time:     24 months

 The contaminated sediments would be excavated
 during periods of no or low flow using
 conventional earth'moving equipment such as
 backhoes, bulldozers, etc. The total volume of
 sediments to he excavated is  estimated to he 125
 cy. Excavation would be performed under
 moistened conditions to minimize the generation
 of fugitive dust. Erosion and sediment control
 measures such as silt curtains would be provided
 during excavation to control migration of
 contaminated sediment.  Adjacent wetlands would
 be protected by erosion and sediment control
 measures.

 The sediments would be'treated via thermal
 desorption along with  the GCL property soils.(see
 Record of Decision dated 9/30/94);  the design of
 the remedy was recently initiated.  A typical
 thermal desorption process consists of a feed
 system, thermal processor, and gas  treatment
 system (consisting of an afterburner and scrubber
 or a carbon adsorption system).  Screened
 sediments are placed in the thermal processor
 feed hopper.  Nitrogen or steam may be used as a
 transfer medium for the vaporized  PAHs to
 minimize the potential for fire.  The gas would be
. heated and then .injected into the thermal
. processor atia-typical operating temperature of
 700°F to 1000°F, PAH contaminants of concern
 and moisture in the contaminated sediments
 would be volatilized into gases, then'treated in
 the off-gas treatment  system. Treatment options
 for the off-gas include burning in an afterburner
 (operated to ensure complete destruction of the
 PAHs), adsorbing contaminants onto activated
 carbon, or collection through condensation
 followed by .off-site disposal.  Thermal desorption
- achieves approximately 98 to 99 percent reduction
 of PAHs in soiL If an afterburner were used, the
 treated off-gas would be treated further in the
 scrubBer for particulate and acid gas removal A
 post-treatment sampling and analysis program
 would be instituted in order to ensure that
 contamination in the  soil/sediment had been
 reduced to below cleanup levels. The treated
sediment would be redeposited along with treated
soils in excavated areas on the GCL property.

The excavated areas of the intermittent stream
and wetlands edge would be backfilled with clean
material and restored to pre-excavation
conditions.  The restoration would take place as
soon as practicable after the sediments have been
excavated, in order to minimize the period of
impact to the stream and wetland. All applicable
wetlands management guidelines would be
followed.
                                 *
Alternative SD-3: Excavation and off-site
disposal
 Capital Cost:
 0 & M Cost:
 Present Worth Cost:
 Implementation Time:
$820,300
$0
$820,300
24 months
 This alternative consists of excavation of 125 cy
 contaminated sediment as described in'
 Alternative SD-2 and transportation of all
 contaminated materials to an off-site RCRA
 permitted facility for treatment and disposal.
 One hundred twenty-five cy of clean fill would b :
 used to restore excavated areas.  Wetlands. woulr;
 be restored as discussed in Alternative SD-2.

 EVALUATION OF ALTERNATIVES

 During the detailed evaluation of remedial alter-./i
 tives, each alternative is assessed against nine
 evaluation criteria, namely, overall protection of
 human health and the environment, compliance
 with ARARs, long-term effectiveness and  -
 permanence, reduction of toxicity, mobility, or
 volume, short-term effectiveness^   ."-.^
 implementability, cost, and state and community
 acceptance.

 The evaluation criteria are described below.
   »•  Overall protection pf human health and the
 environment addresses .whether or not a remedy
 provides adequate protection and describes how ^
 risks posed through each pathway are eliminated,
 reduced, or controlled through treatment, engi-
 neering controls, or institutional 'controls.

   >  Compliance with applicable or relevant and
 appropriate requirements (ARARs) addr'esses

-------
 whether or not a remedy will meet all of the
 applicable or relevant and appropriate
 requirements of other federal. and  environmental
 statutes and requirements or provide grounds for
 invoking a waiver.

  »• Long-term effectiveness and Permanence
 refers to the ability of a remedy to
 reliable protection of human health and the
 environment over tune, once cleanup goals have
 been met.

  »• Reduction of toxicitv. mobility, or volume
 through treatment is the anticipated performance
 of the treatment technologies a remedy may
 employ.

  *• Short-term effectiveness addresses the period
 of time needed to achieve protection and any ad-
"verse impacts on human health and the
 environment that may be posed during the
 construction and implementation period until
 cleanup goals,are_achieved._

  > Imolementabilitv is the technical and
 administrative feasibility of a remedy, including
 the availability of materials and services needed
 to implement a particular option.

  »• Cost includes estimated capital and operation
 and maintenance costs, and net present worth
 costs.

  »• State acceptance indicates whether, based on
 its review of the FFS report and Proposed Plan,
 the concurs, opposes,  or has no comment on the
 preferred alternative at the. present time.

  >• Community acceptance will be assessed in the
 Record of Decision (ROD) following a review of
 the public comments received on the FFS report
 and the Proposed Plan.

 A comparative analysis of the remedial
 alternatives based upon the preceding evaluation
 criteria follows.

 Groundwater                   .

   > Overall Protection of Human Health and the
 Environment

 Over time, Alternative GW-1 would provide some
limited protection of human health and the •
environment since contaminants would be  = -
attenuated through natural processes (e.g.,
biodegradation, dispersion). Alternatives GW-2
and GW-3 would be protective of human health
and the environment, since they would actively
reduce the toxicity, mobility and volume of •
contaminants in the groundwater, and would
protect groundwater surrounding the GCL site
from further contamination.  Although GW-2 and
GW-3 would result hi significant reduction in the
mass of contaminants present hi'the aquifer, it is
unlikely that full restoration of groundwater
resources would be achieved within a reasonable-
time frame.

  »•  Compliance with ARARs

Alternative GW-1 would not comply with federal
or state drinking water standards or  criteria or
those ARARs required for protection of
groundwater.  Alternatives GW-2 and GW-3 would
be designed to treat the aquifer to
chemical-specific ARARs associated with/state and-
federal groundwater and drinking water
standards. Extracted groundwater would be
treated to achieve NYSPDES requirements under
Alternative GW-2; under Alternative GW-3 the ex
tracted groundwater would be treated to local
pretreatment  standards prior to discharge to the
POTW. Each of these alternatives would be
capable of removing a significant mass of
contaminants  in the groundwater. The goal of
these alternatives is to restore groundwater to
drinking water standards.  However, due to the
characteristics of creosote (e.g., extremely viscous
and difficult to pump) and the complex^
hydrogeological setting, it is unlikely..that this
goal will be achieved within a reasonable time
frame for areas containing the creosote layer (e.g.,
shallow groundwater).  Current estimates of
DNAPL remediation are on the order of several
hundred years.  As such, it is likely  that chemical-
specific ARARs will be  waived for those portions
of the aquifer based on the technical
impracticability of achieving further
contamination reducti.onrwith.in a reasonable
timeframe.      :          ,;   ...    .-

  >• Long-Term Effectiveness and Permanence

Alternative GW-1 would not provide for active
 treatment and would rely on natural attenuation
                                                14

-------
 processes to restore the contaminated aquifer.
 Therefore, this alternative would not be an
 effective long-terni remedy.

 Alternatives GW-2 and GW-3 would reduce the
 potential risk associated with groundwater
' ingestion by extracting and treating  the
 groundwater to remove a significant mass of
 contaminants from the aquifer.  The time to
 achieve these risk reductions is limited by the
 effective extraction rates from the aquifer.
 However, it is unlikely that DNAPL
 contamination present in the shallow aquifer can
 be completely remediated due to the tendency of
 DNAPLs to sorb to the aquifer. Although none of
 the alternatives would be able to clean the aquifer
 to drinking water standards in a short period of
 time, the treatment alternatives would protect,
 surrounding groundwater from  further
 contamination.

   >• Reduction in Toxicitv. Mobility,  or Volume
• Through Treatment

 Alternative GW-1 would not involve any removal
 or active treatment of the contaminants in the
 aquifer; therefore, would not be effective in
 reducing the mobility, toxicity,  or volume through
 a treatment process.  However, over time, natural
 attenuation processes would provide some
 reduction of the toxicity and volume of
 contaminants.

 Alternatives GW-2 and GW-3 would reduce the
 toxicity, mobility and volume of contaminants in
 the aquifer to a larger extent than GW-1 since
 extraction and treatment of groundwater are
 provided.

   *• Short-Term Effectiveness

  The implementation of Alternative GW-1 would
  result in no additional risk to the community
  during remedial activities, since no construction
  or remediation activities would.be conducted.
  Workers involved in periodic sampling of site soils
  would be exposed to minimal risks  because
  appropriate health and safety protocols would be
  followed for this activity. For purposes of this
  analysis, monitoring of the site would occur for 30
  years.

  Alternatives GW-2 and GW-3 involve construction
and operation of an on-site treatment plant.
Procedures for proper handling of the treatment
reagents would be followed for all treatment
alternatives. .Any process residuals generated
would be properly handled and disposed off-site.
The risk to workers involved hi the remediation
would also be minimized by establishing
appropriate health and safety procedures and
preventive measures to avoid direct contact with
contaminated materials and ingestion/inhalation
of fugitive dust.  All site workers would be OSHA-
certified and would be instructed to follow OSHA
protocols.

It is estimated that the treatment alternatives
would take well over 30 years to achieve the
remedial action objectives.  However, a 30-year
period was used for costing purposes. Operation
of the treatment plant would be stopped when
remedial objectives are achieved i.e:, levels of
contaminants in the aquifer are reduced to State
and Federal drinking water standards, unless  it is
determined that ARARs must be waived in
portions of the aquifer.

  »• Implementabilitv . .

Alternative 1 would not involve any major site
activities other than monitoring and performing
five-year reviews.  These activities are easily
implemented.
 The treatment components of Alternatives GW-2
 and GW-3 would be easily implemented, as the
 technologies are proven and readily  available.
 The carbon adsorption technology proposed for
 use in Alternative GW-2A is a proven and
 efficient method for removal of organic
 contaminants. Biological treatment, specified in
 Alternatives GW-2B and GW-3, has been used
 successfully for groundwater contaminated with
 creosote wastes. The manganese removal pretreat
 ment technology required under Alternatives GV.-
 2 and GW-3 is proven and readily available.
 Sufficient space is available on-site for a
 treatment plant.                        - —

 Alternatives GW-2 andt3W-3 would require-
 institutional management of the operation and
 maintenance of the treated groundwater
 discharge system. Off-site disposal facilities  are
 available for the disposal of the oil/water
 separator sludge and skimmings generated from
 Alternatives  GW-2 and GW-3. Disposal (or
                                                  15

-------
recycle) facilities are also available for recovered
DNAPL and the other residues generated from
those alternatives....Although treatment processes
utilized in Alternative GW-3 are proven, it is
uncertain whether the Village of Sidney POTW
would accept the treated groundwater.
Acceptance of the GCL.effluent by the POTW
would be contingent upon factors such as capacity
available, waste characteristics, and permit
requirements.

  ••  Cost

GW-1 is the least expensive of all alternatives but
would not involve treatment. Alternative 1 has a
present worth cost of $380,700 which is associated
with conducting a sampling and analyses program
and five-year reviews over a 30-year period.

Alternative GW-2A would be the most expensive
treatment alternative followed by GW-3 and GW-
2B. However, the cost differences between GW-
2A, GW-2B and GW;3_would be so small as to not
be significant.

  »•  State Acceptance

NYSDEC concurs with the preferred remedy.

  >•  Community Acceptance

Community acceptance of the preferred
alternative will be assessed in the ROD following
review of the public comments received on the
RI/FS reports and the Proposed Plan.

Sediments

 . >•  Overall Protection of Human Health and the
Environment

Alternative SD-1 would not meet any of the
remedial objectives and thus would not be
protective of the environment. Contaminated
sediments would remain on-site and would
continue to pose a risk to the biota.  Natural .
flushing would reduce-contaminants in the
sediments somewhat, especially after the
 contaminated soils on the GCL-property are
remediated.

 Alternative SD-2, involving on-site sediment
treatment and Alternative SD-3 involving off-site
treatment/disposal of sediments, would remove
contamination and eliminate any environmental
threats posed by the sediments. Therefore,'these'"
alternatives would meet remedial objectives.

  »•  Compliance with ARARs

There are no chemical-specific ARARs for the con
taminated sediments. Alternative SD-1 would
comply with appropriate requirements such as
New York State Technical and Administrative
Guidance Memorandums.            ,

Alternatives SD-2 and SD-3 would be designed
and implemented to satisfy all appropriate
requirements and location-specific ARARs
identified for the site.  Excavation activities would
be conducted in compliance with the OSHA
standards, soil erosion, sediment control and
wetland protection requirements. Alternative SD-
2 would also comply with ARARs related to on-
site treatment (e.g., disposal of treatment
. residuals, stormwater discharge requirements and
air pollution control regulations pertaining to
fugitive emissions and air quality standards).
Under Alternative SD-3, excavated  sediments
would be sent to an appropriate
treatment/disposal facility in accordance with
applicable ARARs.                       !

  »• Long-Term Effectiveness

Alternative SD-1 would monitor contamination in
 the sediments and would not remove and/or treat
 contaminants. Therefore, this alternative would
 not reduce the long-term, risks to the
 environment associated with the sediments.

 Alternative SD-2 calls for on-site sediment
 treatment along the GCL-property soils. The soil
 treatment system,  currently under design, would
 reduce the levels of PAH contaminants in
 sediments by 98 to 99 percent.

 Alternative SD-3 would provide longrterm
 protection by removing ihe contaminated'
 sediments which would be sent to.an approved
 disposal facility. Soil cover and revegetation
 would provide protection against erosion. No
 long-term monitoring would be required. -
                                                16

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  »•  Reduction of Toxicitv. Mobility or Volume
Through Treatment

Alternative SD-1. would not provide immediate
reduction in toxicity, mobility or volume of
contaminants because treatment is not included
as part of this alternative. Some reduction may
be realized after the GCL-property soils have
been remediated through natural  attenuation
processes.

Alternatives SD-2 and SD-3 would reduce the
toxicity, mobility and volume of contaminants by
removal and  on-site treatment (Alternative SD-2)
or off-site disposal (Alternative SD-3).

  >• Short-Term Effectiveness

The implementation of Alternative SD-1 would.
not pose any additional risks to the community,
since this alternative does not involve any
construction or remediation. Workers involved in
periodic sampling of sediments would be exposed
to minimal risks because appropriate health and
safety protocols would be followed for this
activity.

Alternatives  SD-2 and SD-3 include activities such
as excavation, screening, shredding, and handling
of contaminated sediments which could result in
potential exposure  of workers and residents to
fugitive dust, and possible suspension of
 sediments,  hi order to minimize potential short-
 term impacts, the area would be secured and
 access would be restricted to authorized personnel
. only. In addition,.dust control measures such .as .
 wind screens and water  sprays would be used  to
 minimize fugitive dust emissions from material
 handling.  The risk to workers involved in the
 remediation would also be minimized by
 establishing appropriate health and safety
 procedures and preventive measures, (e.g.,
 enclosed cabs on backhoes and proper personal
 protection equipment) to prevent direct contact
 with contaminated materials and
 ingestion/inhalation of fugitive dust. All site
 workers would be OSHA certified and would be
 instructed to follow OSHA protocols. Some
 increase in traffic and noise pollution would be
 expected from site activities.  Short-term impacts.
 may be  experienced for about a six-month period
 which is the estimated time for construction  and
 remedial activities.
Under Alternatives SD-2 and SD-3, short-term im
pacts on the environment from removal of
vegetation .and. destruction of habitat could occur. .
A plan would be prepared and implemented to
minimize and restore (Le., revegetate) any
damage to the environment. Erosion and
sediment control measures such as silt curtains
and berms would be provided during material
handling activities to control migration of
contaminants.

  >•  Implementability
                                  »
Alternative SD-1 would not involve any major site
activities except monitoring and sampling.  These
activities would be easily implementable.
Alternative SD-2 would be easily implemented, as
the technology is proven and readily available.  •
The thermal desorption component of this
alternative has been shown to be effective for
destruction of PAHs, and is commercially
available. Sufficient land is available at the site
for operation of a mobile thermal desorption
system and supporting facilities. Alternative SD-3
involves off-site disposal.  Capacity for the small
volume of sediment should be available at a
permitted facility. Implementation of
Alternatives SD-2 and SD-3 would require
 restriction of access to the site during the.
 remediation process.  Coordination with state and
 local agencies would also be required during
 remediation.

  -  Cost

 Alternative SDrl.is.the less expensive alternative,
 but does not provide  treatment  of contaminated
 sediments.  Alternative SD-1 has a present worth
 cost of $277,700 which is associated with
 conducting a sampling and analyses program and
 five-year reviews over a 30-year period.

 Alternative SD-2 is the least expensive of the
 treatment alternatives and has a present worth
 cost of $298,000. The most expensive Alternative
 is SD-3 with a present worth cost of $820,300.

   »• State Acceptance	  .     ."

  NYSDEC concurs with the preferred remedy.
                                                 17

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 »•  Community Acceptance

Community acceptance of the preferred
alternative will be assessed in the ROD following
review of the public comments received .on the
RI/FS reports and the Proposed Plan.

PREFERRED ALTERNATIVE

Based upon an evaluation of the various
alternatives, EPA and NYSDEC recommend
Alternatives GW-2 and SD-2 as the preferred
alternatives for remediation of contaminated
groundwater and sediment on the GCL site.

Alternative GW-2 would address the contaminated
groundwater through the extraction, collection,
on-site treatment and discharge  of treated
groundwater to the surface water. Alternative
GW-2 provides two options for primary treatment
of organics, carbon absorption (GW-2A) and
biological treatment (GW-2B). Given the
information currently available, both options
appear to be equally reliable and cost-effective.
Therefore, a more detailed evaluation of the two
options will be conducted during the remedial
design through treatability studies. The
additional information gathered from the
treatability studies will be used to determine
which option is more appropriate and cost-
effective. As noted above, the information
gathered during remedial design would also be
used to reassess the timeframe and technical
practicability of achieving State  and Federal
drinking water standards.
Alternative SD-2 will address the contamination
by excavating and treating contaminated sediment
on-site through a thermal desorption- process.
Treating the contaminated sediments along with
the GCL-property soils provides an effective and
cost-effective method for addressing the
contaminated sediments. Alternative SD-2 will
also provide for the mitigation of damages to the
aquatic environment which may occur during the
implementation of this alternative.

The preferred alternative would provide the best
balance of trade-offs among alternatives with
 respect to the evaluating criteria. EPA and the
 NYSDEC believe that the preferred alternative
 would be protective of human health and the
 environment, would comply with ARARs (unless it
is subsequently proven to be technically
impracticable), would be cost-effective, and would
utilize permanent solutions and alternative
treatment technologies or resource recovery " "
technologies to the maximum extent practicable.
The remedy also would meet the statutory
preference for the use of treatment as a principal
element.
                                                18

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                                                (APPnOX.)
                                                                                            U.S.  ENVIRONMENTAL PR01CCTION AGENCY
                                                                                                    GCL  TIC  &  TREATING 51 IT
                                                                                                           FIGURE  1
                                                                                                       HISTORICAL LAND U5L"
                                                                                                         SITE LAYOUT MAP

-------
  APPENDIX B
PUBLIC NOTICES

-------
1
The  Oneanta  Daily Star
March 1,  1995
       witn ttie  union were never the same,"
       Alou said. "I am not a strikebreaker. It
       isn't us managers putting this show on.
         "If I leave, it won't be on any kind of
       a leave of absence. If I run away from
       this, it's  for the rest of my life. Other-
       wise I'm going to stick around to see the
       end of this."
         Alou also  attacked  acting  commis-
                •gh,  St. Louis, Texas

                .em, that we have no
                to  make,"  Hemond

                ancel the games was
                baseball. operations
                m  of the  commis-

  Pedro Borbon,  48 years old and 15
years removed from the majors, signed
for  real Tuesday  as a  replacement
player, threw in the  bullpen and  de-
clared himself ready to pitch.
  The Reds erroneously issued a news
release Monday saying they had signed
Borbon. General  manager Jim Bowden
later said that the  right-hander would
  "Sometimes it gets  to  a point  you
want to cry because you've got to make
a decision on something you love more
than anything in the world and  maybe
something that's going to ruin you for
the rest  of your career,"  said Carter,
who plans to play in exhibitions but not
as a regular-season replacement.
  Free agent pitcher Todd Stottlemyre.
who spent the last  six seasons with To-
ronto,  thinks the  players will  face a
huge task trying to win back fans.
  "I think it'll  be important ...  that
maybe the.players do stop and sign a
few more autographs, talk to the fans,"
Stottlemyre said.  "They've  been the
ones who've lost the  most in this thing
and you have to have respect for that."
 reer
 rent  New York Giants
 up. Before  taking the
 ylor  stood  shaking  his
 smiling widely as wres-
 aels  delivered a wild,
 i rant.
 ." met Bam Bam.
""Bam *Bigelow"was"on
 ill field, playing- in the
   wouldn't  be  hearing
 •Tence Taylor," Bigelow
 d  with a  straight  (for
  "I know I could  have
 :ter job than LT."
 ight end Howard Cross,
 in the crowd,  was re-
  giggles at this  point.
 •low concluded his com-
 :This is my world. LT"
 Tinned and announced,
 Dt to love that. That was

 Ues Thomas Randolph,
 .om and Willie Beamon
 :ically agreed.
 11  entertainment  and
 .  cornerback Randolph.
 1 well."
  SERVICE
  W YORK, INC.

  :'with the New York
  :h 10.1995.

  : new feature to the
  UWORX will allow
  . digital capability as
  iow are proposed rates
  =5 (PER HOUR OF USB
       $13.20  '   '
       '$13.20
       $13.20  .
                                                      v°/EPA
                                                   THE UNITED STATES
                                       ENVIRONMENTAL PROTECTION AGENCY
                                                             Invites          .

                                             PUBLIC COMMENT ON THE
                                     PROPOSED CLEANUP OF THE GCL
                                     TIE & TREATING SUPERFUND SITE
                                                               at
                                       DELAWARE AVENUE, SIDNEY,  NEW YORK

                     The U.S. Environmental Protection Agency (EPA) and the New York State Department of Environmental
                     Conservation (NYSDEC) will hold a public meeting to discuss the findings of the Remedial Investigation
                     and Feasibility Study (RI/FS) and the Proposed Plan (PP) for the GCL Tie & Treating Superfund Site.
                     The meeting will be held on.Wednesday, March 8,1995 at 7 pm  in the Sidney Civic Center, 21 Liberty
                     Street, Sidney, NY. The release of the Proposed Plan and the scheduled public meeting are in accordance
                     with EPA's public participation responsibilities under Section 117(a) of the Comprehensive Environmental
                     Response, Compensation and Liability Act (CERCLA) of T980.
                     Site remediation activities at this site were segregated into two different phases, or operable units, so that
                     remediation of different environmental media or areas of the site could proceed separately, resulting in
                     the expeditious remediation of the entire site. The first phase remedy, which was selected this past sum-
                     mer, addresses the contaminated soils and debris on the GCL property portion  of the site; this phase is
                     currently in the remedial design stage. The second and final phase, addresses contamination in the groundwater
                     and surface water sediments.  .                              "             .
                     Eiased on  the available information, the goal of the preferred groundwater remedy for the second phase
                     is to restore groundwater to drinking water quality. However, due to the characteristics of creosote (e.g.,
                     extremely viscous and difficult to pump) and trie complex site hydrogeological setting, it is unlikely that
                     this goal will be achieved within a reasonable time frame tor at least some portions of the aquifer. If groundwater
                     restoration is not feasible or practical, the alternative may then focus on containing the extent of ground-
                     water contamination within the site boundaries, and/or using natural attenuation or other processes to achieve
                     contaminant reduction. The preferred remedy for contaminated surface-water sediments is treatment via
                     thermal desorption along with the GCL property soils.
                      EPA, in consultation with NYSDEC, may modify the preferred alternative or select another response ac-
                      tion presented in this Proposed Plan based on new  information or public comments. Therefore, the pub-
                      lic is encouraged to review and comment on all of  the alternatives identified herein.  Documentation of
                      the project findings is presented in the site file.  These documents are available at the:

                                                      Sidney Memorial Library
                                                            Main  Street
                                                            Sidney, NY
                      Comments of the Proposed Plan will be summarized and responses provided in the Responsiveness Summary
                      section of the Record of Decision. The Record of Decision is the document that presents EPA's final, se-
                      lection  for response actions. Written comments on this Proposed Plan  should  be sent by close of busi-
                      ness, March 30,  1994 to:
                                              Carlos R. Ramos, Remedial Project Manager
                                                U.S. Environmental Protection Agency
                                                      290 Broadway, 20th Floor
                                                   New York, New York 10007-1866

-------
                  APPENDIX C
MARCH 8,  1995  PUBLIC MEETIKG ATTENDANCE SHEETS

-------
/   .NAME
                       i
        UNITED STATES  ENVIRONMENTAL PROTECTION AGENCY
                         .  REGION II           .
                         PUBLIC MEETING
                       .       FOR
               GCL Tie  6 Treating Superfund site
                       Sidney, New York
                   Wednesday,  March 8, 1995
                          ATTENDEES
                    (Please Print clearly)'
    STREET
|Q\  OTkil
                     CITY
ZIP
PHONE
J A Lt># w, j  yj)f .
j?/ ^/./^/y >.:>/-
                                1 3% 3?
                                        1*7-
                          •0/t-
                               (•3v^ ^r
REPRESENTING

                                                            fy

-------
UNITED STATES ENVIRONMENTAL PROTECTION AGENCY
                  REGION  II
                PUBLIC  MEETING
                     FOR
       GCL Tie & Treating Superfund Site
              Sidney, New York

           Wednesday, March 8,  1995
                  ATTENDEES
            (Please Print Clearly)
                                             REPRESENTING
                                           T& a.7* <^
                                                Ui

-------
    UNITED STATES  ENVIRONMENTAL  PROTECTION AGENCY
                      REGION II
                    PUBLIC MEETING   ;
                        FOR
           GCL Tie fi Treating Superfund Site
                  Sidney,  New York

              Wednesday, March  8,  1995
                      ATTENDEES            '
STREET
               (Please Print Clearly)
CITY
ZIP
PHONE
REPRESENTING
                                                By&o

-------
              APPENDIX D
MARCH 8, 1995 PUBLIC MEETING TRANSCRIPT

-------
    U.S.  ENVIRONMENTAL PROTECTION AGENCY  PUBLIC  MEETING

             GCL TIE  & TREATING SUPERFUND SITE
     A public meeting held at the Sidney Civic. .Center,

21 Liberty Street, Sidney, New York, 13838,  on Wednesday,

the 8th day of March, 1995, commencing at 7:06 p.m.
APPEARANCES:
          BEFORE:
CECILIA ECHOLS
Community Relations Coordinator

DOUGLAS GARBARINI, Chief
New York/Caribbean Superfund Section I

CARLOS RAMOS
Project Manager
Ruth I. Lynch
Registered Professional Reporter
                  Empire Court Reporters
                 One Marine Midland Plaza
                  Binghamton,  NY  13901

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      MS. ECHOLS:  Okay, we're ready to begin.  Good

evening, I'm Cecilia Echols,  Community Relations

Coordinator for the GCL Tie and Treating Superfund

Site.  We're here to speak about the second operable

unit regarding the site and to give EPA's preferred

remedy for the groundwater and surface water sediments.

I would assume that everyone received a proposed plan

in the mail and has been able to review it, if not I

think- everyone received one from the table in the back.

I hope everyone has signed in.

      The public comment period began on March 1st, it

ends  on March 30th.  If you have any comments or

questions to ask the EPA you can send in your written

comments to Carlos Ramos, his address is in the

proposed plan.  And he will address all of your

questions in a responsiveness summary which will become

part of  the record of decision.  If you're interested

in  finding out more information about the GCL Tie  and

Treating plant,  there is  an information repository at

the Sidney Memorial Library on Main Street.   And  I'm

gonna pass  it  over to Doug.

       MR. GARBARINI:  Okay, thank  you,  Cecilia.

       My name  is Doug Garbarini, I'm  the  supervisor in

 the Region  II  New York  City office, and Region  II is

 one of ten  regional  office across  the country that EPA
                        Empire Court Reporters
                       One .Marine Midland Plaza
                        Binghamton, NY  13901

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has, and we're responsible for environmental protection

in New York, New Jersey, Puerto Rico and the Virgin

Islands.  I think before we get into the project

details here of the GCL site, what I typically do is go

through a ten-minute spiel on the Superfund process.

But looking out here, I think all of you were present

at the last meeting, so I don't want to necessarily .

bore you with that.  There might be one new face.

      AN ATTENDEE:   I was at one — one meeting,  I     -

don't know  whether  —

      MS. ECHOLS:   The  last  one. was in August you

were here probably  for.

      AN ATTENDEE:   Yeah, original  one.

      MR. GARBARINI:  The original  one..  Okay.   Do  you

 have  a  little bit of familiarity with the Superfund

 process,  or do you —                .

       AN ATTENDEE:   Yeah.

       MR.  GARBARINI:  Would you like  me to go over

 anything for you?

       AN ATTENDEE:  I'm just interested in listening to

 what's being said anyway.   I haven't got any ax to

 grind or anything.

       MR. GARBARINI:  Okay, I guess,  then, what we'll

 do is just get right into the project details.  .And if

 you have any overall related questions about the
                         Empire  Court  Reporters
                        One Marine Midland  Plaza
                         Binghamton, NY  13901

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Superfund process, you know, feel free to ask them at


that point in time.


      Yeah, I guess in general, you know that it's —


we're here representing the Federal Government, and the


Superfund program just deals with federally — federal
                                                   ^

sites on the national priorities list, I guess you're


pretty, much familiar with that.  Okay, so what I'll do


is just pass it right on over to Carlos.


      MR. RAMOS:  My name's Carlos Ramos, and I am the


project manager for this specific site.  And I won't


give you too much detail and background because most of


you know the site, you know where it is and everything,


but I just want to go briefly about some of the


features-of the site.


      This is what they call the historical GCL  — can


everybody  see this, or am  I blocking views?


      MS.  ECHOLS:  I'11 turn off the lights.


      MR.  RAMOS:   Okay.  This  is the site,  this  is the


historical size of the site.   We divided the  site into


two  areas, what we call the GCL portion, which is this


area in general,  and  the non-GCL portion,  which is kind


of historical  site.   We did sampling  throughout all  the


property,  we took surface  sediment samples from the


 drainage ditch that  runs  around the south  to  the side,


 this is the  blue  line here, and also  from  the
                        Empire Court Reporters
                       One Marine Midland Plaza

                        Binghamton,  NY  13901

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impoundment area on this other portion of the site.  We

took soil samples from all the areas of the site.  We

took groundwater samples through all the site.

    .  And just to show you the property, you're pretty

much familiar that the shopping center, the Kmart is on
                                                   ^
this outer edge of the property, the northern area is

Keith Clark and the airport, and Route 8 is on eastern

portion of the site.  Just to give you an idea of how

the site, looks.  .             .           -         ..  • : .

      MS. ECHOLS:  Excuse me, by the way, all of this

information that Carlos  is looking at  is in the

handout.  Okay?

      MR. RAMOS:   The second  slide  is  just to refresh

your minds regarding how EPA  is  —  is  working at this

site.   You know, how  —  how is  our  cleanup working at

this  site.

       We have three main phases.  The  first  one  started

 is what we call a. removal action.   And a removal action

was designed to address the most immediate threats

 associated with the site.  And that was the disposal of

 wastes contained in drums, in tanks, and so forth.

 That phase is completed already.  All the immediate

 threats, potential threats associated with the site in

 terms of immediate concerns are being addressed, and

 that — that activity's close.
                         Empire  Court Reporters
                        One Marine  Midland Plaza
                         Binghamton,  NY  13901

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      Last summer we came here to talk about the focus


feasibility study and to talk about cleaning up the


soils on the GCL portion of the site, and that was that


yellow portion of the figure I showed you before.  That


work is already in the remedial design phase.  Tonight
                                                   *

we are here basically to talk about this last portion


of the site, which is the remedial investigation that


we did in the remaining portions of the site, and that


includes -gr.oundwater, surface water and soils on the


non-GCL portions of the site.  That's outside that


yellow area.


      So we did the remedial investigation, we -- we


actually defined the nature and the extent of


contamination of the site, we did a feasibility  study


which tells you what, can you -- what  shall we do or


what alternative do we have, for addressing that


contamination found at the  site, and  we are  here


tonight with a proposed -remedy.  And  inform  you  on ...


that.


      Now  I'm just  gonna go briefly  about  some  of  the


sampling  soil results  that  we  found  at  the site.  This.


figure  again is  in  your  handout.   Specifically for the


non-GCL property soils.  And just  let me  superimpose


another one here.   Remember,  the non-GCL  is the


western — the  eastern portion of  the site.   Which is
                        Empire Court Reporters
                       One Marine Midland Plaza

                        Binghamton, NY  13901

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the non -- non yellow one.

      You can see from -- from this figure, you compare

the benchmark, which is just a level to help you

compare it, the concentration we found on the site

versus what could be considered as a safe level, in
                                                   *
some cases it's just background, like in the case of

metals, these are typical background concentrations for

this area.  That means if you are testing soils that

were not contaminated,' these were the typical

concentration that you will find.  You can see we

didn't  find really much on the .non-GCL property soils.

      We  just try to take concentrations of organic

compounds  and some concentrations of metals which are

close to  background  in most of  the cases.  The

components that we are most interested with are these

components here, which are creosote-related compounds,

and creosote  was the contaminant that we found  at this

property.  So these" are: the-ones that.we are  more

concerned about, polyaromatic hydrocarbons,  as  you  can

see that even those, these benchmark,  and  what we  found

at the site,  the non-GCL property,  is  —  is  way below

benchmarks.   So that means  that there's  really nothing

much to be concerned about  on the non-GGL property, as

 far as soil  contamination.

       We're  going to the groundwater,  we have, a similar
                        Empire Court Reporters
                       One Marine Midland Plaza
                        Binghamton, NY   13901

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analysis.  We have here five columns.  The first column


is the contaminants of concern,  the second column is


the benchmark, which in this case is the drinking water


standard.  The next column is what we call a GCL


property-highest concentration.   Those highest
                                                   ^

concentration are for that yellow portion of the site.


Then we go into non-GCL property and off-site


contamination, which were wells located outside the


influence of the site.


      We have three types of contaminants here also,


three — three criterias.  We have volatile organics,


polyaromatic hydrocarbons, and metals.  Of these three


contaminants the only one which is site related is


polyaromatic hydrocarbons, because those were the


materials used at the site and those were also the


materials found  in  the site  soils.   For a .specific  case


of  polyaromatic  hydrocarbons, you see  that you compare


the benchmark and the GCL concentration-,-we  indeed


have concentration  in the groundwater  which  is above



the drinking water  standards for most  of  the


polyaromatic hydrocarbons.   We  see  that we don't  find


the hydrocarbon  off site of  the GCL property


wells.   We  didn't find them in  locations  outside  the


GCL site influence.


       You look at volatile  organics, you  see that we
                        Empire Court Reporters

                       One Marine Midland Plaza

                        Binghamton, NY  13901

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found very rather low concentration of most of the


volatile organics at the GCL property.  To compare that


to the MCL, or the maximum contaminant level, the


drinking water standard, which is the same thing, _these


are relatively low levels.  We compared those levels to
                                                   *

non-GCL property wells, you can see they are much, much


higher on wells which are not actually affected by the


GCL site but which are actually affected by other sites


in the region.  So'that tells you that there is a


groundwater problem in the area which is not site


related.   Related to other .sites in the area.


      When you go to metals you'll see that  some of  the


metals are elevated, but there are no metals we can  see


that  are much concern.  So in the case of  manganese,


which is much higher elevated, we also find  it  in


other wells outside of  the property.  Most of the


property relates  to polyaromatic hydrocarbons,  which is


related to the operations .of  the GCL  property,  and.


volatile organic compounds, which  are not related to


the GCL site.


      We  go  into surface water, we see that  we  didn't


 have as much a problem there  neither.  There were


 some — some of  the metals  that were slightly elevated,


 but not really in that significant amout. .Arsenic is


 too high.
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      Then we jump in surface water sediments.   And

again we have contaminants of concern and then we have
        »
the benchmark levels which are kind of guidance volumes

that we use to define whether contaminants may be high	

or low, and we have the concentrations that we find at
                                                   \
the site.  As you can see here, again we have kind of a

relatively high concentrations of polyaromatic

hydrocarbons.  On the sediments which we collected from

the — that drainage, ditch at the site. ..Metals can   •-'

kind of vary through, most of the time metals were at

the -- you know, within one or two times benchmark

levels.

      Here we are, okay.  And this is just a figure

that summarize the extent of groundwater contamination

that we  found at the site.  And let me explain this

thing.   The  orange dots are water wells that we  found

or  installed at the  site, and we sampled them.   You  can

see they cover pretty much the whole  property, there_. ~

are some around here also, you can see with  the  colors.

And what we  did, we  sampled  all those wells  twice,  at

different times of  the  year, we collected  the  data,  and

we  —  based  on  that data  we  developed the  extent of the

groundwater  contamination at the site.   And  this is

what  you have here.

       In this area you  have  an aquifer to be called.
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overburden, which is the first aquifer you encounter,

and  then we have what we call a deep aquifer, which  is

kind of bedrock in this area.  The contamination  that

we found which is related to this site is all within

the  overburden, it's on the overburden aquifer.   Within

that overburden aquifer we -- we divided that zone  —

that aquifer  into two zones, we call them shallow zone

and  then we have the intermediate zone.  And that's

where we  had  contamination which is related  to  the GCIr

 site.  The green color, that's the  shallow aquifer.   In

 that area we  found  that we actually had what we call

.pure creosote.  And that  was  creosote  that was

 used during the operation of  the GCL  facility,  and

 through the years  made  its way into the  soils,  into

 the groundwater.   It's  a  very limited area,  about 250

 feet in diameter,  as far  as  we know.   This,  of course,

 will be very further delineated,  but right now

 that's the approximate?extent of contamination.

       Creosote is a very viscous material,  it really

 binds pretty well to the soils.   Once — once it moves

 to  a certain distance it tends not to move anymore.

 It  doesn't move very rapidly also.  Kind of it's like

 you're pouring oil, it's pretty much putting oil into

 the ground, goes down to a certain level, but  at some

 point  it  reaches a depth where it doesn't move anymore.
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That's what we have here.

      The yellow zone is an area where we have a

different type of contaminant, which is benzene.

Mostly benzene.  Which is more soluble and more --

more mobile than — than creosote.  And that's a bit --

bit bigger plume than the one before.  But .it still

is a relatively small area of the site if you look at

the site as a whole.  This is a relatively small area.

      Okay. .This area is to show you the approximate

extent of sediment contamination at the site.  This is

the drainage ditch that runs about the southern edge of

the site, and the approximate extent of the soil

contamination is around this area here.

      Okay.  So what we did with this information?  Now

we know what's at the site, and we know where that

contamination is.  Based on that we  -- we start what we

call  a risk assessment.  A risk assessment is a

document that  looking at the  concentrations  and looking

at the selection of  contaminants  at  the  site tells

you what kind  of risk might be associated with  that

contaminant.   And  to do that  the  first thing that we  do

is that we identify chemicals of  concern.  And  that's

done  based on the  frequency,  on  the  toxicity and  the

distribution  of  those  contaminants  at the  site.   Once

we do that we go through a  screening process and  we.
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determine which -- which chemical we should be paying


more attention to and which chemicals will be driving


the risks at the site.


      Okay.  And this is basically the result of the


risk assessment that we did.  And in the risk
                                                   *

assessment we look at different things.  We look at


different scenarios and we try to check all the


potential population's that could be in contact with


contamination and could-be at risk.  In this case we


have children and adults living off site but near the


site; children and adults trespassing on the site.  We


have -- we have  — we have children living  in the


vicinity  of  the  site, we have.adults living in the


vicinity  of  the  site, and we have  on-site workers.  And


for those scenarios we  have different pathways.  For


children  living  off site, what will happen, they will


ingest  or inhalate  some of  the soils at the site.   What


would happen with them  if they ingest  or  inhalate  some


of the  soil.  And to  each one of  those pathways  and


scenarios we calculated a potential  health risk  number.


We have to tell  you what would be the  potential  risk  to


that person.


       So if you go scenario for  scenario,  you will see


 that most of the risks  are really reasonable.   The EPA


 has what we call an acceptable  risk range, which is.
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actually 1 to 10,000 to 1 in a million.   That's what we


call acceptable risk range.   If we are within that risk


range, .usually we don't take any action at a site.  In


this — in this case you can see that for most of


these pathways, the risk are very small, they're in the
                                                   *

range of 9 out of a million, 4 out of a million, and so


forth.


      The only two pathway scenarios where they have


some significant risk is for people ingesting, inhaling


or in dermal contact with the groundwater.  And that's


an assumption that that — that's a pathway that


assumes that somebody will be drinking that


contaminated water at the site, which is not the case.


The contamination, as you saw, is a very localized to


what's  in the site; nobody's drinking that water.  But


this  scenario assumes that somebody in the future might


drink that water.  And  if that were the case then you


will  assign;the  risk number to that.               ...


       In the case of people exposed to groundwater,


you'll see that  the risk  are much more  significant.


 In the range of  2 out  of  a  thousand.  And we  have  here,


we decorated the risk  of  groundwater  two ways,  since we


 know that we have a. real  groundwater  problem in the


 area, we  have  contamination there which is  not related


 to GCL in that area, we calculated  the  risk posed by
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exposure to all the contamination in the groundwater,



site related and non site related, and that's the



total.  How we decorated the number just for the GCL



contamination.   .



      As you can see, once you take out in1those times
                                                   *


the contamination, the risk is much more smaller.



      Okay.  Knowing all the contamination that we have



at a site, knowing all the risks posed by the site,



we develop.our alternatives for that contamination at



the site.  An alternative available focus on those two



medias which are the concern.  One media that is a



concern  is the groundwater where we found contamination.



which is above drinking.water standard.  The other



concern- is the surface water sediments, since we found



contamination which  Is above the  benchmark  levels that



we  have established.  We went through  a process  where



we  — we tried to look  at different technologies and



different ways ...of getting up  the  groundwater.   And  we



developed these  three alternatives  for the  groundwater.



       The first  once that we  have is  no action.  We are



 required by law to first consider no  action,  as a



 baseline.  Just to give you a comparison number for the



 rest of the alternatives.   So we did no action,  which



 actually what is involved is  long-term monitoring.



 Just going out there and sampling the wells year after
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year to see what will happen to the contamination.  The

cost for that activity over a 30-year period will be

roughly $380,000.

      The next, alternative that we developed was

extraction of the groundwater, on-site treatment of
                                                   ^
that groundwater, and discharge of the treated

groundwater to surface water.  Which was that drainage

ditch that runs around the southern edge of the

property.            .                 -           .

      In terms of treating the groundwater, we had

different ways that we could do that.  We could do

carbon absorption, which is a very common treatment

technology where you put your contamination through a

carbon filter and at the end you have  clean groundwater

and the carbon retains the contamination.  You can also

go a way of biological treatment, which  is not too

far from what you have in your local wastewater

treatment  facility.                            -  .   ...   .

      We have 'some problem at this  site  regarding the


cleaning up  of the aquifer.   And these —  and it

relates  to the  -- to the  type of contamination we have

there,  and —  and the geology that  we  have at the site.

And the  first  one that we have  is  that creosote, as  I


mentioned before, tends  to bind pretty tightly with

 the soil particles.   So  it is very difficult to clean .
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up areas where we have creosote contamination.  And our

experience has been that in places where we have

topical contamination we pretty much can pump the water

for many, many, many years and still there will be some_

residue creosote in the water.  So that's — that's
                                                   *
very unlikely that we'll be able to clean up that

portion of the aquifer containing creosote.

      However, there is another portion of the aquifer,

and that was the benzene area I showed you before  in

green, and that area is -- we would like it to be

clean.  And about  — well, before we start actually

pumping and treating, we would  like to try some things

which have been tried at other  sites to clean up

groundwater.   And  we would like to see whether

technology  such  as bioremediation would work  for the

benzene,  specifically.  We have seen that  sometimes

benzene can be biodegrated.   By treating  the  soils

you provide the  material-with some  help.   Like  '.in  some

 cases  you can provide oxygen or nutrient  to the

 bacteria and that helps to clean  up the water.

       So this is one of the  things  that we have to

 try before we start pumping and treating to see how-

 much of that we can -— how much contamination reduction

 we can achieve that way.   If not/ you know/ you know,

 we will be then pumping and treating.               .
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      Our first concern is to make sure that the plume

doesn't move from the site, it doesn't leave the site

and move anywhere.  And that's — that's our first

priority.  And once we made sure that that's done, then

we -- we have time to address the groundwater either
                                                   «
through pumping it, to pumping and treating, or to

using some of these natural attenuation processes which

might get us the same type of attenuation, at a more

lower cost.        '  .

      For the second alternative we have extracting the

water, doing on-site treatment and then sending the

discharge to a POTW, which is your local wastewater

treatment facility.
                                        %
      And those are the two alternatives that we have

for  the  groundwater.

      The costs associated with those two alternatives

are  two  million, pretty much.  The differentiation of

the .cost estimates  are wide enough that there's no

significant  difference to  those numbers.  So either

alternative  would cost about  2 million  in capital

costs,  and the  alternative, the alternative for on-site

treatment  and the discharge  of  surface  water,  will

take -- cost about ten million.

       You  can see there  is a  long-term operation  and

maintenance  cost of the  wastewater treatment facility.
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For the -- the discharge to a POTW,  the total cost is


about $9.5 million, that's including the operation and


maintenance over a 30-year period.


      The other media that we are addres_sing is surface


water sediments, and again we have three alternative,
                                                   *

the first one being no action, which we're again


required to include.  And the cost of just monitoring


the sediment contamination will cost -- will be roughly


about 277,000 over a 30-year period. "The other      —


alternative that we have  is the first one, on-site


treatment of those sediments, using the same thermal


desorption system  that we're going to be using £or the


GCL property soils.


      As you might remember from  before, last summer we


selected the remedy  for the soils which actually


includes excavation  of the soils  and treating them


on-site using  that thermal desorption  system.   Since


the  sediment has  the same type  of contamination,  you


could excavate the sediments .and  run them  through the


same treatment system as  you  — as  you've  already


assigned  for  the  soils.   The  cost of doing that will be


roughly $300,000.


       If  you  were to take the same  sediments and you


were to send them off site to a private treatment and


 disposal facility, that would cost  you roughly
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$820,000.

      So those are — we have three alternative, then,

for groundwater,  and three for surface water sediments.

      Do you have any questions at any point, please

feel free to interrupt me.
              •                                     ^
      The next thing that we did was we put those six

alternative through a detailed evaluation process, and

for doing that we have a set of criteria that include

nine elements.  And this is what is required by law.for

us to do.  The first criteria is overall protection of

human health and. the environment.--Second one, in

compliance with all applicable regulations.  The third

one is long-term effectiveness and permanence.  The

next one is reduction of toxicity, mobility, or volume

through treatment.  Next one is short-term

effectiveness, implementability, cost, the  state

acceptance, and that's New York State acceptance;  and

the. last one,, which.is the-one that-we are  here-for,  is

community  acceptance.

      So we put our  alternatives through  that  nine

criteria process.  And based on  that  we are

recommending  that  we implement on  the site  the second

alternative  for the  groundwater,.which is extracting

the groundwater and  treating  the groundwater on-site

with  the discharge of the treated groundwater to
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surface water.  And we are proposing that we  implement

.on-site treatment of the sediments with the soils

on-site.

       So  those  — those two  items must constitute  our

preferred alternative  for the site, and we will'-- we.

would like to hear  from you  in  terms of what  you think

of cleaning of  the  property  using those -- those two

alternatives.

       MS. ECHOLS:   Finished?

       MR. RAMOS:   I think that's pretty much it,  yeah.

      .MS. ECHOLS:   Okay, we're  gonna  open up for

 questions and answers.  Please  state  your name loudly

 so the stenographer can record  it  properly.

       Any questions?  Let me turn  on the lights.

       Don't be shy now.

       AN ATTENDEE:   Are you gonna further investigate

 the possibility of using our wastewater treatment

 facility?                       .   .       ...

       MR. RAMOS:  Yes.

       AN ATTENDEE:  Instead of this, you know, as  John

 Woodisheck  expressed earlier?

       MR. GARBARINI:  Yeah.  I guess based upon the

 meeting  that we had this afternoon it sounded like John

 was  going to be sending in  a comment letter  to us.

       AN ATTENDEE:  I just  thought the people here
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might like to know that, that the thing is even

though these are your recommendations at the moment,

John Woo'disheck, the village .engineer, indicated that

he thought it could be done more cost effectively by

putting it through our wastewater treatment plant,

there are certain details that would have to be worked

but, but.  I thought the people should know- that.

      MR. GARBARINI:  Yeah, I think that's very

important.  As with any of the alternatives that were

mentioned there, the people here could express their

desire for us to implement any one of those, but I

think the Town's willingness to allow us  to use the

POTW is a very  important consideration foflus.  And  I

guess John will be putting something  in writing to that

effect.

      AN ATTENDEE:  Right.

      MR. GARBARINI:   It had  seemed  a lot more

uncertain to  us going  back  a. few months  ago whether

there would be  the  ability  to use  the POTW.   But  if  we

could get something in writing.           K

      AN ATTENDEE:   John will get  something  to  you in

writing.

      MR.  GARBARINI:   And  I guess  actually in going

 through our cost analysis  we had used the higher end

 range of treatment costs for going through the POTW.
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But apparently John is indicating that's probably a  •

high end range cost, and maybe he will give us some

additional cost- information.  That may make that

alternative the less costly or significantly less

costly than the one we're currently proposing.

      AN ATTENDEE:  Okay, thank you.

      MR. GARBARINI:  I guess, I guess one thing I just

can't emphasize too much here regarding the groundwater

remedy is the  fact that when we deal with pump and

treat systems,  we really are dealing with some great

unknowns as to how long .it might take to clean up an  .  .

aquifer and how effective actual pumping and  treating

might be.  We  get into a lot of these cases where we

have dense, nonaquous phase liquids on-site,  and as

Carlos has mentioned we  found out  that  it could take,

you know, centuries to clean them  up.   So that's a

very, very  important consideration.  We do  have the

benzene  plume...here, which  looks  like  it might.be

manageable.   And  we're  really gonna start to  target  our

efforts  at  cleaning that benzene plume  up.   But  again,

during  the  design phase  we'll be doing  greater

 investigation of  the subsurface.

       AN ATTENDEE:   Good question.

       MR.  GARBARINI:   And that  could definitely impact

 the type of remedy we ultimately implement here.
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      We had stated that we would try to achieve the

ARARs, which are basically drinking water standards for

the groundwater.  But it may not actually be possible

to achieve those levels.  So that's an important

consideration in selecting a remedy as well as how .long

we actually operate the system that is designed to

achieve those levels.

      AN ATTENDEE:  I should point out that if it were

feasible to use the wastewater treatment plant, we —

we aren't proposing that we lock you into a long-term

.contract, -because .at some time you -- at some point  ...

decide that you didn't need to do it anymore or

whatever.  So there'd be that flexibility built into

the agreement, which — which could be lived — lived  ,

by by both parties.  I'm sure we could work that  out.

      MR. GARBARINI:  Okay.

      AN ATTENDEE:  We  aren't particularly interested

in — I mean  this .isn't baseball, but this is, you

know.

      MR. GARBARINI:  Right.  Right.

      AN  ATTENDEE:   Go  on  strike?

      MR. GARBARINI:  As  I had  mentioned to  you

 earlier,  sometimes we're  a little  bit reluctant  to go

 ahead and select a remedy that  involves sending the

 discharge off to a POTW —
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      AN ATTENDEE:  Right.

      MR. GARBARINI:  — when we really don't have a

firm commitment on behalf of the town.  Certainly as

you understand with potential change in administrations

and all that, we have to take that all into

cons-ideration.  So the stronger opinion we get from you

on that end of things the better the likelihood that we

would, you know, select that alternative.

      AN ATTENDEE:  Well, it's in our best interest as

taxpayers to keep the costs down as much as possible,

and if we can —  and we,have.the capacity at our

treatment plant and it's doable from your standpoint,

why not   So.

      MR. GARBARINI:  I appreciate that.

      AN ATTENDEE:  James Carr.  I assume that area

down  there will be  locked as  far as  further usage for

quite a  period  of time  for  anything  else?

       MR. GARBARINI:  The'site?                 .  .

       AN ATTENDEE:  That  GCL will be a 30-year plan?

       MR. GARBARINI:  No, not necessarily.

       AN ATTENDEE:   Okay.

       MR.  GARBARINI:  Basically the key thing that we

 are concerned about is  getting the  soils and the

 leftover creosote scraps of wood out of there,

 basically,  and treat it.   And then obviously if —
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depending upon what our ultimate groundwater remedy

looks like, we're gonna need some space for piping and

for the treatment facility itself.  So, but aside from

that small amount of area, the rest of the property

would be useable.  After the soil work is all

completed.

      AN ATTENDEE:  I should point out that that area

is zoned industrial, and there's -- I can't see

anybody's intention of ever zoning it otherwise.  I

mean it's -- it's all contiguous with other industrial

facilities,, so it -- there'd_be no point, the point

being that nobody is going to sell it for a housing

development.

      AN ATTENDEE:  Which wouldn't be recommended by

you people anyway.

      MR. GARBARINI:  Exactly.  And I guess we'd be

very interested  in working with you and  trying  to get

the property back to some sort of use as soon as

possible  also.

      AN  ATTENDEE:  Let us know who owns it.

      AN  ATTENDEE:  Do  you have any — do you have  any

 target, target dates  or time frame, or,  am I putting

 you on  the spot?

      MR.  GARBARINI:   Well,  you're putting us  on the

 spot,  but that's fine.   Basically, as Carlos  mentioned,
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we're about to go through the remedial des.ign process

no>w for the soil treatment system.  So generally, you

know/ that takes us anywhere about — I'd say about  18

months or so to complete that process.  And then I

think we were projecting about another year to trea£

the contaminated soils after that.  So I think we're

probably looking at about two and a half years from  now

before the soil work  is all done.  And in the meantime

the design, if we go  ahead and move forward with the

.selection of the groundwater remedy, we would be out

there probably doing  some significant additional

investigatory work to try and figure out exactly how

to implement the remedy.  And I'd  — I'd say the design

of 'that  system would  probably be more in the order of .-

maybe two and a half  years,  two,  two and a half  years.

      AN ATTENDEE:  Thank you.

      MS.  ECHOLS:   Any more  guestions?

      AN ATTENDEE: --Brent Hollenbeck  for the Daily

 Star.   I talked with  Carlos  last  week.   I'm still  a.

 little  unclear as  to  the total,  total  cost  of  the

 Phase 1 and Phase 2.   I know the  EPA talked about a 15

 million cost at one point,  and I  wasn't sure if that

 was just for Phase 1 or if  that included Phase 1 and

 Phase 2, the entire cleanup at the site.   Do you have

 an overall total cost estimate for the work there?
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      MR. RAMOS:  Yes, but you called it Phase 1, this

is remedy/ we selected last summer for the soils, and

that's roughly close to five — you know, 14 point

something, I guess, or roughly about $15 million.

That's only for the soils.  What we're saying today,,is

the cost for this additional work that needs to be done

at the site, and that's — that's the cost for the

groundwater and the sediments, and the groundwater I

guess the cost is roughly about ten million over a

30-year period, and for the sediments about $300,000.

So you add all .that up, I guess we have  15 plus  10,

plus 25, plus 300, so it's about 25.3, roughly.

      AN ATTENDEE:  25.3 million for the both phases?  .

      MR. RAMOS:  Yeah, all the phases.

      MR. GARBARINI:  That is an estimated cost  too.

One thing that we've  learned  since the last public.

meeting,  actually when we came — arrived at those

costs of.  the  $15 million, is  that there  is the

possibility that approximately one-third of the

material  may  be able  to go over to the New York  State

Electric  and  Gas authority for treatment.  We're going

to be exploring that  option with  them based upon some

input we got  from  the community  and  --  and NYSEG also.

So that could result  in  some  significant savings on

that front.   And  again,  this  —  this estimate for the
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groundwater, we're looking at $2 million in capital

costs, and then the projected cost for 30 years of

treatment bring it up to the $10 million total.  So

there's — depending upon what our future

investigations reveal, that number could be very   0  -

different.

      MS. ECHOLS:  Any more questions?  Okay.

      MR. GARBARINI:  People want a few more minutes

to think about things before we close the meeting?

See  if you  have any other questions?

      AN ATTENDEE.;-  Does anybody check your risk

ctnalysis figures?

      MR. RAMOS:  We  do have our contractor working out

the  numbers and we have our  in-house  risk assessor that

verify  the  numbers.   So they are checked twice,  by our

contractors, by ourselves.   Plus we brought  it up for

public  comment also.

      AN ATTENDEE: -~  So  if  — if someone  had  made a —

mistake,  say, and —  and  I  guess  the  one risk area was

 the groundwater,  if  someone actually  ingested the

 groundwater?

       MR.  RAMOS:   Yeah.

       AN ATTENDEE:  That's the one that is requiring

 this to be cleaned up?

       MR. RAMOS:   Yes.
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                                               30  .


      AN ATTENDEE:  And there's only —..

      MR. RAMOS:  In addition to that risk, the

contaminations in the groundwater is above the drinking

water standards.  So just by being above the drinking

water standard, which is a health based number, an 0

action may need to be taken.  This just quantifies a

number of what would be the risk.  But yes, we have a

very lengthy internal review and extensive review

process, comes from the contractor to us, we review

them, we send them also to New York State and they

review them.

      AN ATTENDEE:  So that was two -- there was a risk

of 2 in  1,000 or  2 in 10,000 was it, that —

      MR. RAMOS:  For —

      AN ATTENDEE:  For drinking the groundwater?

      MR. RAMOS:  If the groundwater will be roughly  at

two  — two  in  a thousand for adults living  in  the

vicinity of the site.                                 	

      MR. GARBARINI:  Lots  of  time  at  sites groundwater

remedies will  just be driven by the fact that  levels

are  above drinking water standards.

       AN ATTENDEE:   How much,  can you  reach that —

 just from background information for future thought,  to

 reach that  2 in 1,000,  how much water did the

 individual  have to  drink over how much — what period
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of time?                    .
      MR. RAMOS:  I don't recall the exact number.  But
it's — it considers the amount of water that the
person drinks, it includes the body weight/ children
have a different body weight than adults; it includes
the typical contaminated areas, it includes the amount
of time, I mean the — the — for example, children who
were drinking water for a year, that can happen.  So
there are different -- all these factors are — are put
together into a formal list, then you come up with a
calculation on that. . .The specific numbers, liters
of — of water per day, I don't recall.  We can check
it out when the meeting's finished, I have the report
there.  And we can — do you remember that by any
chance, off the top of your head?   I'm  sorry, do  you
remember  from the top of your  head?
      AN ATTENDEE:  No.  It's  a reasonable amount.  All
the  —  there  is three factors  there too,  there's  --
there's  not only  ingestion but there's  inhalation,  if
you  have  volatiles  and you —  typical case is  in  a
 shower,  where it  volatilizes  and  it also contacts
 with the skin.   Through  washing of hands and other
 things.   All  the parameters that  went  into the models
 are in the remedial investigation report.
       MR.  RAMOS:   Yeah.
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      AN ATTENDEE:  And they're all based, as Carlos
said, upon body weight, upon number of days in the
area, especially when you deal with older children who
may be gone.  And all those are based upon EPA
acceptance standards and practices which we employ ^
quantitative amount.
      AN ATTENDEE:  But it's just like not casual
contact if you —
      AN ATTENDEE:  They're based on prolonged
exposure.
      MR. GARBARlNI:-  And lots' of cases,  I'm not saying
for  this site that was done, but in a lot of cases
standards of acceptances are something like 2 liters
a day over  the course of 30 years, assuming a lifetime.-
of 70 years, something like that.
      AN ATTENDEE:  And then there is an  increased
possibility of the  2  in  17000  that they could develop
some .-.-
      MR. RAMOS:  That's — that's a potential  risk,
doesn't mean that you're gonna get any  cancer,  that's
 just a potential risk.   And that's  just a way  for us  to
assess the  potential  problems  that maybe  that will be
 caused by the site.   So it's  not that it's gonna
 happen,  but there's a potential  that it can happen.
       MR.  GARBARlNI:   Especially, as you know,  we've
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 all  discussed before,  no one is  currently .drinking the

 groundwater at the site, and it  is  zoned industrial.

 So.

       MS.  ECHOLS:   Okay.  Any more  questions?

       AN ATTENDEE:  Thank you for the presentation and

 the  opportunity to ask questions.  Appreciate your

 coining.

       MR. RAMOS:  As Cecilia mentioned,  the.comment

 period ends on March 30th.  So if you have any comments

 you want to put in, you know, on paper,  please feel

.. free to do-that.-  .And send it. to us, we'll be. happy to. .

 include that in our responsiveness  summary section of

 the record of decision.  Or, you know, just a comment,

 if you want to call us  up and just let us know about

 it, that's fine.

       AN ATTENDEE:  Who reads that?

       MR. RAMOS:  Who reads what?

       AN ATTENDEE..::_ .Reads the public comment.

       MR. GARBARINI:  Basically the way  the  process.

 works is the  public comments will  come  in to .Carlos  and

 Cecilia, either written or  verbal  here  tonight,  then

 there will  be —  the  responsiveness  summary will be

 prepared.   It usually goes  — that's part of a  larger

 document called the record  of decision.  And a  record

 of  decision is the document that provides a conceptual
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plan for the remedy, it actually selects the remedy

that's gonna be implemented, and that's signed by the
         *
highest ranking official in the Region II office, the

regional administrator.  And so the entire document

generally goes through the loop all the way up the ,

chain of command, so a lot of people read it.

      AN ATTENDEE:  Well, what just appears to me is .

that you've already got -- you've got those nine

criteria, you've already made your decision, we've got

public comment tonight, it's kind of after the fact.

      MR. GARBARINI: ..No.  No.  That's not the case.

The idea, that's why we're using the term the

preferred alternative.  We're saying that that's what's

preferred at this point in time.  We've basically taken

our -- we've — we've  figured out what the nature and

extent of contamination is, we have determined what  the

risks are, we have  determined that there are  some

unacceptable risks. ;and some- levels of  contamination  in

the groundwater  that  look  like they heed remediation,

we've  looked at  different  alternatives  for  cleaning  up

the site to acceptable levels, and now what we're doing

is saying based  upon  our evaluation of those

alternatives we  are preferring the one alternative  for

the groundwater, alternative  two,  and alternative  three

 for the — alternative two for the soils  — sed —  I'm
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sorry, surface water sediments also.   But that's why

we're soliciting comments/ because we could ultimately

change that when we sign the record of decision.  And

that would also be documented, any significant changes

would be documented in the record of decision.

      MR. RAMOS:  I just -- I mean we take comments

very seriously.  Last year we did modify the remedy

between -- the remedy for the soils to incorporate the

comments that we received here.  So, you know, we do

indeed take very seriously your comments.  And  in many

cases we will modify or change remedies based on that.

      MS. ECHOLS:  Sir?

      AN ATTENDEE:  Glen Umbra, from Unadilla.  Do

you —  it says here in the risk assessment,  it  just

says  potential excess cancer  risk  for GCL  related only.

There seems  to be  a lot more,  you  know,  chemicals,

metals  in there  other than what is just  from the

polyaromatic from  the..plant.itself.  Are you gonna  —

are you doing anything with these  other, you know,  the

 other high  metal con'  —  you  know, concentrations  that

 are in there?  Is  there  any risk  from them being there?

       MR.  RAMOS:  You  talking about the  metals  —

 excuse me,  let me just put that  table up.   Okay.   Here

 we are.  Yes.  Your comment specifically about the

 non-GCL risk?
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      AN ATTENDEE:  Right, well, you've.only '— you've

only covered — there's only so many things from the

GCL plant that's on the — in the ground there.

      MR. RAMOS:  Yeah.

      AN ATTENDEE:  There seems to be a heck of a lot

more with your volatile organics and your metals that

are in there.

      MR. RAMOS:  That's true.

      AN ATTENDEE:  Are you taking that into

consideration with these risks?

      MR.. RAMOS:  Yes, it is.  When.we have the risk..

that we  calculated for total, which is this — this

column here, we have total risk, it includes

everything;  includes metal, volatile organic compounds,

all the  contamination  that we found there, which is  —

which isn't  the less contaminant of concern.   Let me

just backtrack  a  bit here.  You can see this is more

from.this figure.  These  are the contaminants  of

concern.  You can see  quite a  few  of the  contaminants

have to  be more clear  asterisks next to it.  And

there's  a note  at the  end to  say not a contaminant  of

concern  when Route  8  landfill  wells  are excluded.   And

what that means is  that those were contaminants which

were  included  in the  risk assessment for  total risk.

 But we  know that they are not site related.   So that/
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to answer your question, we have, yes, you're right,

there are many other contaminants which are not GCL

site contaminants.  But they were indeed included when.

we calculated the total risk.

      AN ATTENDEE:  You already have the Route -- the

Route 8 site's already there, you're gonna be setting

up another site, another whatever you want to call it,
                      »
on that site, the GCL site, to —

      MR. RAMOS:  You're talking about groundwater

restoration system.

   ..  AN ATTENDEE:  Right.          .     :.

      MR. RAMOS:  Exactly.

      AN ATTENDEE:  So you're gonna be more  or  less,

are  you gonna be working hand in hand with the  other

one  to be remediating that site?  Of  everything?

      MR. RAMOS:  From  the very  beginning, for  example,

we went to  Una-Lam  and  asked them for the information

that they have.,in the groundwater.  They have a very

€jxtensive network of  -- of monitoring wells.  So from

the  beginning we  went there to  say, you  know, you have

wells in the area,  can we  have  your data.  So they

 supply us with data.   After we  examine that data we

 say, you know,  we want samples  on your wells as part of

 your investigation.  So we use  — we  used their wells

 and took samples  for us.  And we used that to determine
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what was site related, and what wasn't site related.
And also determine the full extent of contamination
from the GCL site.
      After that the Route 8 landfill was in the
process of putting together groundwater extraction and
treatment system, they have remediation system on
their — under the — under the New York State
Department of Environmental Conservation oversight/
which is actually addressing groundwater contamination,
they're already there pumping their own water and
treating the groundwater.  And we certainly -- we
will continue to make efforts in the future to make
sure that one system doesn't interfere with the
other system, second, make sure that whatever they —  :
you know, we do,  just addresses our plume, if they're
doing something  to help  us then we don't have to redo
it.
      Certainly  as more  information  is developed from
their system and more information is developed  from: our
system, we  will  make  sure that  -- that both  systems
are  —  are  operating  in  the  fashion  that they
compliment  each  other and they  don't actually  interfere
one  with the other.   So  there will be a  lot  more
coordination in the  future as we  move from the design
.into the actual  remedial action phase.
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      AN ATTENDEE:   Okay.   What about the — you said

over land flow, you're gonna be -- that was one option

of pumping it out and then just over land flow to

the — after you treat it?

      MR. RAMOS:  Discharging into the drainage ditch.

      AN ATTENDEE:   The drainage,  where does that flow?

      MR. RAMOS:  That flows eventually through the

Una-Lam and further down the line to the Susquehanna

River.  And that's the same point where — actually

where that landfill is — is discharging their treated

water.

      AN ATTENDEE:  Okay.  My — my  —  I guess what  I

was asking is  there •—

      MR. RAMOS:  I'm sorry.

      AN ATTENDEE:  Is there a potential risk  for the

farther  on,  like the  back River Road and on the back

side  of  the  airport farther  on down  Gifford Road?

      MR. RAMOS:  No, we  didn't find any contamination

outside,  as  a matter  of  fact we have a well which  is

 close to the railroad tracks,  let me just  pull the

 other figures with  the nice  colors on.

      MR.  GARBARINI:  Are you  concerned about the

 existing contamination or contamination that might be

 caused by our discharge?

       AN ATTENDEE:   Both.  Both from, you know,
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going — it would be heading — well, this is north so

it would be heading toward west, toward the back River

Road and back of the airport.  Where.there's a farm

back that way.

      MR. RAMOS:  From groundwater or from discharged

water?

      AN ATTENDEE:  Discharge water.

      MR. RAMOS:  Okay, the water which is gonna be

discharged somewhere around this drainage ditch here.

And we'll meet all — all the cleanup standards, that's

the Federal Government and. the state required to make

sure that doesn't have any impact in the — in the eco

system or in the drinking wa' — in  the surface water

or supposed to be made for the underlined.

      MR. GARBARINI:  You could probably — you could

drink the water that we're gonna be  discharging in

there.

    '  MR. RAMOS:  Basically  many times  it's  -  it's more

cleaner  than  drinking water.

      MR. GARBARINI:  Yeah.

      MR. RAMOS:  You know,  sometimes  —  sometimes  some

of  these cleanup  numbers  are more  stringent than

drinking water standards.   So.   It is  extremely good

quality water.   So,  and that's —  I mean that's for the

discharge.
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      As of contamination of the property, so far we

haven't found any GCL related contamination of the

groundwater outside the property/ there is some

contamination in the area, in the groundwater, but it's.

not site related.  It's probably that renewed program

with the VOCs for the Route 8 landfill, and that's, as

I mentioned before, being addressed, they're now

operating groundwater pump on two different systems so

hopefully that will resolve significantly that problem.

      That's  —  I mean creosote, you know, has a  good

side- and a bad side.  You know./  the -- the bad ;Side is

.that once  it  gets into the groundwater it's very  hard

to  clean.  But the good  side  is  that it doesn't move

freely  much.  So once  it gets there and reaches  a

certain level it really  doesn't  move much more.

Doesn't move  more, much, it will stay  pretty much put.

And that's why  after all these  years at the  site you

 only have, you  know, some ..very  limited areas of

 groundwater  contamination.

       MR.  GARBARINI:   They really —  our  primary

 concern too  is  making  sure that the contaminants don't

 migrate off  site.   So  the key thing is to make sure

 everything is contained.  I mean we could — we could

 ultimately just end up in designing some sort of remedy

 where we made sure if the contaminants aren't already
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 1         contained,  just made sure that they don't migrate off

 2         site.   And  then perhaps when we look at the pumping and

 3         treating we may find out that hey,  we're really not

 4         doing the groundwater any good by continuing to pump

 5         and treat.   So let's just hold our horses and make sure

 6         that we contain the contamination.   Because :—

 7               AN ATTENDEE:  The groundwater flow actually does

 8         flow that — toward the west, right?

 9               MR. RAMOS:  It flows towards the Susquehanna

10         River.

11               AN ATTENDEE: .To the .northwest, right? .

12          .     MR. RAMOS:  No, actually it runs toward — funny

13         thing is that groundwater movement there is a bit

14         complex in terms of shallow aquifer is a little bit

15         different than the deep aquifer in a different

16         direction.   But generally it moves toward the

17         Susquehanna River.  This is north here, the Susquehanna

18         is near ..north, kind .of northeast kind  of fashion.  So

19         this  is most  of the general  flow of the groundwater.

20         there.   In different areas  it moves a  bit different,

21         but it moves  always toward  the Susquehanna.

22               AN ATTENDEE:  Where does your ditch  go  you're

23         talking  about?

24               MR.  RAMOS:   It will be on-site,  it will —

"25               AN ATTENDEE:   On-site,  where does it— it's got


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to go somewhere, is it just gonna be a lagoon?

      MR. RAMOS:  Exactly, it would be on the edge —

you mean the collection?

      AN ATTENDEE:  Where is it gonna go eventually,

the ditch?

      MR. RAMOS:  Oh, the ditch where we're gonna be

discharging the water?  Yeah, that's the --  .

      AN ATTENDEE:  It isn't gonna go north towards the

Susquehanna.

      MR. RAMOS:  Eventually, eventually goes to the

.Susquehanna. -                                   • . ^

      AN ATTENDEE:  Yeah, it will, but  it  has to go

west, as he  says, before  it ever  gets there.  East,  I'm

sorry,  I'm sorry.

      MR. RAMOS:  Yeah,  this  is additional here, the

 discharge to this point,  let's  say discharge  here  the

 water would  direction this way.

      AN. ATTENDEE:   It's, gonna  go that  .way..

      MR.  RAMOS:   That way,  until eventually --

       AN ATTENDEE:   That's  toward the town wells.

       AN ATTENDEE:   On the other side of Route 8.

       AN ATTENDEE:   Okay, okay, now I see.

       AN ATTENDEE:   It goes both ways,  doesn't it?

 Right about — right about where your pen is it starts

 going the other way, doesn't it?
                        Empire Court Reporters
                       One Marine Midland Plaza
                        Binghamton, NY  13901

-------
                                                          44
 1

 2

 3

 4

 5

 6

 7

 8

 9

10

-ll-

12

13

14

15

16

17

18


19

20

21

22

23

24

"25
      MR. RAMOS:  You are down here, this is a wetland

here, if you are within the wetland area, it goes that

way.

      AN ATTENDEE:  Right.

      MR. RAMOS:  It goes toward the west.

      AN ATTENDEE:  How far?

    .  AN ATTENDEE:  It's heading west, and the

groundwater flows toward the back River Road toward the

barn, toward that farm.

     . AN ATTENDEE:  No.

      MR. 'RAMOS:" That water moves  towards the

Susquehanna that way.

      AN ATTENDEE:  Surface water does.

      MR. RAMOS:  Surface water.  There's a point

here, there's  like  a barrier here,  from  —  from some

point here down the groundwater moves  —  moves  east.

At  some point  here  it  moves west.

      AN ATTENDEE:  Surface.water.  .

      MR. RAMOS:   Surface water we're talking about,

yeah.   Surface water.   So if  it went to  the chart,  it

would  chart  someplace  here, which would  eventually go

 towards this,  from the drainage  ditch to that Una-Lam,

 and eventually it would reach into the Susquehanna

 River.

       But as I mentioned before,  the water that will be
                        Empire Court Reporters
                       One Marine Midland Plaza
                        Binghamton, NY  13901

-------
                                                          45
 1

 2

 3

 4

 5

 6

 7

 8

 9

10

11

12

13

14

15

16

17

18

19

20

21

 22

 23

 24

"25
discharging there is'-- is many cases cleaner than

drinking water.  So we -- you know, we are not

discharging -- if we were to pump and treat, you know,

we would not be discharging any water that have

contamination that would affect either the biol -- the

biology of the stream or people down the line.

      MS. ECHOLS:  Any more questions?

      Okay, I guess we're gonna wrap it up.  And as

Carlos said, the public comment period ends  on

March 30th, if you have any comments you can write  into

our ..office, our  address is .in  the  proposed  plan.  And _

thanks so much for coming out.

      MR. GARBARINI:   Thank you very much.

      MR. RAMOS:  Thanks a  lot.

       (Proceedings were adjourned  at 8:06  p.m.)
                        Empire Court Reporters
                       One Marine Midland Plaza
                        Binghamton,  NY  13901

-------
 6

 7

 8

 9

10

11.

12

13

14

15

16

17

18-

19

20

21

22

23

24

"25
                         CERTIFICATE
                                                          46
1

2 .

3    IN THE MATTER OF:        Public Meeting
                              GCL Tie & Treating Superfund Site
4
     ON:            •          Wednesday, March 8, 1995
5
      BEFORE:                  RUTH I. LYNCH
                              Registered Professional Reporter
          This is to certify that the foregoing is a true  and

     correct transcript, to the best of my ability, of the

     stenographic minutes  of a public hearing held in the

     above-mentioned matter, on the above-mentioned date,  and

     of the whole thereof, taken by Ruth  I. Lynch, Registered

     Professional Reporter.
                             EMPIRE  COURT  REPORTERS

                      Signed this ^O_^day of  /^L
-------
                    APPENDIX E
LETTERS SUBMITTED DURING THE PUBLIC COMMENT PERIOD

-------
                                            FAXED  & MAILED
              VILLAGE-OF SIDNEY
                                           Sidney Civic Center, 21 Liberty Street
                                                   Sidney, New York 13838
                                                     Phone (607) 561-2324
                                                       Fax (607) 561-2310

                                     March 21,  1995
Mr. Carlos R. Ramos
Remedial Project Manager
US Environmental Protection Agency                            .   .
290 Broadway, 20th Floor
New York, NY  10007-1866

Re:  GCL Tie & Treating Site Operable Unit 2
     Village of Sidney, Delaware County, New York

Dear Mr. Ramos:'                                      	   	

The  following  comments  are  provided  in  review  of  the  above
.referenced project:

1.  Ground   water   contaminant   boundaries   in   the   shallow
    intermediate   and   deep  zones  have   apparently   not  been
    established  and confirmed  as  evidenced by  contamination in
    perimeter wells.  At  the preliminary meeting on March 8, 199.5
    it was noted by EPA representatives that contamination due to
    GCL   site   activities   have  .been  established   and  that
    contamination  especially  in  the  wells  along the  northern
    perimeter  is attributed to  the  Rt. 8  landfill project.   As
    there    are    residential    ground   water   users   located
    nort'hwes'terly  of the  site the  potential impact to thes-e • users
    due  to  off site migration  whether., GCL or  non GCL  related
    should be considered.

2.  With  respect  to  alternatives evaluation  consider  including
    monitoring  of  existing  down stream wells in all alternatives
    including "no  build"  for reasons mentioned above.

3.  After  soils  are remediated through operable unit 1 and 2 and
    the  ground water recovery system is in  place,  can the  land be
    utilized?                                                  ....

4.  Ref.  page  12   of   Summary:    The   goal  of  alternative GW-3
    referred in  the last  paragraph of  the alternative description
    is  not  stated.    I  would  suggest inserting  "the  goal of
    alternate GW-3  is  	"  prior to last paragraph  (complete
    the  statement  as appropriate).

-------
                                              Mr.  Carlos  R.  Ramos
                                                       U.S.E.P.A.
  	                                             March  21,  1995
                                                           Page 2


5.  Although the  closest connection  point to  the public  sewer
    system on  the south  side of  Delaware  Avenue, probably  the
    most expedient connection point would be  to the  public sewer
    on Unalam property running in  a north-south direction  in  the
    vicinity of the Unalam water well which sewer continues along
    the southerly side of the railroad near MW-04 shown on  figure
    1-12 (see attached sewer drawing).
                                                                 i
6.  Can EPA  furnish  the  anticipated makeup (even worst  case)  of
    the    discharge    following    separation   and   manganese
    pretreatment,  i.e.,  what would be  discharged to  the  public
    sewer under alternate GW-3?

7.  EPA  has   identified  two  basic   technologically  feasible
    remediation  alternative  with treatment  "onsite   (GW-2)  and
    treatment  offsite  at  the  Village  POTW  (GW-3).    Carbon
    adsorption and  biological treatment would  be  options  within
    the .GW-2 alternative.   .    .

    $5/1000 gal',  was used as the treatment cost at the POTW which
    implies $92,000/yr. O&M cost.

    The current rate  for sewage  treatment  is  S2.26/1000  gal.   At
    30 gpm this rate would imply $35,635/yr. O&M cost.

    The Present Worth (P.W.) of $92,000/yr.,
                                        30 yrs., 7% = $1,141,628
               The P.W. of $35,635/yr., 30 yrs., 7% =    442,194
                                    P.W. difference =   $699,434

    Therefore, the potential P.W. of alternate GW-3 = $8,818,766

    Both-alternatives,  GW-2 "and GW-3,  are expected  to require
   ' phase  separation  and pretreatment.	The GW-2 alternative may
    require  bench or  pilot  studies  for:    bioreaction sizing,
    nutrient addition,  media replacement;  provision  for removal
    of  excess  biomass,  recycling  of  biomass,  and/or  excess
    biomass  disposal;  contaminant  degradation levels evaluation
    with  further  bench  or  pilot studies to  determine if  carbon
    adsorption would be  needed  to polish  the  effluent  prior to
    surface  discharge.   In  other words, the selection of GW-2 is
    not without possibly significant  further  investigation.

    With  respect to  alternative GW-3  (treatment  at  the Village
    POTW):   30 gpm is small  in comparison with  the normal 416 gpm
    average  plant flow  and  is not expected to interfere  with the
   . treatment  process.   Discharges from the  POTW as in  the case
    of GW-2  are liquid  (effluent), solid  (sludge)  and  air.  Plant
    effluent is  discharged  to the  Susquehanna River via a SPDES
    permit regulated by NYSDEC.   Dewatered sludge is  disposed of
    at the Delaware County  landfill regulated  by  Delaware  County
    and NYSDEC.   Air  discharges  are not regulated.

-------
                                             Mr. Carlos R.  Ramos.
                                                       U.S.E.P.A.
  -------                                             March 21,  1995
                                                           Page  3


    If EPA  requires  a  long  term commitment  on behalf  of  the
    Village  to accept the  effluent, the Village prudently  should:

    1)  Get  a formal opinion on the likely impact on our effluent
       and  sludge discharges based on a  profile of  the expected
       influent.
    2)  Obtain concurrence  of  NYSDEC with  respect  to the  SPDES
       discharge permit.
    3)  Obtain concurrence  of  Delaware  County  and NYSDEC  with
       respect  to  the  sludge  discharge  to  Delaware   County
        landfill.                             .

    I expect  that  Delaware  County would  require that  our sludge
    not exceed land  application criteria  and I have no reason to
    believe  that  it would  exceed this criteria as a result of
    accepting this discharge.

The- revenue  te--the Village of- Sidney -would benefit  the sewer fund.
budget.  One  of the  reasons and probably  the  primary reason that
the Village  has  not  implemented water metering for residential
customers is  due to  the loss  of revenue  that would  take  place in
the switch  from  flat rate to metered  rate.  The revenue  accrued
from accepting this  flow  could help  make complete  water metering
feasible  thereby providing a secondary benefit to the Village and
help meet the "NYSDEC objective  of metering.

We  request   that   EPA  consider making   alternative  GVJ-3  the
preferred alternative.

It  is  understood  that  with preliminary  conceptual  approval the
Village would pursue the  three items  outlined above in a timely
fashion ..... and--- would  complete  same   on a mutually  .agreed  upon
schedule.                                            .   .

We  would  appreciate your  consideration and response,  and if you
have any questions ,  please  contact me.

                                     Sincerely,
                                     VILLAGE OF  SIDNEY
                                          J. Woodyshek, P.E.
                                     Village Engineer
JJW:hj

Attachment

cc:   Mayor  Davis
      Trustees
      Frank  Holley

-------

-------
                                           March 17, 1995
 Mr. Timothy Fields, Jr.
 Deputy Assistant Administrator
 Office of Solid Waste and Emergency Response
 U.S. Environmental Protection Agency
 401 M Street, S.W.
 Washington, D.C. 20460

 Dear Mr. Fields:
-	It was indeed a pleasure meeting you at-Temple-University's workshop on	
 "Impact of Environmental Remediation Requirements on Inner City Revitalization" and
 listening to your update on the Superfund program and the Brownfield Redevelopment.:
 Program.  As we had discussed, I've attached information for your review on what
 NYSEG is doing for remediation of former Manufactured Gas Plant (MGP) sites.

       NYSEG has obtained permits from NYSDEC to burn coal tar soil (CIS) from
 MGP sites  in  our utility boilers. In the last six months, NYSEG has provided an
 environmentally safe and economic remediation technology for clean-up of four MGP
 sites in the northeast.

       Maybe just a drop in the bucket when considering the estimated  1,500 to 2,500
-•sites-that-may exist nationwide^ but it was only.six months,, and doesn't.include..th.e   _..:	
 other utilities  across the  country with similar capability.                           .•••.:-•

       The biggest asset to this movement has been the EPA's approval of  EEl's MGP
 site remediation strategy.  Rather  than having to manage the MGP contaminated soils
 as a characteristic hazardous waste, the strategy allows for blending the other less
 contaminated material on site to render the entire volume non-hazardous. As a result,
 the utility can transport and burn the material as a solid waste.  In addition,  the cost
 associated with remediation is significantly reduced. As the  cost of remediation goes
 down, this  is  an incentive to clean up more sites.                 	

       If the strategy developed by EEI for MGP sites could  be utilized  on other
 contaminated sites, similar remediation activity would begin to take place.  Many sites
 have contaminated material of high BTU value, making them ideal for combustion in


  An Equal Opportunity Employer


  New York Slate Electric & Gas Corporation Corporate Drive-K/rtwooo industrial Park. P.O. Box 5224. Binghamton. New York »3902-5224 #07; 729-2551

-------
Mr. Timothy.Fields, Jr.       "     "  Page 2                     March-14;-1995-


utility boilers as an alternative fuel.  So, rather than these sites continuing to cause
harm to the environment until Superfund or the PRP's have the money to dean them
up, lets begin to extract the beneficial use from these sites.

      I will be developing a cost estimate for remediation of the GCL tie and treating
creosote contaminated Superfund site located in Sidney, NY which will demonstrate
how the EEI strategy document, when applied to this site, results in significant
remediation cost savings, while at the same time meeting the required site clean-up  *
standards.  It is anticipated that the estimate-will be completed by the end of April.
Once completed, I will provide copies to you, Carlos Ramos, Remedial Project
Manager (Sidney site), and Doug Garbami, Chief NY Region Superfund Section I.

      I believe that this strategy wiN support the objectives of the Brownfield
Redevelopment Program, as well as the new direction of the Superfund Program.

      I look forward to your suggestions and comments on this idea.

                                          Sincerely,
                                          Keith C. Day

Attachments

cc:   C.'Ranios - EPA  '1
      D. Garbarni - EPA
      A. Butkas - DEC
      W.  R. Weisman - Piper & Marbury


KCD:tfas:fle«s.wp

-------
               APPENDIX VI




STATISTICAL SUMMARY OF ANALYTICAL RESULTS

-------
                                                                                        Table   1

                                                                         SUMMARY STATISTICS l?OU SOILS '• yOLATII.K OHCANICS
                                                                                      OCL Tic and Trailing!Site  .          '           .
i
Compound
ClilotoineUune
OromoinelluiK'
Vin)1 chloride

0
0.
3
0
0
1
0
1
0
13
0
5
3
5
Undelec
31
31
31
31
29
3D
28
31
30
30
31
31
30
30
31
31
31
31
30
31
31
28
31
31
30
31
30
31
IB
31
26
28
26
Eillmite
' 0
0
0
0
1
1
3
0
1.
1
a
0
i
i
0
0
0
0
0
0
0
2
0
0
1
0
1
0
9
a
4
2
2
RtjK
0
0
(I
0
0
0
0
a
0
0
a
o-
o-
o:
0
o-
.0
o-
o-
0
o-
a
0
0
a
0
0
0
0
0
0
0
0
Frequenc;
Detected
. 0.00
O.UO
0.00
0.00
0.06
0.0)
0.10
0.00
0.03
. 0.03
0.00
O.UO
0.03
0.03
0.00
0.00
• o.oo
o.uo
• 0.03
0.00
• o.oo
• o.io
1 0.00
• o.oo
0.03
• o.uo
0.03
0.00
0.42
o.oo
0.16
' 0.10
0.16
Minimum
Concentration
Detected
o'.oo
0.00
0.00
0.00
11.00
130.00
1.00
D.UO
2.00
; 2.00
• 0.00
0.00
9.00
4.00
0.00
0.00
0.00
0.00
12.00
0.00
0.00
5.00
0.00
0.00
6.00
O.UO
2.00
0.00
1.00 .
0.00
2.00
11.00
11.00
nUilmum
Concentration
Sii-iccied
0.00
0.00
0.00
0.00
18.00
130.00
3.00
0.00
1.00
2.00
0.00
0.00
8.00
4.00
0.00
0.00
0.00
0.00
12.00
0.00
o.oo-
. 1100.00.
0.00
'o.oo
6.00
0.00
2.00
0.00
89.00
0.00
100.00
1 20.00
560.00
Mcdlii
6.00
.6.00 ,
6.00
6.00
6.110
6.00
6.00
6.00
6.00
6.00
6.00
6.110
6:00
6.00
6.00
6.00.
6.UO
6:00
6.00 '
6.00
6.00
6.00 '
6.00
6.00
6.00
6.00
6.110 '
6.00
6.00
6.00
6.00*
.6.00
6.00.
Geometric
Mean
6.506)
6.5063
6.5063
6.5063
6.9307
8.0771
5.9255
6.5063
6.2798
6.2798
6.506)
'6.5063
16.3670
: 6.4218
. ''6.506)
, -6.5(163
:. 6.5063
•6.506)
6.6534
6.5063
•6.5063
7.2/141
.6.5063
6.506)
'6.35
7.8250 i
7.8976 J
7.S9J6 «
7.8250 «
7.BJ50 >
7.9070
7.7825 >
7.8250 i
7.8250 i
7.8J50 «
7.8250 «
8.0980
7.8150 i
7.8J50 >
I8J0568
7.8250 «
7.8250 «
7,1276 *
7.8250 >
7.8557 i
7.8250 i
16.9206
7.8250 i
12.6898
II £795
39.6264
CcnccimiiiolMira given In ugfti; (jipb).                                :                 .,         •
|lw "A" In UK lu ilglil column Imliulei'diil I)K 9i1i Upper Confidence l.imil a greglcr Ihen Hie iii>xiniuin ilelecled coliccnlnlinn.
     lUte I ol I
UM1SI/VOI..XI.S

-------
                            Table  1
CIIGMIUAI.SUMMAKY STATISTICS FOR SOILS - SKMI-VOUTIM! ORKANICS
         !         .          (;CI/l'lcandTrcnllii|i.Sllc
Compound
Phenol
bii(2-Cliloroelhyl|ellier
2-Clilorophenol '
1 ^-Dichlorubcnzene
1 .4-Dichlornbcnzene
1 ,2-Dichlorobcnieno
2-Mclhylphenol
2|2>oxyt)ii-l-Chloropropano
4-Melliylplicuol
N-Nitrosodi-n-propylamine
lexachloroclliaiio
Nitrobenzene
sopliarone
2-NJIrophenol
2,4-Diinclhylphenol
biiU-Cliloroethoxy (methane
!,4-Diclllorophenal
,2,4-Trichlorobciizeiie
(aptulialciio
.Chloroaniline
llexachlorobulidiene.
4-Cldoru-3-inclliylphenol
2-Meihyhiiiphilinlcno
leiachlorocyclopenladieno
2,4,6-Trichlorophenol
2,4,5-Triclilorophenol
-Chtoronaphlhaleno
-Nilroaniline
Dimclhylphllialalo
Accitaphdiylene
,6-Dinitrotoluene
•Nilroaniline
Acuiaphlhene-
.4-Dinitroplicnol
-Niirophenol
Dibenzofuran
^-Diiiit/olotueno
ielliylpdlhalale
-Clilorophcnyl plienylellier
uorcne
Nilroanilinc
.6-L>iniUO'2*inelhyipheliol
Vail
29
29
29
29
29
29
29
29
29
29
29
29
29
29
29
29
29
29
138
29
29
29
30
29
29
Z9.
29
29
29
139
29
21
137
29
29
30
29
29
29
139
28
29
Occu
0
0
o-
0.
0
0
0
0
2
0
0
0
0
0
0
0
0
0
471
0
0
0
. 8
0
0
0
0
0
0
24
0
0
33
0
0
8
0
1
0
37
0
0
tlndelee
29
29
29
29
29
29
29
29
27
29
29
29
29
29
29
29
29
29
91
29
29
29
22
29
29
29
29
29
29
113
29
21
102
29
29
22
29
28
29
102
28
29
Estimated
0
0
0
0
0
0
0
0
2
0
0
0
0
0
0
0
0
0
28
• 0
0
0
7
0
0
0
0
0
0
22
0
0
27
0
0
7
0
• 1
0
28
0
0
Rtjtc
2
2
2
2
2
2
2.
2
2.
. 2
2
2
2
2
2
2 .
2
2
20.
2
2
2
1 .
2
2
2
2
2
2
19
2
10
21
2
2
1
2
2
2
19
3
2
I'requene
jlclcclcd
i 0.00
! o.oo
1 0.00
0.00
0.00
. 0.00
. 0.00
0.00
0.07
0.00
0.00
0.00
0.00
0.00
; .0.00
j 0.00
:•. o.oo
. 0.00
.0.3-1
0.00
0.00
.0.00
.0.27
0.00
o.oo
O.IK)
0.00
0.00
0.00
0.17
0.00
o.oo
0.26
0.00
'o.oo
0.27
o.oo
0.03
0.00
0.27
:, lino
i 0.00
Minimum
Concentration
Delected
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
53.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
22.00
o.oo
0.00
0.00
30.011
0.00
0.00
0.00
0.00
0.00
0.00
1 35.00
0.00
0.00
34.00
0.00
0.00
. 691(10
0.00
1 10.00
. 0.00
19.00
0.00
0.00
Maximum
Concentration
Delected
0.00
0.00
o.oo
0.00
0.00
0.00
0.00
0.00
1600.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
92000.00
0.00
0.00 .
0.00
36000.00
0.00
0.00
0.00
0.00
0.00
0.00
11000.00
0.00
0.00
410000.00
0.00
0.00
31000.00
0.00
110.00
o.oo
240000.00
0.00
0.00
Media
193.00
193.00
193.00
193.00
193.00
193.00
193.00
195.00
195.00
195.00
195.00
195.00
195.00
195.00
I9S.OQ
I93.no
W.oo.
195.00
165,00
195.00
195.00.
195.00
I917.5H.
195.00.
193.00
475.00
195.00
475.00
195.00
165.00
195.00
490.00
165.00
475.0|)
475.00
195.00
195.00
95.00
95.00
65.00
480.00
475.00
( eomclrl
.Menu
• 244.6336
244.6336
,2*44.6336
244.6336
244.6336
i-14.6336
2/14.6336
244.6336
222.896.)
244.6336
244.6336
244.6336
2-14.633f.
244.6336
244.6336
244.6336
244.6336
2J4.6336
2-15.4386
244.6336
244.6336
244.6336
2(|>.5522
24[f.6336
244.6336
592.5723
244.6336
540.5496
244.6336
176.8729
244.6336
660.4250
216.6689
592.5723
592.5723
26^4305
244.6336
240.5143
244.6336
210.8038
i 00. 158 7
5921.57J3
Arlllimcll
, Mean
593.9655
593.9655
593.9655
593.9655
593.9655
593.9655
593.9655
59319655
436.8276
593.9655
593.9655
593.9655
593.9655
593.9655
593.9655
593.9655
593.9655
593.9655
2566.5145
593.9655
593.9655
593.9655
1528.7.133
593.9fi55
593.9635
1469.8276
593.9655
1442.9310
593.9655
318.7626
593.9655
1859.7619
4347.5547
H69.8276
1469.8276
2083.1333
593.9655
591.5517
593.9655
3023.7698
1507.5000
1469.8276
Standard
Deviation
1497.4433
1497.4433
1497.4433
1497.4433
1497.4433
M97.4433
I497.J433
1497.4433
1101.9699
1497.4433
1497.4433
1497.4433
1497.4433
1497.4433
1497.4433
1497.4433
1497.4433
1497.4433
13377.9568
1497.4433
1497.4433
1497.4433
6332,2726
M97.4433
H97.44J3
3750.1475
1497.4433
3758.6376
1497.4433
1078.5680
1497.4433
4371.5159
5846.9136
3750.1475
3750.1475
7211.1072
1497.4433
498.1906
497.4433
1223.5957
3813.3711
3750.1475
meant;
5.4998
5.4998
5.499H
5.4998
5..I998
5..I998
5..I998
5.4WS
5.41167
5.4998
5.4998
5.49')S
5.499S
5.499B
5.4998
5.49')8
5.4998
5.4998
5.5030
5.4998
5.4998
5.4998
3.5fi2fl
5.4998
3.4998
6.3845
5.4998
6.2926
5.4998
5.1754
5.4998
6.4929
5.3784
6.3845
6.3845
5.5662
5.4998
5.4828
5.4998
5.3509
6.3972
(1.3845..
9ldev(;
0.8891
0.8891
0.889!
.0.8891
0.8891
0.8891
0.8891
0.8891
0.7903
0.8891
0.8891
0.8891
0.88,91
0.8891
0.8891
0.8891
0.8891
0.8891
1.3191
0.8891
0.8891
0.8891
1.1940
0.8891
0.8891
0.8975
0.8891
0.9682
0.8891
0.6475
0.8891
1.0403
1.2673
0.8975
0.8975
1.3121
0.8891
X8998
0.8891
1.2796
0.9113
1.8975
n(T
29
29
29
29
29
29
29
29
29
29
29
29
29
29
29
29
29
29
138
29
29
29
30
29
29
29
29
29
29
39
79
71
37
29
29
30
29
29
29
39
28
29
(.offer
qimrlll
134.275
134.275
134.275
134.275
134.275
134.275
134.275
134.275
130.7788
134.2756
134.2756
134.2756
134.2756
134.2756
134.2756
134.2756
134.2756
134.2756
100.7926
134.2756
134.2756
134.2756
116.4235
114.2756
134.2756
323.4150
134.2756
181.2871
134.2756
114.2701
134.2756
327.3428
92.1478
323.4150
323.4150
07.8696
34.2756
31.0644
34.2756
88.9090
24.5192
23.4131)
Upper
Quarllle
445.6921
445.6921
445.692
445.6921
445.6921
445.6921
445.6921
445.6921
379.8998
445.6921
445.6921
445.6921
445.6921
445.6921
445.6921
445.6921
445.6921
445.6921
597.6636
445.6921
445.6921
445.6921
383.IOHI
445.6921
445.6921
1085.7317
445.6921
1038.7747
445.6921
273.7728
445.6921
1332.4295
509.4578
085.7317
085.7317
633.5971
445.6921
441.3642
445.6921
499.8168
109.9203
085.7317
•i
Upper 9
535.9449
5,35.9449
535.9449
535.9449
535.9449
535.9449
535.9449
535.9449
423.4977
535.9449
535.9449
533.94-19
535.9449
535.9449
535.9449
5315.9449
5J5.9449
535.9449
7714.1675
5*5.9449
53*5.9449
5J5.94-I9
992.0109
53J5.9449
535.9449
1314.9355
535.9449
1341.5739
535.9449
242.2552
535.9449
2086.6320
629.2528
314.9355
314.9355
233.1480
535.9449
535.5947
535.9449
623.0291
372.8563
311.9.155

X
X
X
X
X
X
•'
*

\\
•M
M
XI
X
X
x
X
X


»

-
-j


















Conccnlrfliioru nre given in ug/kg (ppb).                             .   ;.  '
Tlift "x* in (lie fu right column indicates thai the 95% Upper Coiifiilencc Limit is grcnicr ilien (lie iiiaxiinuin ileieclctl coiicaitraiion.
                                                                                                                           I'atf I ol 2
                                                                                                                      IlillSI.SMV.XI.'!

-------

                                                                              V      Table  1  .              .

                                                        CIIKMICAI, SUMMARY STATISTICS FOIl SOII.S - SKMI-VOI.ATI1.K OIICANICS
                                                                                     «CL Tic and TrcnlhiR Sllc
Compound
N-Nilro»odiplienyUinlno
4>Uroniophenyl pheoyledier
llcxachlorobenzene
Pcnlachlorophenol
riKiianthicnc
Anthracene
Catbazoh)
Di-n-bulytplilhalate
Flliorantheno
Pyrcno
Bulylbenzylplillialata
J.T-Dichlolobaizidino
Duuo|i)inlhricene
Cliiyseno
bii|l-GlliyllK>»yl)p"lhalala
Di-n-ociyliJilluUle
lenzo(b|fhioranlheno
lenzo|k]nuoianluem
Icuiolb/klduorainlicne
£izo(a)pyrehe
Indenol 1.2.3-cdJpyreno
XbenzafaJilantbraceno
)en»|g.h.i|peryleno
Valid
29
39
29
29
140
MO
30
29
143
144
19
20
143
142
31
28
30
30
113
141
139
137
137
Occur
0
0
Q
0
51
40
9
0
58
60
0
0,
48
4»
10
0
•8
9
37
41
33
22
26
Undtltcl
29
29
29
29
87
100
21
29
85
84
29
20
95
91
21
28
22
21
76
100
106
III
III
Efllmaltd
0
0
0
0
37
31
9
0
36
38
0
0
32
32
10
0
7
8
20
29
19
16
19
Hcjcc
1
2
1
2'
IB
18
r
2
15
14 '
' 2 '
II
13
"6
0'
3
1
1
14
17
19
21
21
Frequent;
• i)«lcc(ed
0.00
0.00
0.00
0.00
0.38
0.29
0.30
0.00
0.41
0.42
0.00
0.00
0.34
0.35
0.32
' 0.00
' 0.27 '
0.30
0.33
0.29
0.24
0.16
0.19
Minimum
'Concentration
DcfttUd
0.00
0.00
0.00
0.00
22.00
J5.00
4I.OU
0.00
26.00
49.00
0.00
0.00
47.00
22.00
40.00
0.00
240.00
150.00
34.00
150.00
100.00
60.00
28.00
Multnum
Concentration
StSidii
0.00 •
0.00
0.00
o.oo
570000.00
330000.00
27000.00
0.00
980000.00
600000.00
0.00
0.00
190000.00
210000.00
180.00
0.00
77000.00
81000.00
12000.00
64000.00
14000.00
8300.00
- 8700.00
Medlsa
195.00
195.00
195.00
475.00
165.00
165.00
192.50
195.00
165.00
163.00
195.00
187.5Q
165.00
165.00
190.00
197.50
205.00
105.00
165.00
165.00
165.00
165.00
165.00
lieomelrlc
Menn
244.6336
244.6336
144.6336
592.5723
263.0221
218.1026
124.9271
244.6336
324.0151
321.0549
244.6336
I89.3M8
2J8.27I3
179.7824
115.2594
246.8517
359.5353
369.6181
181.8111
174.1705
130.8309
100.6938
209.8463
Arithmetic
Mean
593.9655
593.9655
593.9655
1469.8276
5346.5429
3964.4357
1272.4331
593.9655
8356.6923
5325.5278
593.9655
189.7500
1949.6294
2521.5182
558.9032
608.3929
3090.3333
3286.3333
732.8584
1157.6241
416.5468
360.1460
379.7126
Standard
Deviation
1497.4433
1497.4433
1497.4433
3750.1475
48683.0623
29885.3442
4978.1315
1497.4433
82059.4096
50039.9020
1497.4433
12.9244
15945.2828
18321.5524
1453.7869
1522.8677
13985.9126
14717.5741
1619.1043
6106.1583
1248.5085
1008.8369
985.9136
nicnn(jj_
5.-199B
5.4998
5.4998
6.3845
5.5745
5.3850
5.4158
5.499H
5.7808
5.7716
5.4998
5.2435
5.5540
5.6340
5.3718
5.5088
5.8848
5.9125
5.6448
5.6141
5.4417
5.3018
5.3464
sldev(j)
0.8891
0.8891
0.8891
0.8975
1.351 1
1.2478
1.1885
0.8891^
1.4859
1.4381
0.8891
0.0678
1.1378
1.2736
0.9773
0.9041
1,3446
1.3764
1.1627
1.0364
0.7431
0.6604
0,7403
«(1
29
19
29
29
140
140
30
29
143
144
29
20
143
142
31
28
30
30
113
141
139
137
137
l.oner
Quarllle
134.2756
134.2756
134.2756
323.4150
105.9520
93.9811
100.8803
134.2756
118.9022
121.6650
134.2756
180.8676
119.8698
118.4779
111.3270
114.1323
145.1344
146.0415
129.0759
136.3059
139.8147
128.5421
127.3508
Upper
Quorllle
445.6921
445.6921
445.6911
1085.7317
655.9152
506.1521
501.5071
445.6921
882.9591
847.1137
445.6921
I98.I9R4
556.4709
660.6987
416.2206
454.2959
890.6616
935.5214
619.6998
551.8784
381.0966
313.3449
345.7808
Upper 95
535.9449
535.9449 I
535.9449 *
1314.9355 x
874.8563
612.5094
811.4556
535.9449 »
1358.0923
1133.0200
535.9449 t
194.8931 *
6,14.1456
816.5507
532.2508 it
558.3151 >
1821.0814
2010.7316
719.2950
583.0572
344.5796
2.78.1171
312.6983
Concentrations are given in ug/kg (ppb).   '                        .               .
ITIit"»" In the far right column Indicates that die 95% Upper Confidence Limit lj greater then Hit nmilimim delected concentration.
                                                                                                                                                                                UTBSI
Page 2 if 2
 SMV.XU:

-------
                                                                                   Table.1

                                                                 CII1CMICAI, SUMMARY STATISTICS POR SOILS  • MICTAUS
                                                                                   (id. Tic nml TrcnllhR Sllc
Mclil Aiu)j(c>
Aluminum
Antimony
Arsenic
Uiriuin
Ueiylliuin
Cldmiuin
Cikiuin
Guomium
Cobill
Coppci
lion
Lied.
Magnesium
MaiigineK
Mercury
Nickel
Potassium
Selenium
Suve,
Sodium
fdilliuin
tanldium
'.ins
Villd
31
31
31
31
31
31
31
31
31
31
31
31
31
31
31
31
31
31
31
31
31
30
31
Occur
31
|
30
31
14
3
31
31
31
31
31
31
31
31
0
31
30
0
0
31
9
30
31
Undelccl
. 0 •
30
1 i
0'
11
28,
0
0
0
0
0
0
0
0.
31
01
1
31
31 •
0
n
0
0
Efllmilcd
0
1
10
0
0
0
5
0
0
11
0
31
0
0
0
1
0
0
0
. 0
8
0
7
Reject
•o
0
• 0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
1
0
Frequency
Delected
1. 00
0.03
0.97
1.00
0.45
0.11)
1.00
1.00
1.00
1.00
1.00
1.00
1.00
1.0Q
o.oo
1.00
0.97
0.00
0.00
1.0(1 '
0.29,
1.00
i.oo
Minimum
Concentration
Detected
3670.00
10.40
4.30
22.80
0.22
0.86
303.00
8.SO
5.50
10.80 •
13600.00
$.50
1500.00
114.00
0.00
13.50 •
429.00
0.00
0.00 •
52.50
0.19 •
5.70
34.10
Miilnituu
Concentration
Delected
14300.00
10.40
13.60
82.SO
3.20
1.10
14200.00
23.30
17.20
176.00
32100.00
46.00
5380.00
865.00
0.00
29.60
1400.00
0.00
0.00
412.00
1.30
20.50
78.90 '
MedUn
10100.00
4.10
7.00
39.80
0.25
0.35
1070.00
14.00
10.10
22.20
22200.00
9.80
3350.00
440.00
0.06
21.20
990.00
0.25
0.65
126.00
0.38
13.20
57:00
(ieoinelrlc
Mean
9689.5184
3.8572
6.4865
40.1772
0.3245
0.3918
1352.9337
14.0705
9.4667
24.4416
22116.6306
11.0092
3336.9784,
395.6301
0.0601
21.15)4
835.7229
0.3588
0.5450
127.7032
0.37? 1
12.8662 :
55.6731
Arithmetic
Mean
9987.7419
4.0903
7.0703
43.1290
0.4202
0.4158
2338.9032
14.4903
9.8065
30.4677
22745.1613
12.2871
3429.3548
439.4194
0.0603
21.5677
899.1774
0.6052
0.5719
151.2226
0.4715
13.4933
57.0097
Stand trd
Deviation
2387.3105
1.4961
2.2424
16.8031
< 0.5168
0.1859 __,
3069.9587
3.5234
2.6825
30.3286
5270.0942
7.7355
778.1257
187.4675
0.0056
4.2366
. 297.1177
0.7899
0.1648
96.3311
0.3061
4.1003
12.1220
tne>n(j)
9.1788
1.3500
1.8697
3,6933
• 1.1254
•0.9370
7.2100
2.6441
2.2478
3.1963
10.0041
2.3987
8.1128
5.9805
•2.8121
3.0517
6.7283
•1.0250
•0.6070
4.8497
•0.9885
2.5546
4.0195
»ldc»(;)
0.2568
0.3533
0.5)98
0.1808
0.5791
0.31(13
0.9977
0.2494
0.2695
0.5843
0.2-158
0.4351
0.2459
0.4945
0.0902
0.2015
0.4316
0.9096
0.3501
0.5761
0.7692
0.3207
0.2266
•t(j)
31
31
31
31
31
31
31
31
31
31
31
31
31
31
31
31
31
31
31
31
31
30
31
l^on-er
Quirllle
8148.1087
3.0391
4.5065
31.0751
0.2196
0.3178
690.1415
11.8913
7.8928
16.4793
18737.3610
8.264)
2826.7983
283.4069
0.0565
18.4383
624.5892
0.1942
0.4303
86.560)
0.2215
10.3628
47.7813
tipper
Quirllle
11522.5227
4.8956
9.3363
. 51.9453
0.4796
0.4830
2652.2526
16.6491
11.3544
36.2511
26105.3489
14.6658
3939.2357
552.2915
0.06)8
24.2638
1118.2275
0.6627
0.6902
188.4017
0.6253
15.9743
64.8682
Upper 95
10880.6957
4.6188
9.1024
49.1030
0.4737
0.4552
3458.7,178
15.7304
10.7134
35.8710
24672.2994
13.9356
3722.9406
531.8669
0.0620 i
21.0)88
1063.6061
0.7977 »
0.651 1 i
185.8991
0.6785
15.0851
61.4204
BOIES;                                                                 -
'Coneemiitlonj ttt given in mgAit (ppm).
(The V in tin fu iltht column Indicate! lint Die 95% Upper Confidence Limit Is gicucr Own i)» minimum delected concenmtion.
    I'lte I of I
U niSI.MTI..XI.S

-------
                                                                                 Table  1  .

                                                            CIIICMICAI, SUMMARY STATISTICS FOR SOILS - I'KSTIUDES
                                                                                 (JCi/llc	ITrcnflrtjj'Sllc
CCilipGiiilu
alplia-UIIC
bcla-DllC
della-HIIC
gnninia-llllC
llcplnclitor
Alclrin
ii ii *i

Endcuulfan 1
Dieldrin
1)1)1!
liiulrlil
indoaulfim II
DIN)
liulusulfnn sulfnle
DDT
rfc'riioxyclilor
Sndrin ketonc
£ndriit aldehyde
Ipha-Chlordane
gmiuiH-Chlofdiinc
oiaphciie
Aioclor-1016
Aroclur-1221
Afoclor-1232
Aroclor-1242
Aioc!or.|24B
Aroclor-1254
roclot-1260
V=!!d
29
29
29
29
29
29


29
28
29
27
27
30
29
19
26
28
29
27
29
29
29
29
29
29
29
30
29
Oscar
0
0
0
0
0
1


0
0
0
0
1
1
0
3
2
3
0
0
0
0
0
0
0
:!;:i;d
o.oo
• Q.OO
0.00
0.00
0.00
(Ml.)
:

'0.00
0.00
0.00
0.00
0.04
, 0.0,1
0.00
0.10
0.08
0.11
0.01)
0.00
0.00 •
p.o«
0.00,
(1.00.
0.90
0.00
0.03
0.03
0.07
Minimum
:!:c!cd
0.00
0.00
0.00
0.00
0.00
0.70
rt 111!

0.00
0.00
0.00
0.00
" 2.20
11.00
0.00
1.40
0.68
•1.00
. 0.00
0.00
o.cio
• 0.00
0.00
0.00
0.00
0.00
HO.OO
440.00
12.00
Maximum
roiicenlrnllon
!>:!e:!:d
0.00
0.00
0.00
0.00
0.00
0.70


0.00
0.00
0.00
0.00
2.20
. 11.00
0.00
120.00
39.00
38.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
140.00
440.00
14.00
Media!
1.00
I.OU
I.OU
1.00
1.00
1.00


1.00
1.9S
2.00
2.00
2.00
2.00
2.00
2.00
10.25
2.03
2.00
1.00
1.00
Kio.no
20.00
40.30
20.00
20.00
20.00
20.00
19.50
(itnuirlrlc
Mean
1.1588
1.1588
1.1588
(.1588
1.1588
1.1-188


1.1588
2.2226
2.2700
2.2880
2.0151
3.3926
2.2700
2.4937
9.7336
3.6982
2.2700
1:0739
I.I58R
115.88-16
2216999
45.9115
22.6999
22.6999
24.3637
25.0575
22.0923
Arllluiifllc
Mee»
1.4448
I.4-M8
I.44.-I8
1.4448
1.44-18
1. -1.179


1.4-148
2.7554
2.8017
2.8574
2.0144
3.0/50
2.8017
6.4500
11.1608
4.6500
, 2.8017
1.2889
1.4448
144.4828
.28.0172
56.9828
28.0172
28,0172
32.2241
41.7500
27.5862
Sli.nJ.rd
!)tv(9l!ei!
1.6433
1.6433
1.6-133
1.6-133
1.6433
1.6461


1.6433
3,1376
3.0912
3.2001
0.4324
3.W)2
3.0912
21.8927
6.4096
8.0121
3.0912
1.5429
1.6433
164.3.149
30.9116
03.8108
30.9116
30.9116
37.1682
81.1187
31.0791
nifnnfyj
0.1474
0,1474
0.1474
0.147-1
0.1474
O.IJHR
II nHrio

0.1474
0.7987
0.8I9A
0.8277
0.7007
11.8 /2.|
0.8198
0.9138
2.2756
0.9926
0.8198
0.0713
0.1474
•1.7526
3.122-1
3.8267
3.122-1
3.1224
3.1931
3.2212
3.0952
siitevft.
0.5171
0.5171
0.5171
0.5IJI
0.5171
(1.5235


0.5171
0.5032
0.5071
0.5246
0.1576
0.5755
O.S07I
0.8,319
0.6243
0.8075
0.5071
0.4314
0.5171
0.5171
0.5071
0.5133
0,5071
0.5071
0.6068
0.7356
0.5262
n(»
29
29
29
29
29
29


29
28
29
27
21
311
29
29
26
28
29
27
29
29
29
29
29
29
29
30
29
l,ow»r
Ouarlllc
0.8176
0.8176
0.8176
0.8176
0.8176
0.8071)


0.8176
1.5827
1.6123
1.6060
I.8IJ8
1.6227
1.6123
1.4226
6.3877
1.56-18
1.6123
0.8027
0.8176
81.7569
16.1233
32.4724
16.1233
16.1233
16.1789
15.2543
15.4902
tlppfr
Ounrllle
1.6426
1.6-126
1.6426
I.M26
1.6426
U.J55


1.6-126
3.1210
3.1959
3.2596
2.2412
3.5278
3.1959
4.3712
14.8321
4.6524
3.1959
1.4.366
1.6426
1 64.2581
3I.95B9
64.9124
31.9589
31.9589
36.6891
41.1607
31.5082
(loot r 95
1.6027 s
. 1.6027 i
1.6027 x
1.6027 x
1.6027 x
: 1.5989 x


1.6027 x
: 3.0153 x
3.1095 x
3.2146 x
.2.1524
'3.4942
3.1095 X
5.0216
15.3039
5.2891
3.1095 J
1.3834 i
-1.6027 x
160.2730 x
31.095-1 x
6,3.2696 x
3,1.0954 x
31.0954 x
36.9529
44.0149
30.8272 n
MOUiS:
Concern/aliens are given In ug/kg (ppb),                           .   - §
The "x." in (lie far right column indicates Dial (he 95% Upper Confidence Limit It greater Hint (lie niaxliiiuinitnccted c
    I'afte I of I
IMIISI.I'Sr.XI.S

-------
                                                                               Table  2
                                                 CIIEMICALSUMMAIlYSTATIJmtS FOIl SURFACE WATER •  VOLATILE OIUJANICS
                                                                               GCLTIc nnd Trailing Site
Compound
Chloromelliine
BromoiueUiane
Vinyl chlaidc
Clilorocdiane
kleUiylete chloride
Acetone
Carbon disulfide
l.l-DichloioedKiK
|.l-l)ichlorix:Uuiie
1,2-DichloroeilKrra
JMoroform
l,2iDidiloroeUiiin
2-UuUnoire
,1,1-TricliloroeUiane
'ubon telracliloride
IroniodichlorotneUiane
,2- Dicliloropropane
c'a- 1,3-DichloiopropeiK
TricliloroeUieM
Uibromoclilorome thine
1-,1,2-Trichioroedume
eiizeiie
If till- 1 .3 -Dkliloropr opeiw
Iromofonn
4>MeUiyi-2-penUnone
•HexanoiiG
elracritof oclhe ne
1,1,2,2-Tclrichloroellune
'olueiK
ChlorobeiiMne
!mylbcnzcne
Styretw
ylenci
V.lld
6
6
6
«
6
6
6
6
6
6
6
6
6
«
6
<
6
6
6
6
6
6
6
6
6
6
6
6
6
6
6
6
6
Occur
. (1
0
0
I
0
q
0
0
0
P
0
0
0
0
0
a
.0
0
a
0
0
0
0
0
0
a
0
0
0
0
0
0
0
Untletec
6
6
6
5
6
6
6
6
6
6
6
6
6
6
6
6
6
6
6
6
6
6
6
6
6
6
6
6
6
6
6
6
6
l!fllili»led
' 0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
llejec
0
0
U
0
0
0
0
n
n
0
0
0
0
0
0
0
0
0
0
a
0
0
a
0
0
0
0
0
0
0
0
0
0
l-'renucliCY
Delected
o.uo
0.00
0.00
0.17
0.00
0.00
0.00
0.00
o.oo
0.00
0.00
0.00
0.00
0.00
0.00
0.00
•o.oo
o.oo
o.oo
0,00
0.00
0.00
0.00
u.oo
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
• Minimum
Concentration
. Detected
0.00
; 0.00
: 0.00
u.oo
! 0.00
0.00
: 0.00
0.00
! o.oo
• o.oo
< 0.00
1 0.00
0.00
0.00
0.00
0.00
• 0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
o.oo
0.00
0.00
0.00
0.00
0.00
0.00
Q.OO
0.00
Maximum
Concentration
Detected
0.00
0.00 .
0.00
12.00
o.oo
o.oo
0.00 .
0.00
0.00
o.oo
o.oo
o.oo
o.oo
o.oo
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
Meet In
5.00
5.00
5.00
5.00
5.00
5.00
5.00
5.00
5.110
5.00
5.00
8.00
5.00
5.00
5.00
5.00
5.00
5.00
5.00
S.oo
5.00
5.00
5.00
5.00
5.00
5.00
5.00
5.00
5.00
S.OO
5.00
5.00
5.00
ficomclrlc
Mean
S.UOOO
5.0000
5.0000
5.7855
5.0000
6.134)
5.0000
5.0000
5.0000
5.0000
5.0000
7.9187
5.0000
5.0000
5.0000
5.0000
5.0000
5.0000
5.0000
5.0000
5.0000
5.0000
•5.0000
5.00UO
5.0000
5.0000
5.0000
5.UOUO
5.0000
5.0000
5.0000
5.0000
5.01100
Afllnntclle
mean
5.0000
5.0000
: 5.0000
6.1667
• 5.0000
• 6.8J33
5.0000
5.0000
i 5.11000
1 5.0000
1 5.0000
8.3333
. 3.0000
! 5.0000
> 5.0000
5.0000
5.0000
5.0000
5.0000
5.0000
5.0000
5.0000
5.0000
5.0000
5.0000
5.0000
5.0000
5.0000
5.0000
5.0000
3.0000
5.0000 .
5.0000
Standard
Deviation
0.0000
0.0000
0.0000
2.8577
0.0000
4.2505
0.0000
0.0000
0.0000
0.0000
0.0000
3.0768
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
o.oooo
0.0000
0.0000
0.0000
0.0000
o.oooo
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
IHQ»n(Tj
1.6094
1.6094
1.6094
1.7553
1.6094
1.8139
I.60V4
1.6094
U.OV4
1.6094
1.609-1
2.0692
1,609-1
1.6(194
1.6094
1.6094
1.6094
1.6094
1.6094
1.6094
1.6094
1.6094
1.6094
1.6094
1.6094
1.6094
1.609-1
1.609-1
1.609-1
1.6094
1.6094
1.6094
1.6094
ildevfj
0.0000
0.0000
0.0000
0.3574
0.0000
0.4557
0.0000
0.0000
0.0000
0.0000
0.0000
0.3430
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
n(T
6
6
6
6
6
6
6
6
6
6
6
6
6
6
6
6
6
6
6
6
6
6
6
6
6
6
6
6
6
6
6
6
6
l>ower
Qunlllc
5.0000
5.0000
5.0000
4.5459
5.0000
4.5106
5.0000
5.0000
5.0000
5.0000
5.0000
6.2830
5.0000
5.0000
5.0000
5.0000
5.0000
5.0000
5.0000
5.0000
5.0000
5.0000
5.0000
5.0000
5.0000
5.0000
5.0000
S.oooo
5.0000
5.0000
S.OOOO
5.0000
5.0000
Upper
Qnaillle
5.0000
5.0000
5.0000
7.3631
5.0000
8.3423
5.0000
5.0000
5.01)110
5.0000
5.0000
9.9802
5.0000
S.OOOO
5.0000
5.0000
5.0000
5.0000
5.0000
5.0000
5.0000
5.0000
5.01100
5.0000
5.0000
5.0000
5.0000
S.OOOO
5.0000
5.0000
S.OOOO
5.0000
5.0000
Upper 95
5.0000 i
5.0000 I
5.0000 x
8.9S06
S.OOOO x
11.4082 I
s.JKxxi x
5.0000 x
S.ODOO x
5.0000 I
5.0000 X
11.9564 I
5.0000 i
5.0000 I
5.0000 i
5.0000 x
5.0000 l
5.0000 x
5.0000 >
5.0000 x
5.0000 x
5.0000 x
5.0000 i
5.0000 >
5.0000 x
5.0000 i
5.0000 i
s.oooo i
5.0000 x
5.0000 i
5.0000 x
S.OOOO x
S.OOOO «
(Joncentiat iom lie (jiven in uiiiu of ug/L (pph).
The "x" in UK fa right column indicates that UK 95ft Upper Confidence Limit u greaii
r Ihen lite maximum detected concentration.
                                                                                                                IV I of I
                                                                                                           IIII1SWVOI..XI.S

-------
                                                                                  Table  2

                                                 CHEMICAL.SUMMARY STATISTICS I'OKSUIWACIC WATI5K - SKMI-VOLATILEORCANICS
                                                                                   tiCI/llc mid Trailing SHc  .
Compound
rhtnol
bh|2-Chloroeiliyl]ether
2-Chtoro|>licnol
1,3-Dielilorobenzene .
1,4-Dicliloiobenzene
1 ,2-UicliloiotKnzene
2-McUiylplicnot
2,2'-oxybis-I-Chloropropane
4-Methylplicnol
N-Niuosodi-n-propylaniine
Hexachloroelliatie
Nitrobenzene
sophorone
2-NilropItcnol
2,4-Diiiiclliylplieiiol
bi3l2-C!ilofoeihoxy]mcthano
2,4-DicMoroplieiiol
1.2.4-Trichlorobcniene
[aphtha lene
4-OitoroaniliiiD
ex acbloro butadiene
4:-Chloro-3-inethylphenol
-Methyl naphthalene
exachlorocyclopeatadiena
2,4,6-Tiichlorophenol
,4,5-Trichloroplienol
•Cbloronaplithalene
•Nilroaniline
Diinelhylpbllialalo
Acenaphthylcne
,6-Diniirololueiie
Nilroaniline
ceniplilhene
2,4-Dinitrophenol
4-Nilrophenol
Dibenzofurmi
2.4-DinUrololucno
eiliylphlhalate
"hlorophcnyl phenylelhtr
uoreiie
Nilroaniline
i-Dinitro-2-inciliylplienol
V.ll
6
6
6
6
6
6
6
6
6
6
6
6
6
6
6
6 '
6
6
6
1
6
6
6
6
.6
6
6
6
6
6
6
5
6
6
6
6
6
6
6
6
I
6
Occu
0
0
o
p
.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
o •
0
0
0
0
0
0
0
0
0
0
0
0
Undcltc
6
6
6
«
6
(,
6
6
6
«
6
6
6
6
6
6
6
6
6
1
6
6
6
6
6
6
6
6
6
6
6
5
6
6
6
6
6
6
6
6
1
6
Eillmalc
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
0
0
0
0
0
0
0 '
0
0
0
0
0
0
0
llcjfc
0
I)
0
n
0
0
0
0
0
0
0
o
0
p
. 0
0
0
0
0
5
0
0
0
0
0
0
0
0
0
0
0
i
0
0
0
0
0 :
0
o ;
0 :
5
,0
I'ltquenc
lltltcltii
0.00
0.00
. 0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
o.uo
0.00
' 0.00
0.00
0.00
0.00
o.oo
.0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
o.ou
0.00
0.00
Minim inn
Oiicciitrnllon
Ucfccitu
0.00
0.00
0.00
0.00
0.00
0.00
• o.ou
0.00
0.00
0.00
0.00
0.00
o.ou
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
o.oo
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
.0.00
0.00
0.00
0.00
0.00
o.oo
0.00
0.00
Maximum
('ontcnlrftllon
iiiicc'.c;!
o.oo
0.00
0.00
o.oo .
o.oo
0.00
o.oo
0.00
0:00
0.00
0.00
0.00
0.00
0.00.
0.00
o.oo
0.00
0.00
0.00
0.00
o.ou
0.00
o.oo
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
•o.oo
Mtc!!;!
5.00
5.00
5.00
5.00
5.00
5.00
5.00
5.00
5.00
5.00
5.00
5.00
5.00
5.00
5.00
5.00
5.00
5.00
5.00
5.00
5.00
5.00
5.00
5.00
5.00
12.50
5.00
12.50
5.00
5.00
5.00
12,50
5.00
12.50
12.50
5.00
5.00
5.00
5.00
5.00 •
12.50
12.50
i (tcnmclrl
Menn
5.0000
5.001K)
5.00UO
5.0000
5.0000
5.11000
5.0000
' 5.0000
5.0000
5.0000
5.0000
5.0000
5.0000
5.0000
5.0000
5.0000 .
5.0000
5.0000
5.0000
5.0000
5.0000
5.0000
5.0000
5.0000
5.0000
12.5000
5.0000
12.5000
5.0000
5.0000
5.0000
12.5000
5.0000
12.5000
12.5000
5.0000
5.0000
5.0000
5.0UOO
5.0000
12.5000
12.5000
Arlllinttllc
Mefln
5.0000
J.0000
5.0UOO
5.0000
5.0000
i.OHHU
5.0000
5.0000 .
5.0000
5.0000
5.0000
5.0000
5.0000
5.0000
5.0000
5.0000
5.0000
5.0000
5.0000
5.0000
5.0000
5.0000
5.0000
5.0000
5.0000
12.5000
5.0000
12.5000
5.0000
5.0000
5.0000
12.5000
5.0000
12.5000
12.5000
5.0000
5.0000
5.0000
5.0000
5.0000
12.5000
12.5000
Slnndnrd
Devlallo
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
o.oooo
0.0000
0.0000
0.0000
0.0000
IDIV/OI
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
»DIV/DI
0.0000
lncnn(^
1.6094
1.61)9.1
1.609-1
1.6094
1.609.1
1 .609.1
1 .SII94
1.609.1
1.609-1
1.609-1
1.6094
1.609-1
1.6094
1.6094
1.6094
1.6094
1.6094
1.6094
1.6094
1.6094
1.6094
1.6094
1.6004
1.6094
1.6094
2.5257
1.6094
2.5257
1.6094
1.6094
1.6094
2.5257
1.6094
2.5257
2.5257
1.6094
1.6094
1.6094
1.6094
1.6094
2.5257
2.5*57
3(dev
-------
                                                                                   Table  2
                                                CIIEMICALSUMMAHY STATISTICS FOR SURFACE WATKIl
                                                                                   (JCL Tic nnd Trent lug Sllc
SEMI-VOI jVTIl.E OUC ANICS
Compound
N-Nitrosodiphenyuunlns
4-Bromophenyl plienylotlier
llexachloroberizeno
Penlacliloroplienol
Phcnanihreno
Anthracene
Carbazolo
Di-n-bulylphlhilato
Fluorantliene
Pyiene
Oulylbenzylphdialite
3!?-Dichlorobenzldino
3enz0[*)uidiracene
Clirysene
blsll-BUiylhexyltFlilhalale
)i*n*oclylplitlui1ato
Uenzolbjriuoriuilhene-
Jenzo[k|nuoraAi1ieno
)«nto[a)pyrene
lnd«io[l ,2,3-cdJpyreno
>ibenzot'a,li)»nuiracene
Henzo|g,li,ijperyleno
V«lld
6
6
6
6
6
6
6
6
6
6
6
1
6
t
6
6
6
6
•6
6
6
6
Occur
0
0
0
0
P
P
0
0
0
0
0
0
0
0
0
P
0
• 0
0
0
0
0
Undclecl
6
6
6
0
6
6
6
6
6
6
6
I
6
6
6
«
6
6
6
<
«
6
Estimated
0
0
0
0
a
0
0
0
0
a
0
0
0
0
0
0
0
0
0
'0
0
0
Reject
0
0
0
0.
a
0
0
0
0
0
0
5
0
0
a
0
0
a
0
0
0
0
Frequency
Delected
0.00
0.00
0.00
0.00
o.ou
0.00
0.00
0.00
0.00
0.00
0.00
0.00
o.oo
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
Minimum
Concentration
Delected
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
Maximum
Concentration
Delected
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00 .
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
o.oo
0.00.
0.00 .
Mtdlon
5.00
5.00
5.00
12.50
5.00
5.00
5.00
5.00
5.00
5.00
5.00
5.00
5.00
5.00
5.00
5.00
5.00
5.00
5.00
5.00
5.00
5.00
Geometric
Mean
5.0000
5.0000
5.0000
12.5000
5.0000
5.0000
5.0000
5.0000
5.0000
5.0000
5.0000
5.0000
5.0000
5.0000
5.0000
5.0000
5.0000
• 5.0000
5.0000
5.0000
5.0000
5.0000
Arithmetic
Menn
5.0000
5.0000
5.0000
12.5000
5.0000
5.0000
5.0000
5.0000
5.0000
5.0000
5.0000
5.0000
5.0000
5.0000
5.0000
5.0000
5:0000
5.0000
5.0000
5.0000
5.0000
5.0000
•Standard
Deviation
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
o.oooo
0.0000
0.0000
»D1V/UI
0.0000
0.0000
0.0000
0.0000
o.oooo
0.0000
0.0000
•0.0000
0.0000
0.0000
meim(j)
1.6094
1.6094
1.609-1
2.5257
1.609-1
1.6094
1.6094
1.6094
1.6094
1.6094
1.6094
1.6094
1.6094
1.6094
1 .6094
1.6094
1.6094
1.6094
1.6094
1.6094
1.609-1
1.6094
sldev(j)
0.0000
0.0000
0.0000
o.oooo
0.0000
0.0000
o.oooo
o.oooo
0.0000
0.0000
0.0000
•DIV/OI
o.oooo
o.oooo
0.0000
0.0000
0.0000
0.0000
0.0000
o.oooo
0.0000
0.0000
n(r)
6
6
6
6
6
6
6
6
6
6
6
1
6
6
6
6
«
«
6
6
6
6
Lower
Querllle
5.0000
5.0000
5.0000
12.5000
5.0000
5.0000
5.0000
5.0000
5.0000
5.0000
5.0000
»DIV/OI
5.0000
5.0000
5.0000
5.0000
5.0000
5.0000
5.0000
5.0000
5.0000
5.0000
Upper
Qunrille
5.0000
5.0000
5.0000
12.5000
5.0000
5.0000
5.0000
5.0000
5.0000
5.0000
5.0000
KDIV/OI
5.0000
5.0000
5.0000
5.0000
5.0000
5.0000
5.0000
5.0000
5.0000
5.0000
Upper 95
5.0000 x
5.0000 x
5.0000 x
12.5000 x
5.0000 *
5.0000 x
5.0000 x
5.0000 x
5.0000 i
5.0000 x
5.0000 x
»DIVAM 1
5.0000 x
5.0000 x
5.0000 x
5.0000 x
5.0000 x
5.0000 x
5.0000 x
5.0000 x
5.0000 x
5.0000 x
MQIES:                                                     ;              '
Coiicemriiloni we given In ujilu of u&rt, (ppb).                            .                  .
Tim "«" In llio tu right column Indicated that Ilia 95% Upper Coiificlenco l.iiuil it greater Ihcn Hie minimum Jelectrrl coiicenlralion.
                                                                  Tag
                                                                                                                                                                             UTIISWSMV.XLS
                                                                      2 of 2

-------
                                                                                Table  2

                                                        CHEMICAL SUMMARY STATISTICS FOR SURFACE WATER • METALS
                                                                                (JCL Tie nnd Trcnlhm Silt;
Mclil AnaEjic:
Aluminum
Antimony
Anenic
[janum
Ikrylliujn
-•dmiuin
Calcium
3iromiuiR
Cobill
Copper
Iron
Lied
hlagnejium
klanganett
rieicury
Nickel
'otujlum
Selenium
Silver
Sodium
Thilliuin
Vuudium
inc
VeJU
<
f
6
6
6
6
6
6
6
<
«
0
6
6
6
6
6
6
6
6
6
«
6
Occur
6
0
3
6
0
0
6
3
0
3
6
0
6
6
0
2
6
1
0
6
6
0
<
Unefelcc
0
6
3;
0
6.
6'
0
3
6
)
0
0
0
0
6
4
0
S^
6.
0
6
6
0
!!:!!::i:!cd
0
0
1
0
0
0
0
0
0
0
0
0
0
0
0
0
0
1
0
0
0
0
6
ricj— !
0
0
0
0
0
0
0
0
0
0
0
6
0
0
0
0
0
0
0
0
0
0
0
Preqtiencj
L'ciccijJ
1.00
0.00 .
0.50
1.00
0.00
0.00
1,00
0.50
0.00
0.50
1.00
•DIV/UI
1.00
1.00
0.00 :,
0.3]
1.00
0.17
0.00
1.00
0.00
0.00
1.00 '
Minimum
Concentration
Dttec'.cd
124.00
0.00
5.00
48.10
0.00
0.00
37900.00
6.20
0.00
16.80
756.00
0.00
2480.00
110.00
0.00
12.30
3450.00
2.00
0.00
4940.00
0.00
0.00
14.20
Minimum
Concentration
DelKied
8420.00
0.00
11.40
298.00
0.00
0.00
64400.00
12.20
0.00
13.20
1 1700.00
0.00
16400.00
8710.00 .
0.00
19.60
9620.00
2.00
0.00
34000.00
0.00
0.00
116.00
.MrJ!:r.
2292.00
18.00
3.50
66.05
1.00
I.JO
44150.00
4.60
4.00
11.15
3I30.OO
I01V/OI
5071.00
1097.10
0.10
6.00
5880.00
1.00
3.00
18185.00
1.50
6.00
48.75
Ocomelrlc
Mean
1311.8401
18.0000:
4.0S85
8)'.8)20'
1.0000
1.5000
41254.9556
5.1372 .
4.0000
11.6946.
3113.512]
nuiv/ui •
5291.4066'
777.6803:
0.1000 :
.8.2597 '
5725,3877
1.1225 .
3.0000 :
14572.7417.
1.51)00 '.
6.0000
46:2014
Arlllimcllc
Me£»
3432.6667
18.0000
5.3667
107.0500
1.0(100
1.5000
4)100.0000
6.0667
4.0000
15.7500
4889.3)3]
IUIVAII
6780.0000
22)6.0000
0.1000
9.3500
614).)))}
1.1667
3.0000
22688.333J
1.5000
6.0000
54.9500
Standard
!!c:!s!bn
3686.7409
0.0000
4.2472
96.8497
0.0000
0.0000
1)768.9506
3.8588
0.0000
12.6464
4561.6412
HUIV/OI
5)85.0720
3302.6)86
0.0000
5.6546
2469.3940
0.4082
0.0000
20407.I8S4
0.0000
0.0000
33.8460
nu>n(r)
7.1807
2.8904
1.4008
4.4288
0.0(100
0.4035
10.6275
I.C365
1.386)
2.4591
8.0435
JUIV/UI
8.5738
6.656)
•2.3026
2.1 114
8.6327
0.1155
1.0986
9.5869
0.4055
1.7918
3.8330
:!.-!=s^j!
1.78)8
0.0000
0.82)4
0.7011
0.11000
0.0000
O.J271
0.6270
0.0000
0.8592
1.0972
ADIV/UI
0.7616
1.701)
0.0000
0.5152
0.4 164
0.28)0
0.0000
1.0871
0.0000
0.0000
0.6854
"(S
6
6
6
6
6
6
6
6
6
6
6
0
6
6
6
6
6
6
6
6
6
6
6
Lower
QavlRt
394.3376
18.0000
2.3287
52.2374
1.0000
1.5000
3)084.1057
3.3651
4.0000
6.5500
1485.1662
>DIV/OI
3165.3926
246.7522
0.1000
5.8)46
4)2).0)09
0.9274
3.0000
6998.8444
1.5000
6.0000
29.0953
Upper
Qua;i!!c
4)77.406)
18.0000
7.07)2
134.3)58
I.OOOU
1.5000
5I44J.7772
7.8424
4.0000
20.8801
6527.1880
•IDIVAII
8845.3432
2450.9879
0,1000
11.6926
7582.6579
1.3586
3.0000
30)42.8379
l.iOOO
6.0000
73.3649
!!f per SJ
1597293.2913 *
18.0000 >
21.0544 »
290.1790
1.0000 \
1.5000 J
607()3.I92I
14.3631 «
4.0000 «
69.143) X
506)8.9535 *
»DIV/BI 7
22192/45)2 <
505323.5278 K
0.1000 I
17.4672
9853.0333 »
1.5428
3.0000 i
2259)0.3156 »
1.5000 >
6.0000 i
151,5501 *
Cnncenlralidns are given in unlliof ug/1, Qipb).                        ...
    x" In (lie (u light column Indicates thai Ute 95% U|i|Kf Confidence Limil b Riealei tlren Uw inaxiinuin detected concentiition.
      I'.je I of I
• irmswtiii..xi.s

-------
                                                                           Table  2
                                                                                      '
                                                 CIIHM.CAL SUMMARY STATISTICS FOR SUUFACU WATBU -

                                                                          GCI/nenwl Treating Sllc,           '
Compound
alrJIia-BIIC
bcla-UIIC
delta-DIIC
gamina-DltC
lleplichlor
Aldrin
llcptachlor epoxlde
Eixlosullan 1
Dieldiln
UDU
Endrln
Rjidosulfnii II
DUD
EndosuUan sullale
our
Methoxycliloi
Endrin kctonc
latorin aldehyde
alplia-Qdordane
Ramma-Clilordane
'oxapliene
Aroelw-1016
Aroclor-1221
Aroclor-1232
Afbclor-I2
-------
                                                                                  Table  3
                                                      CIIEMICALSUMMARYSTATISTICSKOIlSEDIMENT r VOI.ATII.K(MOANICS
                                                             !                     «CI, Tie nmrrronllnK Silo  .
Compound
Chloiontcihinc
Dioinomediane
Vinyl chloride
Chloioelliiiio
Mclhyfeic chloride
Actloire
Caibon dhulfiile
l.l'DkliloiocUicne
I.l-Dicliloioetliane
1,2-Dicliloiocllicne
Cliloiofoini
,2-DidiloioetltiiK
2-OuUnoue
yj-Trtchloioeilume
Cubon lelracliloride
DromodichloiaiKUune
.2-Didtloropropine
cb. I.J.Dicliloropropsne
TricliloroelheiK
)ibronioctilorome(luite
1.1,1-Trlchloroelluiie
«nzene
iraiu>l,3-Dichloropropeno
romofoim
4-Metliyl-2-petiunone
•llexinone
etradiloroelhene
1,1,2,2-Telncliloiaelhiiw
olueiK
ilorobenzene
nUiylbciucirt
SlyieiK
Xyknei
Vill
6
6
6
6
6
6
6
6
6
6
6
6
6
6
6
6
6
6
6
6.
6
6
6
6
6
6
6
6
6
6
6
6
6
Occu
0
0
0
0:
1
0
0
0
0
a.
0
0
0
a
0
0
.0
a
0.
a
0
0
a
0
0
0
a
0
0
0
0
0
0
Unrfelec
6
6
6
6
1
6
6
6
6
6
6
6
6
6
6
6
6
6
6
6
6
6
6
6
6
6
6
6
6
6
6
6
6
Klllinafed
• o
0
0
0
1
0
a
0
0
0
0
a
0
0
.0
0
0
0
.0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
Rejec
0
0
0
0
0
0
0
0
0
0
a
a
0
0
0
0
0
o •
0
0
0
0
0
0
0
0
0
0
0
a
0
0
0
premicnc
Detected
1 0.00
'0.00
0.00
0.00
0.17
0.00
0.00
0.00
0.00
0.00
0.00
0.00
. 0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
o.oo
0.00
0.00
0.00
0.00
Minimum
Concentration
Delected
0.01)
0.00
0.00
o.oo
15.00
o.oo
0.01)
o.oo
0.00
0.00
0.00
0.00
o.oo
o.oo
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
Maximum
Concentration
Detected
0.00
0.00
0.00
0.00
IS.OO
0.00
0.00
0.00
0.00
0.00
0.00
0.00
o.oo
o.oo
o.oo
0.00
0.00
0.00
0.00
0.00
o.oo
0.00 •
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
r.ic.iiii
a. 25
8.25
8.25
8.25
10.00
10.25
8.25
8.25
8.25
8.25
8.25
8.25
8.25
8.25
8.25
8.25
8.25
B.2S
8.25
8.2S
8.25
8.25
8.25
8.25
8.25
8.25
8.25
8.25
8.25
8.25
8.25
.8.25
8.25 .
Geometric
Mesa
.8.71)2
8.7132
8.71)2
8.71)2
9.578)
14.0659
. 8.7 13Z
8.7132
8.71)2
8.71)2
8.7132
.8.71 32
8.71)2
.8.7132
,8.7132
8.7132
8.7132
8.71)2
8.71)2
jB.7132
8.71)2
,8.7132
H.7I32
8.71)2
8.7132
.8.7132
8.7132
•8.7132
.8.7132
.8.71)2
• 8.7132
.8.7132
8.7132
Arithmetic
mean
9.08))
9.118)3
9.08)3
9.083)
10.1667
21.9167
9.1)8))
9.083)
9.08V)
9.08)3
9.08))
9.08)3
9.08)3
9.08))
9.083)
9.0833
9.0833
9.0833
9.0833
9.08)3
9.083)
9.08))
9.08)3
9.08)3
9.08))
. 9.08)3
9.08)3
9.0833
9.08))
9.08)3
9.08))
9.08))
9.083)
Standard
Devlilloi
2.8534
2.8534
2.8534
2.8534
3.6968
21.4229
2.85)4
2.85)4
2.8534
2.85)4
2.85)4
2.85)4
2.85)4
2.15)4
2.85)4
2.8534
2.8534
2.8534
2.8534
2.85)4
2.85)4
2.83)4
2.8534
2.85)4
2.85)4
2.85)4
2.85)4
2.85)4
2.85)4
2.85)4
2.85)4
2.8534
2.85)4
tnein(j
2.16-18
2.16-18
2.1618
2.1648
2.2595
2.6855
2. IMS
2. IMS
2. IMS
2.16-H
2.16-ta
2.16-tfl
2.1 MS
2.lf>l8
2. 16-18
2.1648
2.1648
2.16-18
2.16-18
2.1618
2.16-18
2.1648
2.1648
2.16-18
2.16-18
2.16-18
2.1648
2.16-18
2.16-W
2.16-18
2.16-18
2.16-18
2.16-18
ilderlL
0.3177
0.3117
0.3177
0.3177
0.3861
0.9647
0.)I77
0.)I77
0.3177
0.3177
0.3177
0.3177
0.3177
0.3177
0.3177
0.3177
O.JI77
0.)I77
O.)|77
0.3177
0.3177
0.3177
0.3177
0.3177
0.3177
0.3177
0.3177
0.3177
0.3177
O.W7
0.3177
0.3177
0.3177
nlf
6
6
6
6
6
6
6
6
6
6
6
6
6
6
6
6
6
6
6
6
6
6
6
6
6
6
6
6
6
6
6
6
6
l/mcr
yuiillle
7.032)
7.0)2)
7.0)2)
7.0)2)
7.3818
7.649*
7.0)23
7.0)2)
7.0)2)
7.0)2)
7.0323
7.0)2)
7.0)2)
7.03S3
7.0)2)
7.0)23
7.0)23
7,032)
7.0323
7.0323
7.0)2)
7.0)2)
7.0)2)
7.0323
7.0)23
7.032)
7.0)2)
7.0)23
7.032)
7.0323
7.0)23
7.0)2)
7.0)23
Upper
Quarllle
10.7959
10.7959
10.7959
10.7959
12.428)
28.1180
10.7959
10.7959
10.7959
10.7959
10.7959
10.7959
10.7959
10.7959
10.7959
10.7959
10.7959
10.7959
10.7959
10.7959
10.7959
10.7959
10.7959
10.7959
10.7959
10.7959
10.7959
10.7959
10.7959
10.7959
10.7959
10.7959
10.7959
Upper 95
12.6285
12.6285 »
12.6285 x
12.6285 i
15.5818 *
1)1,7117 >
12.6285 >
12.6285 >
12.6215 i
12.6285 «
12.6285 x
12.6285 I
12.6285 >
12.6285 >
11.6185 »
12.6285 >
12.6285 >
12.6285 «
12.6285 i
12.6185 i
11.6185 i
12.6285 „
12.6285 «
12.6285 «
12.6285 i
12.6285 >
12.6285 <
12.6285 >
12.6285 <
11.6185 »
12.6285 >
12.6285' <
12.6285 »
(.'nicenlf ttloia lie tlveti III uniu nf u|^k|! (|i|ib|.
• TlK "x" in tin fir riRll! column indicate* dial UK 95% U|iper ConMdeiKe Limit is Kiealer then lite ttelecleil rnlicclilralinil.'
                                                                                                                                                                                I'.rr I "I I

-------
                                                                                 Table  3
                                                               .SUMMAItY.STATISTICS I'ORSEUIMKNT  • SHMI-VOI.ATII.KOHCANICS
                                                                                  CCLTIpniiilTrenllngSllc  i
Compound
Phenol
bii| 2-Ctiloroetliyllelher
2-Oilorophenol
1,3-Dichlorobenzene
1,4-Diciilorobenzeno
1 .2-1 )icliluiobcii7.eno
2-Metliylplienol
2,2'-oxyl>ij-l-Chloropropane
4-Meihylplienol
N-Nitrojodi-n-|>fopyliuniiie
I lexachloro ethane
Nitrobenzene
lopliotoiie
2 -Nilro phenol
2,4-Uimelhylplienol
bi3(2-ChloroeUioxylntechane
2,4-Dicliloiophcnol
1 ,2/1-Trichlurubenzeiio
Juplillialene
4-Cliloroanilino
[cA«clilorobui»dicne
4-Cliloio-3-nicthylpticuoi
-Mclhylnaphilialcne
M acli lorocyc lopenlid icno
.4.6-Triclilorophenol
,4.3'Triclilorophenol
-Cliloronaplillialeue
2-Nitroaiiiline
Dimethylphlltalato
Acenaplilhyleno
f6»Dimi/otolucn6
•Nitroaniline
Accnapliihene
2.4-Diiiiuoplienol
4 •Nilro phenol
)ibeiizofurau
,4-Diniiroioluene
Dielhylplillialale
•Chlnroplieiiyl pheuylcttier
uorcne
4 -Njf roan Hi lie
,6-l.)iiiiuo-2-mel1iylphcnol
Valid
6
6
6
6
6
6
6
6
«
6
6
6
«
6
6
6
6
6
6
6
6
6
6
6
6
6
6
6
6
6
6
1
6
6
6
6
6
6
6
6
4
6
Occu
1
0.
1
0
0.
0
0
0
0.
0
0
0
0
0
0
0
0
0
0
0
0
1
0
0
0
0
0
0
0
0
0
0
1
0
1
0
1
0
0
0
0
0
Undtlcc
5
6
5
6
6
6
6
6
6
6
«
6
6
6
6
6
6
6
6
6
6
i
6
6
6
6
6
6
6
6
6
2
5
6
i
6
i
6
6
6
4
6
Efllinaled
1
0
' 1
0
0
0
0
0
0
0
0
0
0
0
O
0
0
O
0
0
0
1
O
O
0
O
0
0
0
0
0
0
1
0
1
0
1
0
0
0
0
0
Ittjcc
0
0
0
0
0
0
0
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
0 >
0
0
0
0
0
u
0
2
0
Frequent
Delected
0.17
0.00
0.17
0.00
0.00
11.00
,u.oo
0.00
0.00
u.oo
u.oo
0.00
o.oo
0.00
0.00
0.00
0.01)
0.00
0.00
0.00
0.00
0.17
.0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.17
0.00
0.17
0.00
0.17
0.00
0.00
0.00
0.00
. :0.00
Minimum
Coneenlrnllon
Delected
730.00
0.00
690.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
o.ou
o.oo
980.00
0.00
0.00
0.00
0.00
o.uo
0.00
0.00
0.00
0.00
0.00
680.00
o.uo
690.00
0.00
560.00
(f.00
u.uo .
0.00
0.00
0.00
Maximum
Concentration
Delected
750.00
0.00
690.00
0.00
U.OO
0.00
o.oo
0.00
0.00
0.00
0.00
u.oo
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
o.uo
980.00
o.oo-
0.00
0.00
0.00
o.oo
o.uo
0.00
0.00.
0.00
• o.oo
680.00
0.00
690.00
0.00
560.00
0.00
0.00
o.oo.
0.00
o.uo
Median
335.00
267.50
335.00
267.50
267.50
267.50
267.50
267.50
267.50
267.50
267.50
267.50
267.50
267.50
267.50
267.50
267.50
267.50
267.50
267.50
267.50
335,00
267.50
267.50
267.50
650.00
267.50
650.00
267.50
267.50
267.50
610.00'
335.00
650.00
695.00
267.50
335.00
267.50
267.50
267.50
775.00
65U.001
(icoinelrle
.-Mean
^M 7. 1586
280.7.163
312.5055
280.7463
280:7463
281). 7.163
28U. 7.163
280.7463
280.7463
280.7463
280.7463
280.7463
280.7.163
2J0.7463
2*0.7463
280.7463
280.7463
2|0.7463
2(0.7463
2(0.7463
2$0.74G3
352.5291
28*0.7463
200.7463
280.7463
61J9.I797
280.7463
67.9.1797
280.7463
28U.7463
2(J0.7.(63
648.0741
331.6974
679.1797
695.1859
200.7463
321.1357
280.7463
280. 7463
280.7463
69.5.2879
679.1797
Arllhmell
Mean
376.6667
293.3333
366.6667
293.3333
293.3333
293.3313
293.3333
293.3333
.293.3333
293.3333
293.3333
293.3333
293.3333
293.3333
293.3333
293.3333
293.3333
293.3333
293.3333
293..1333
293.3333
415.0000
293.3333
293.3333
Z93.333J
710.111)00
293.3333
710.0000
293.3333
293.3333
293.3333
650.0000
365.0000
710.0000
725.0000
293.3333
345.0000
293.3333
293.3333
293.3333
740.0000
710.0000
Standard
Deviation
204.1976
93.2559
182.5833
93.2559
93.2559
93.2559
93.2559
93.2559
93.2559
93.2559
93.2559
93.2559
93.2559
93.2559
93.2559
93.2559
93.2559
93.2559
93.2559
93.2559
93.2559
291.3074
93.2559
93.2559
93.2559
226.2742
93.2559
226.2742
93.2559
93.2559
93.2559
70.7107
179.0531
226.1742
22U.4314
93.2559
139.0683
93.2559
93.2559
93.2559
282.9605
226.2742
ineontj
5.8206
5.6375
5.8067
5.6375
5.6375
5.6375
5.6375
5.6375
5.63/5
5.6375
5.6375
5.6375
5.6375
5.6.175
5.6375
5.6375
5.6375
5.6375
5.6375
5.6375
5.6375
5.8651
5.6375
5.6375
5.6375
6.5209
5.6375
6.5209
5.6375
5.6375
5.6375
6.4740
5.81142
6.5209
6.5442
5.6375
5.7719
5.6375
5.6375
5.6375
6.5443
6.5209 '
9ldev(I
0.5083
0.3289
0.4825
0.3289
0.3289
0.3289
0.3289
0.3289
0.3289
0.3289
0.3289
0.3289
0.3289
0.3289
0.3289
0.3289
0.32S9
0.3289
0.3289
0.3289
0.3289
U.5965
U.3289
0.3289
0.3289
0.3313
0.3289
0.3313
0.3289
0.3289
0.3289
0.1090
0.4781
0.3313
0.3257
0.3289
0.4232
0.3289
U.3289
0.3289
0.4204
0.3313
n(T
6
6
6
6
6
6
6
6
6
6
6
6
6
6
6
6
6
6
6
6
6
6
6
6
6
6
6
6
6
6
6
2
6
6
6
6
6
6
6
6
4
6
l.ouer
Quit III
239.281
224.882
240.113
224.882
224.882
224.882
224.882
224.882
224.882
224.882
224.882
224.8821
224.8821
224.8821
224.8821
224.8821
224.8821
224.8821
224.8821
224.8821
224.8821
235.7326
224.8821
224.8821
224.8821
5.13.1547
124.8821
543.1547
124.8821
224.8821
224.8821
602.1253
240.2421
543.1547
158.057 1
224.8821
241.3660
24.8821
24.8821
24.8821
23.5847
43.1547
Upper
Quorllle
475.0724
35U.4880
46U.448
350.4880
3J0.4880
35U..IH81
35U.4H80
350.4880
350.4880
350.4880
350.4880
350.4880
350.4880
35U.4880
350.4880
350.4880
350.4880
350.4880
350.4880
350.4880
350.4880
527.1939
350.4880
350.4880
350.4880
849.2700
350.4880
849.2700
350.4880
350.4880
350.4880
697.5292
457.9680
849.2700
866.0109
350.4880
427.2687
350.4880
350.4880
350.4880
923.2990
49.2 700
Upper 95
7QI.960I
414.2380
654.2036
414.2380
414.2380
41-4.2380
41.4.2380
414.2380
414.2380
414.2380
414.2380
414.2380
414.2380
414.2380
414.2380
414.2380
4I4.238U
4I4.238U
414.2380
414.2380
414.2380
908.6905
4)4.2380
414.2380
•114.2380
UX>ii.6l59
414.2380
1006.0159
414.2380
414.2380
414.2380
1002.6683
646.4972
1006.0159
1020.4732
414.2380
559.9252
414.2380
414.2380
414.2380
622.4045
006.0159


ft








































MQIES:                                                   •   i                         .
All concentrations are given in ugAg(ppb).  '                           |
The "n" in ihe tut right column imlic»lc> that ihe 95% Upper Confidence l.unil jj gi|,ilcr Ilieli Hit maximum delccled conccniraiinn.
     race I of 2
lirilSI)SMV.XI.S

-------
                                                                     :         Table  3

                                                                     I
                                                 CHEMICAL SUMMARY STATISTICS FOR SEDIMENT • SI£M1-VO1,AT1I,E()R«ANICS
                                                                     ;         (JCI.TlcomlTrcnllnR.Sllc

Compound
N-NitroiodiphenyUmino
4-Dromoplioiyl plienylelha
leiachlotoboiiMno
Pentachlotophcnol
Phenanthrene
Anthracene
Caibazole
X-n-buiylpliilialalo
Fhioranihent
Pyiene
lutylbenzylplilhatalo
3.?-Dielilorobenzidin<>
enzolalanthracene
Chiyiene
biill-Bihylhexyllplilhataio
>i-n-octylp1itbable<
lenzotbJUuorHillieno
enzolkltluorontheno
cnzo[a]pyrene
lndeno[l,2,3-cd|pyrene
>ibenzota,hJuithraceDe
leiizo(K,li,iJperyleno

Valid
6
6
6
6
6
6
6
6
6
6
6
6
6
6
6
6
6
6
6
6
6
6

Occur
0
0.
0
|i
0
1
0
0.
3
3.
0.
0
3
4:
1:
0
•3
2
3
1
0
2

Undelec
6
6
6
5
6
5
6
6
3
1
6
6
3
2
5
6
3
4
3
5
6
4

Estimated
0
0
' 0
1
0
1
0
0
3
4
0
0
3
3
1
0
3
2
2
1
0
2

Rejec
0
0
0
0
0
0
0;
0
0
0
0
0
0
0
0:
0
0
0
0
0
0
0

Delected
0.00
0.00
0.00
0.17
0.00
0.17
0.00
0.00
0.50
0.83
0.00
0.00
• 0.50
0.67
0.17
0.00
0.50
0.33
•0.50
•0.17
•0.00
0.33
• Minimum
Delected
0.00
0.00
0.00
1000.00
0.00
1200.00
0.00
0.00
770.00
620.00
0.00
' 0.00
540.00
510.00
1200.00
0.00
1100.00
1700.00
540.00
1100.00
0.00
750.00
Maximum
Detected
0.00
0.00
0.00
1000.00
0.00
1200.00
O.OO
o.oo •
2600.00
3000.00
0.00
0.00
2200.00
4000.00
• 1200.00
O.OO
4)00.00
3100.00 .
1700.00
1100.00
0.00
850.00 '

Median
267.50
267.50
267.50
825.00
267.50
267.50
267.50
267.50
51 O.OO
1215.00
267.50
267.50
395.00
855.00
392.50
267.50
692.50
267.50
480.00
317.50
267.50
335.00

Mean
280.7463
280.7463
280.7463
739.5362
280.7463
339.3132
280.7463
280.7463
604.7652
9*79.2567
280.7463
280.746)
516.1651
7-76.0742
424.6479
$0.7463
690.95M8
501.7616
473.756)
351.6187
280.7463
376.4232

Mean
: 293.3333
293.3333
. 293:3333
776.6667
293.3333
429.1667
293.3333
293.3333
1056.6667
1386.6667
293.3333
293.3333
818.333)
1)71.6667
525.833)
29).3333
13)4.1667
939.1667
628.3333
419.1667
293.3333
448.3)))

Deviation
93.2559
93.2559
93.2559
245.4927
93.2559
386.3731
93.2559
93.2559
1104.3128
1052.1533
93.2559
93.2559
838.7471
1477.3411
385.8810
93.2559
1600.1638
1201.2594
557.9755
341.5906
93.1559
286.1060

m«.n(,)
5.6375
5.6375
5.6375
6,6060
5.6375
5.8269
5.6375
5.6375
6.40-18
6.8868
5.6375
5.6375
6.2466
6.6542
6.051)
5.6375
6.5381
6.2181
6.1607
5.8625
5.6375
5.9)07

"««1»
0.3289
0.3289
0.3289
0.3576
0,3289
0.6835
0.3289
0.3289
1.1951
1.0372
0.3289
0.3289
1.0513
1.2357
0.7134
0.3289
1.2935
1.2056
0.8080
0.6483
0.3289
0.6508

„(,
6
6
6
6
6
6
6
6
6
6
6
6
6
6
6
6
«
6
6
6
6
6

ijjiariiie
224.8821
224.8821
224.8821
580.9962
224.8821
213.9610
224.8821
224.8821
270.0388
486.4041
224,8821
224.8821-
253.9948
337.1380
262.4272
224.8821
288.7102
222.4612
274.6630
227.0486
224.8821
242.6594

Quartlie
350.4880
350.4880
350.4880
941.3381
350.4880
538.1023
350.4880
350.4R80
1354.4014
1971.4956
350.4880
350.4880
1049.3507
1786.3768
687.1460
350.4880
1653.8165
1131,7240
817.1653
544.5340
350.4800
583.9231

Upper 9S
414.1380 x
414.1380 x
414.1)80 »
1 144.5449 x
414.2380 I
1113.9161
414.1380 x
414.2)80 <
160)8.0704 x
12054.7707 x
414.2380 X
414.2380 x
6777.7014 x
235-28.6109 x
1516.2698 x
414.2380 i
31261,2924 x
14059.6839 x
232J.7585 x
1042.7293
414.2380 x
1 124.1 168 x
: All concentriiloni are given III ugAg(ppb),                        •
.^Tllfi "x" In d)6 far figJU column indicate} that Uio 95% Upper Confidence l,ilnll is greater then lire maximum delected concentrallon.
     P«ge2 o(2
UHISDSMV.XLS

-------
                                                                                  Table  3
                                                         CIIICM1CAL SUMMAIIV STATISTICS FOR SKIMMtiNT
                                                                                 CCI, Tic mid TrcnlliiR.Site
I'GSTICIDKS
Compognd
atpha-DIIC
bel>-nilC
ddla-nilC
ganina-BIIC
llepladilor
Alclrtn
lleptnclilorcpoxlde
GndosuKan 1
Dleldrln
DOG
Undrln
Endoculfan II
ODD
nndosufftut autfale
DDT
Melltbxycldor
llndrlh ketune
Endrih aldehyde
alplta-Chlordiinc
gairana-Qilordane
Touplicne
Aiocloi-1010
Aioclor-1221
Aroclor-1232
Aioclor-1242
Aroclor-1248
.roclor-1254
Arocloi-1260
Valid
5
5
5
5
S
4
5
]
4
5 .
5
5
5
5
4
2
3
5
5
4
5
5
5
5
5
5
5
5
Occur
0
0
0
0
0
2
0
0
0
2
0
4
0
0
1
0
0
0
0
1
0
0
0
0
0
1
0
0
Undtlicl
5
s
s
s
5
Z
5
5 .
4
3
5
1
J
J
3
2
. J
5
5
3
S
S
5
5
S
4
S
5
Estimated
0
0
0
0
0
2
0
0
0
2
0
4
0
0
1
0
0 .
0
0
1
0
0
0
0
0
1
0
0
Reject
1
1
1
1
1
2
1
1
2
1
1
1
1
1
2
4
1
1
• 1
2
1
1
1
1
1
1
1
1
frequency
Delected
. 0.00
0.00
p.oo
0.00
0.00
0.50
0.01).
0.00
0.00
0.40
0.00
0.80
0.00
. 0.00
0.25 .
o.oo
O.QQ .
0.00
Q.oq .
0.25
o,oq :
o.oo1
o.op :
o;op: ;
0.00
0.20
o.oo
0.00
Minimum
Concentration
Detected
0.00
0.00
0.00
0.00
0.00
0.67
0.00
0.00
0.00
2;50
0.00
0.22
0.00
0.00
1.00
0.00
o.oo
0.00
0.00
0.^6 ..
0.00
0.00
0.00
0,00
0.00
90.00
0.00
0.00
Maximum
Concentration
Delected
0.00
0.00
0.00
0.00 .
0.00
O.S2
0.00
0.00
0.00
• 3.80
0.00
6.60
0.00
0.00
1.00
0.00
0.00
0.00
0.00
0.76
0.00
0.00
0.00
0.00
0.00
90.00
.0.00
.0.00
Median
1.30
1.30
1.30
.1.30
1.30
1.06
1.30
1.30
2.55
2.55
2.55
1.50
2.55
2.55
7.85
59.00
2.55
2.55
1.30
4.18
130.00
25.50
50.00,
25.50
25.50
90.00
25.50
25.50
Geometric
Mean
2.5746
2.57.46
2.57-16
2.5746
2.57-16
I.654R
2.5746
2.57-16
3.8799
3.5659
5.0151
2.1187
5.0151
5.0151
4.6998
36.9439
5.0151
5.0l4l
2.57-
2.67(
6
7
257.4<{09
50.15)3
I00.fr
5,0.15
50.15
00
3
3
64.539,1
50.1513
50.151)
Arithmetic
mean
4.2900
4.2900
4.2900
4.2900
4.2900
3.3225
4.2900
4.2900
6.8250
4.9100
8.2600
4.7440
8.2600
8. 2600
9.3000
59.0000
8.2600
8.2600
4.2900 :.
4.9025
429.0000
82.COOO
167,9000
82.6000
82.6000
95.5000
82.600(1
82.6000
Standard
Deviation
4.4323
4.4323
4.4323
4.4323
4.4323
4.7925
4.4323
4.4323
9.1255
5.1367
8.5295
5.7291
8.5295
8.5295
9.5600
65.0538
8.5295
8.5295
4.4323
4.8875
443.2324
85.2946
175.2592
85.2946
85.2946
79.1565
85.2946
85.2946
incin(j)
0.9-157
0.9457
0.9457
0.9457
0.9-157
0.5037
0.9457
0.9-157
1.3558
1.2714
1.6125
0.7508
1.6125
1.6125
1.5475
3.6095
1.6125
1.6125
0.9-157
0.9823
5.5509
3.9150
4.6115
3.9150
3.9150
4.1673
3.9150
3.9150
sldev(j)
1.1490
1.1490
1.1490
I.L490
1.1490
1.2626
1.1490
1.1490
1.1261
0.8158
1.1315
1.6029
1.1315
1.1315
1.5044
1.4772
1.1315
1.1315
1.1490
1.3941
1.1490
1.1315
1.1456
1.1315
1.1315
1.0826
1.1315
1.1315
n(T
5
5
5
5
5
4
5
5
4
5
5
5
5
5
4
2
5
5
5
4
5
5
5
5
5
5
5
5
Lower
Quirllle
.1859
.1859
.1859
.1859
.1859
.7060
.1859
.1859
.8150
2.0566
2.3374
0.7185
2.3374
2.3374
1.7033
13.6381
2.3374
2.3374
1.1859
1.0427
118.5873
23.3741
46.4628
23.3741
23.3741
31.0900
23.3741
23.3741
Upper
Quarllle
5.5896
5.5896
5.5896
5.5896
5.5896
3.8789
5.5896
5.5896
8.2941
6.1828
10.7604
6.2-178
10.760-1
10.7604
12.9683
1(10.0872
I0.76W
10.760-1
5.5896
6.8407
558.96-18
I07.6IHJ
217.9897
107.60-13
107.60-13
133.9752
107.60-13
107.6043
Upper 9S
121.1389 *
121.1389 x
121.1389 x
121.1389 x
121.1319 • x
1611.4639 x
121.1389 x
121.1389 x
941.5504 x
26.7700 x
210.9570 x
33jK>.3699 X
210.9570 x
210.9570 x
79*37.1645 x
2.62IU28 x
21.0.9570 x
210.9570 x
121.1389 i
11522.8303 x
12113.8857 i
2109.5705 >
463,1.4394 x
2109.5705 x
2109.5705 x
2003.2465 x
2109.5705 X
2109.5705 x
MU1ES:                                                    ['•'
Concentrations tie given In units of ug/lcg (ppb).                       :   .
Tito "x" In the far right column ItuScalea dial die 95% Upper Confidence Limit is greater then die maximum detected concentration.
                                                          Page I nfI
                                                      uinsi)i«;r.xi.s

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                                                                                   Table  3
                                                               CIIICMICAI, SUMMARY STATISTICS 1'OH SEDIMENT -  MICTALS
                                                                         !           GCL Tie niidTrcalliiK Site
Mclil Analflei
Aluminim
Anliinoliy
/Vracnic
Uitium
[kiyllium
lUianiuni
Calcium
Quomium
Cobalt
Copper
ion
tied
Migneiium
Minjinesc
Mercury
Nickel
'olusluni
Selenium
Sll«r
Sodium
hillhiin
Vinidium
Ziic
Valid
6
6
6
6
6
6
6
6
fi
6
6
6
6
6
6
6
6
6
6
6
6
6
«
Occur
6
0
6
6
0
0
6
6
«
«
6
6
6
6
2.
6
6
0
0
6
0
6
6
Undelcc
0
6
0
0
«
6
' 0
0
0
0
0
0
0
0
4
0
.0
6
6.
0
6
0
0
Billmiled
1
0
1
1
0
0
6
1
I
6
|
6
1
|
0
|
1
0
0
. 1
0
1
G
Rejec
' 0
0
0
0
0
0
0
0
0
0
0
0
0 •
D
0
0
0
0
0
0
0
0
0
Fieqiitncj
Delected
1.00 .
0.00
1.00
1.00
0.00
o.on
1.00
1.00
1.00
1.00
1.00
1.00
1.00
1.00
0.3.3
i.oo •
1.00 '
0.00
0.00
1.00
0.00
1.00,
1.00
Minimum
Concentration
Delected
10700.00
0.00
7.00'
45.70
0.00.
0.00
t 2280.00
15.00
7.JO
21.90
15600.00
22.80
2560.00
310.00
0.47 .
14.40
801X10
0.00
0.00
. J7S.OO
0.00 :
15.901
63.00:
Maximum
Concentration
Delected
27800.00
0.00
16.40
127.00
0.00
0.00
13600.00
32.00
16.40
51.90
40)00.00
70.20
6160.00
547.00
0.69
43.60
4480.00
0.00
0.00
002.00 .
0.00
38.90
173.00
Median
14550.00
6.68
8.25
88.70
0.37
0.58
2915.00
19.90
8.60
30.0S
23700.00
28.45
3480.00
391.50
0.12
24.40
1220.00
3.70
1.10
519.50
0.58
I9.5S
150.00
ticomvlrlc
Mean
15J6I.80IO
6.6104
9.0957
85.4538
0.3671
0.5565
3621.1085
21.0698
10.0354
31.8510
2)772.1423
34.3205
3638.1499 '•
392.0690 .
0.1686, 1
24.5810 *
1468.6617 '
3.6666 '
1.09-14 '
539.I2H
0.5565
21.8569 '
118.5629
Afllhmcllc
r.ie»n
16133.333)
6.7917
9.5000
89.483)
0.)775
0.5708
4600.000(1
21.7500
10.5167
33.1667
24916.6667
37.30W
3820.0000
399.1667
0.2567
26.3000
1755.1667
3.7667
1.1250
562.1667 .
0.5708
22.983)
128.7000
Standard
!kv!;!fc =
6071.1339
1.7571
3.4653
27.3744
0.0989
0.1400
4.122.0)12
6.1899
3.7064
10.7925
8696.7618
18.6845
1363.7008
85.3075
0.2609
10.6733
1366.7510
0.9714
0.2962
188.1)55
0.1400
; 8.6456
50.7998
RscanCy]
9.6396
1.8886
2.2078
4.4480
• 1.0018
.0.5861
8.1945
3.0478
2.3061
3.4611
10.076)
3.5357
8,1992
5.9714
•1.7802
3.2020
7.2921
1:2993
0.0902
6.2899
•0.5861
3.0845
4.7754
S!der(£
0.)282
0.25-12
O.)0)7
0.3491
0.2565
0.2-192
0.6519
0.2724
O.J2&I
(1.3058
U.JJIO
0.4-125
0.3355
0.2CM8
0.9791
0.4029
0.59S4
0.2537
0.2554
O.)09)
0.2-192
0.3)38
0.4686
n(f
6
6
6
6
6
6
6
6
6
6
6
6
6
6
6
6
6
6
6
6
.6
6
6
l>ower
Quirlile
12310.4910
5.5688
7.4105
67.5232
0.3089
0.470-1
2319.9844
17.532)
8.0519
25.9139
19013.9081
23.4622
2901.1194
341.4780
0.0871
18.7)01
980.8)96
3.0899
0.9212
437.5900
0.4704
17.4489
86.4244
Upper
Ouirllle.
19169 A 166
7.8469
II. 16-1)
108.1458
0.4)66
0.6584
5651.9-161
25.3211
12.5074
)9.H82
29721.1254
.46.2607
4562.4233
450.1551
0.3264
)2.2596
2199.1029
4.)5IO
1.3002
664.2M5
0,6584
27.3784
162.6327
Upper IS
22642.1657
8.7175 »
12.8992
l)0.)507 \
0.4859 *
0.7288 x
1 1098.5257
28.5169
14.7482
4SJII7
35199.3125
62.1498
5426,6068
484.1015
1.6087 I
41.2402
)804;'15I8
4.8)20 >
1.4458 >
771.1589
0,7288 x
32.5114
226.4990 «
 Concentnllojuare(!ven[Inmgftn(ppm).                            '   .  .
IllK "»" in the fir right column Indicate! Dial lire 95% Upper Confidence l.imil a (tealer HKII UK Minimum dclecleil cnncenlrilion.
rue I ol I

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                                                                             !      Table  4               .'••'_

                                                   CHEMICAL SUMMARY STATISTICS FOU GHOUNDWATEIl  -  VOLATILE OIUiANICS
                                                                                      (ALL SAMPLES]
                                                                  '                (JCL Tie onrtTreallnj! Site
Compound
ChloroinelhaiK
[IfuinomelliaiK
Viiiyldiluide
ridufoclltane
Melliyleu: cliloiidc
Acetone
CM ton disutfide
1.1-DidilocoeUicne
1,1-Dichloroelhane
cil-l.2-DidiloioeUiene
Irani- 1,2-Diclilofoelliciw
Clilorofoiiii
l.2-l>idiloioetlitne
Mlutanone
l.l.l-TiicMo.oeiluiK
Ctilxmlttiachloride
BfOinodichloromctlline
l.2-niclilnio|i[ opine
cia- l.3-Dicldoropiu|>ene
TrKldoroelhenc
Dibromocliloroinelhane
1,1.2-Trichloioediane
1,2-DibroitKiliKdianc
lenzcne
uilu- 1,3-DicliloropropeiK
Droiiioform
4-Meiliyl-2-[xmaiioiie
2-llcxanoiic
Teli achloroellic ne
Dioinodiloroincdiane
1,1,2.2-Tctiacliloioeiliane
Toluene
CliKiiobeiuene •
Utliylbeiuelte
Siyiene
Xylenci
1.2-Diclilorobciuci*
1.3-Oiclilorobeiueiie
1.4- Diditorolieiuclie
l,2-nibromo-3-chloro|>(optne
V.lld
•10
40
10
40
40
16
40
4Q
40
40
40
40
40
2
40
40
40
40
40
40
40
40
40
40
40
40
37
21
40
40
40
40
40
40
40
40
40
40
40
n
Occur
I
0
IS
i
3
6
0
13
20
24
6
II
4
I
IJ
2
0
1
0
18
0
5
0
g
0
0
7
0
3
0
0
9
2
12
4
10
7
0
0
0
Mndclvcl
39
40
25
35
37
10
40
27
20
16
34
29
36
0
27
38
40
39
40
22
40
55
40
32
40
40
30
21
37
40
40
31
38
28
36
30
33
40
40
22
L'lllmaled
1
0
8
1
1
6
0
i
10
12
3
8
0
2
6
0
0
1
0
8
0
1
0
1
0
0
i
0
1
0
0
6
2
4
1
3
4
0
0
0
Hejec
0
0'
0
0
0
24
0
0
0
0
0
0
0
38
0
0
0
0
0
0
0
0
0
0
0
0
3
19
0
0
0
0
0
0
0
0
0
0
0
18
I'reijm-iicjr
Delected
0.03.
0.00
0.38
0.13
0.08
0.38
n.oo
0.33
0.50
0.60
0.15
O.J8
(|.IO
\,.m
Q.33
0.05
n.oo
0.03
p.oo
0.45
0.00
0,13
0.00
0.20
0.00
0.00
0.19
0.00
0.08
0.00
0.00
0.23
0.05
0.30
0.10
0.25
0.18
0.00
0.00
0.00 •
Minimum
t'oiM.-1-nlrallon
Delected
0.80
0.00
0.10
2.110
8.00
3.00
0.00
0.20
10.00
0.02
0.20
0.20
1-1.0(1
6.00
0.60
2.00
000
0.20
0.00
0.60
0.00
0.30
0.00
2.00
0.00
0.00
0.60
0.00
O.SI)
11.00
0.00
2.00
0.70
0.20
11.00
Q.50
U.)0
n.oo
0.00
0.00
Mtilmuin
Concenlrallon
Delected
0.80
0.00
4700.00
19.00
25.00.
8000.00
0.00
17.00
1200.00
4)00.00
5.00
110.00
23.00
520.00
200.00
7.00
0.00
0.20
0.00
1000.00
0.00
6.00
0.00
220.00
0.00
0.00
18.00
0.00
1.00
0.00
0.00
180.00
0.70
580.00
130.00
2200.00
1200.00
0.00
0.00
0.00
Median
O.SO
0.50
O.SO
0.50
2.00
3.50
O.SO
0.65
12.75
17.50
0.50
0.50
2.00
263.00
0.75
0.50
O.SO
0.50
O.SO
3.00
O.SO
•0.50
O.SO
0.50
0.50
O.SO
2.50
2.50
0.50
O.SO
O.SO
O.SO :
O.SO
O.SO .
o.so
0,50
0.50
o.so
0.30
0.50
(leolltHlrlc
Mean
1.2016
1.1876
6.8336
1.61 -19
4.S692
9.0737
1.1876
2.2170
7.8663
11.7593
1.7128
I.BI30
3.J24-I
55.8S7P
3.3)8<[
1.3131
1.1876,
I.IGIII
1.1876,
4.93)4
1.1871!
I.447IT
1.1876;
3.4339
1.1876
1.1876
6.021)9
3.32S4
1.229-1
1.1876
1.1876
2.4497
1.2077
2.34-H
1.557-1
2.9841
1.8020
1.1876
1.1876
0.6565'
Arlllunellc
Mean
7.09SO
7.0875
391.7900
8.075(1
S6.062S
909.5938
7.0875
9.0500
111.7250
397.4198
11.0500
12.0750
9.7750
263.0000
24.8875
7.2875
7.0875
7-1180(1
7.0875
60.5650
7.0875
7.4575
7.0875
21.7875
7.0875
7.0875
34.6297
7.023H
7.1125
7.0875
7.087S
16.5125
7.0975
33.3375
12.1750
97.4000
48.8925
7.0875
7.0875
1.3636
Standard
Deviation
15.8382
15.8413
I09S.SSSI
15.8007
145.4642
2490.1469
15.8413
15.5539
277.8728
834.8435
22.3390
23.S66I
15.5819
363.4529
46.5880
15.7907
15.8413
I5.H446
15.8413
174.9370
15.8413
15.7281
15.8413
52.2861
15.8413
15.8413-
79.9957
14.2876
15.8310
15.8413
15.8413
33.3094
IS.837I
103.6189
27.2834
356.2928
194.2211
15.8413
15.8413
2.7953
meaiifj
0.1836
0.1719
1.9291
0.4793
I.SI93
2.2054
0.1719
0.7961
2.0626
2.4646
0.5381
0.59SO
1.2013
4.0228
1.2056
0.2725
0.1719
0.1490
0.1719
1.5957
0.1719
0.3700
0.1719
0.8895
0.1719
0.1719
1.7952
1.2016
0.2066
0.1719
0.1719
0.8959
0.1887
0:8520
0.4430
1.0933-
0.5989
0.1719
0.1719
•0.4208
ildovlj
I.635S
1.6102
3.2245
1.7117
2.0746
2.6361
1.6402
1.7580
2.6508
3.4673
1.8661
1.9783
I.4U29
3.1552
2.2174
1.6520
1.6-102
I.65H9
1.6402
2.3-184
1.6402
1.6636
1.6-102
2.0379
1.6-102
1.6402
1.6755
0.9011
1.6285
1.6-102
1.6402
2.0323
1.6328
2.2561
1.9029
2.6083
2.2635
1.6402
1.6402
0.8815
n(r
40
40
40
40
40
16
40
40
40
40
40
40
40
2
40
40
40
40
40
40
40
40
40
40
40
40
37
21
40
40
40
40
40
40
40
40
40
40
40
22
Ijnwer
Qiiarllle
0.3986
0.3927
0.7817
0.5089
1.1271
1.5325
0.3927
0.6771
1.3154
1.1336
0.4864
0.4773
1.2224
6.6-166
0.7480
0.4308
0.3927
0.3790
0.3927
1.0113
0.3927
0.4713
0.3927
0.6154
0.3927
0.3927
1.9-141
1.8106
0.4098
0.3927
0.3927
0.6218
0.4014
0.5117
0.4314
O.SI35
0.3913
0.3927
0.3927
0.3622
Upper
Quirlllo
3.6222
3.5912
60.6178
5.1251
18.5224
53.7258
3.5912
7.2587
47.0-101
121.9857
6.0323
6.8873
9.IM09
469.4098
14.9048
4.0032
3.5912
3.5544
3.5912
24.0480
3.5912
4.4477
3.5912
9.6254
3.5912
3.5912
18.6464
6.1076
3.6887
3.5912
3.5912
9.6SI3
3.6338
10.7413
5.6228
17.3403
8.2979
3.5912
3.5912
1.1899
Upper 95
10.3188 x
10.3174 x
20128.9616 i
16.8239
134.5584 «
63752.4643 x
10.3174, x
26.0795 x
1809.0187 i
1 17126.1930 x
27.0999 x
39.7522
19.900-1
4.I6BH24 x
1 56.2246
1 1. 7509 x
I0.3I74- x
IO.S656 <
I0.3I74 x
362.3978
10.3174 x
13.3361 X
10.3174 x
63.9591
10.3174 x
10.3174 x
60.2417 x
8.1490 l
10.3774 x
10.3174 i
10.3174 x
63.2741
10.3007 x
124.9673
27.3674
579.6993
98.5379
10.3174 x
10.3174 x
1.5338 x
HUD'S:
Cuicciitiaiium aic given in unili uf ug/l. (1'lib).                              •
Tlie "x"-in the lai litlil column indicate) lint the 95ft ll|i|Ki Confidence Limit U greiler Ilian ilic mitiimmi deiericil ciiiiivnttiiiini.
irriKiWVI.AJfl.S

-------
                                                                                    Table   4
                                                 CHKMICAI.SIJMMjAKY STATISTICS FOR GllOUNDWATKIl
                                                                   .  :                   IAI.LSAMPI.liSI
                                                                     1               CtXTie nnd Trailing Site
                                        SEMI-VOLATILE OIICANICS
•
Con^nC
riitnoi
bii|2-Cliloioeiliyl|ciliei
2-Cliloiupheiiol
2-Meibylpliciiol
2,2'*oxybii-l-Clilofopropaue
4-Mclliylphenol
^•Nitroiodt-ii-iroirylamine
lexBcbluiuelliano
"liuobeiuene
iopliorune
l-Nilrni>lieiml
!,4-Diinelbylplienol
>i3(2*Qilorocl)ioxy|inelhaiie
2,4-niclilorophcnol
,2.4-Tricliloroben/eue
lapliihalene
•Clilofoanihiio
lexaclilorobutadicne
-ChloiO'3-inelbyt|4icaol
-Methylnaplnliklene
cxaclilofvcyclopcntatlieii*
,4,6-Tricbloroplicnol
2,4,5-THcliloropbcnol
-Cbloronapbtbalcno
2-Niiromilino
>tinediylphtlialale
Acciiaplifliylcno
,6-Diniuofi)ltie!ie
-Nilfoaniljiio
Acenaplillieno
,4-Duiiuoplicnol
-Niuo]ilieiiul
beiizofuran
,4-DuiiUololueno
ielliylpliltioblo
4-Cblofophenyl pbeuylelher
Fluoieno
4-Niirowiliin
4.6-Dinhio-2-ineiliylplicnol
N-Nllroiodipuciiylaniino
4-Ilioiiioplieuyl nlieiiylcllin
lleiichlaiobeiueiio

Vsl!
39
39
39
39
39
39
39
39
39
39
39
39
39
39
39
39
39
39
39
39
39
39
39
39
39
39
39
39
39
39
39
39
39
39
39
39
39
39
.9
39
39
39

Oeeu
7
0
0
a
p
s
0
0
0
0
0
]
0
0
0
12
0
0
0
7
0
0
o
0
0
0
7
0
0
7
0
0
7
0
1
0
7
0
0
0
0
0

Undcler
31
39
39
36
39
34
39
39
39
39
39
38
39
39
39
27
39
39
39
32
39
39
39
39
39
39
32
39
39
32
39
39
32
39
38
39
32
39
39
39
39
)•>

Billm.it
5
0
0
3
0
3
0
0
0
0
0
I
0
0
0
5
0
0
0
6
0
0
0
0
0
0
0
0
0
4
0
0
2
0
I
0
4 ,
0 '
0
0
0
0

Ittler
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0

Delected
0.18
O.UO
(1.1(0
0.09
0.00
0.13
0.00
0.00
0.00
0.00
' 0.00
0.03
0.00
0.0(1
o.oo
0.31
o.oo
o.oo
0.00
0.18
0.00
0.0(1
0.00
0.00
0.00
0.00
0.18
0.00
. 0.00
0.18
O.Oil
0.00
0.18
0.00
0.03
0.00
0.18
0.00
o.ob
0.110
0.00
0.00
Minimum
Delected
1.00
0.00 .
o.oo
0.70
O.OO
1.00
0.00
.0.00
0.00
0.00
0.00
'4.00
0.00
O.flll
0.00
0.60
0.00
0.00
•0.00
92.00
:o.oo
O.IK)
•0.00
0.00
0.00
0.00
8.00
0.00
o.oo
25.00
0.00
n.oo
35.00
0.00
0.80
n.oo
2.00
0.00
0.00
0.00
0.00
0.00
Minimum
Delected
42.00
o.oo
n.oo
3.00
0.00
26.00
0.00
0.00
o.oo
0.00
o.oo
4.00
0.00
• o.oo
0.00
12000.00
0.00
0.00
0.00
1400.00
0.00
0.00
0.00
0.00
o.ou
o.oo
25.00
0.00
0.00
310.00
0.00
0.00
180.00
0.00 .
0.80
0.00
140.00
0.00
o.oo
0.00
o.oo
n.oo

Media
2.50
2.50
2.50
2.50
2.50
2.50
2.50
2.50
2.50
2.50
2.50
2.50
2.50
J.50
2.50
2.50
2.50
2.30
2.50
2.50
2.50
2.50
IO.IX)
2.50
10.00
2.50
2.50
2.50
10.00
2.50
io.no
10.00
2.50
2.30
2.50
2.50
2.50
10.00
10.00
2.50
2.50
2.50

Me/in
2.8027
2.5117
2.51.17
2.45,39
.2.51,17
2.6-192
2.51.17
2.5117
2.5117
2.5117
2.5117
2.5-122
2.5117
2.5117
2.5117
7.8505 '
2.5117
2.5117
2.5117
5.5709
2.5117
2.5M7
IO.IM69
2.5117
IO.IU69
2.SII7
3.4134
2.5117
10.IM69
4.6357
IO.IH69
IU.0-169
-1. 5.116
2:5117
2.4394
2.5117
3.5043
10.0-169
10.0169
2.5117
2.5117
J.SII7

Mean
4.1667
2.5128
2.5128
2.4923
2.5128
3.3462
2.5128
2.5128
2.5128
2.5128
2.5128
2.5513
2.5128
2.5128
2.5128
806.9718
2.5128
2.5118
2.5128
72.6282
2.5128
2.5128
10.0513
2.5128
10.0513
2.5128
4.7564
2.5128
10.0513
23.0385
10.0513
10.0513
16.3974
2.5128
2.4692
2.5128
11.5256.
10.0513
10.0513
2.5128
2.5128
3.5118

Devlnllon
7.5353
0.0801
0.0801
0.3239
0.0801
4.2475
0.0801
0.0801
0.0801
0.0801
0.0801
0.2512
0.0801
0.0801
0.0801
2379.4252
0.0801
0.0801
- 0.0801
253.5510
0.0801
0.0801
0.3203
0.0801
0.3203
0.0801
5.5142
0.0801
0.3203
63:8486
0.3203
0.3203
36.9265
0.0801
0.2858
0.0801
31.5056
0.3203
0.3203
0.0801
0.0X01
0.11801

meant;
1.031)6
0.9210
0.9210
0.8977
0.9210
0.9742
0.9210
0.9210
0.9210
0.9210
0.9210
0.9330
0.9210
0.9210
0.9210
2.0606
0.9110
0.9210
0.9210
1.7176
0.9210
0.9210
2.3073
0.9210
2.3073
0.9210
1.2277
0.9210
2.3073
1.5338
2.3073
2.3073
1.5133
0.9210
0.8917
0.9210
1.2540
2.3073
2.3073
0.9210
0.9210
0.9210

)ldet(/
0.6177
0.0292
0.1)292
0.2119
0.0292
0.5213
0.0292
0.0292
0.0292
0.0292
0.0292
0.0800
0.0292
0.0292
0.0292
2.9149
0.0292
0.0192
0.0291
1.7795
0.0191
0.0292
0.0292
0.0292
0.0292
0.0292
0.685-1
0.0292
0.0292
1.3843
0.0292
0.0292
1.3024
0.0292
0.1855
0.0292
1.0746
1.0292
0.0292
0.0292
1.0292
U.II292

n(r
39
39
39
39
39
39
39
39
39
39
39
39
39
39
39
39
39
39
39
19
59
39
39
39
39
39
39
39
39
39
39
39
39
39
39
39
39
39
39
39
39
39

Quorlll
1.8475
2.4627
2.4627
2.1270
2.4627
1.8637
2.4627
2.4627
2.4627
1.4627
2.4627
2.4086
2.4627
2.4627
2.4627
1.0986
2.4627
2.4627
2.4627
1.6770
2.4617
2.4617
9.8509
2.4627
9.8509
2.4627
2.1496
2.4627
9.8509
1.8219
9.8509
9.8509
1.8863
2.4627
2.1524
2.4627
1.6972
9.8509
9.8509
2.4627
2.4627
2.4627


4.2515
J.56I7
2.5617
2.8311
2.5617
3.7657
2.5617
2.5617
2.5617
2.5617
2.5617
2.6832
2.5617
2.5617
2.5617
56.1014
2.5617
2.5617
2.5617
18.5064
2.5617
2.5617
10.1467
2.5617
10.2467
2.5617
5.4203
2.5617
10.2467
11.7956
10.2467
10.2467
10.9346
2.5617
2.7647
2.5617
7.2357
10.2467
10.2467
2.5617
2.5617
2.5617

Upper 95
4.1361
2.5327 x
2.5327 x
2.6635
2.5327 x
3.5657
2.5317- »
2.5327 x
2.5317 x
2.5327 i
2.5327 n
2.6066
1.5327 x
2.5327 i
2.5327 x
5730.3856
2.5327 x
2.5327 x
2.5327 x
70.6635
2.5327 i
2.5317- »
10.1310 x
2.5327 x
10.1310 x
2.5327 x
5.4144
2.5327 x
10.1310 x
22.6367
10.1310 x
10.1310 X
18.7338
2.5327 x
2.6136 x
2.5327 x
9.5293
10.1310 x
10.1310 x
2.5327 x
2.5327
2.5327 .
C-'mieeiiiiaiioiii are given in ug/1. (|vM.  •                                   .
Tlic ">" iii Clio far rijjlil column inilicalei llial Ihc95% Upper Culllulciicc l.iinil is greulcl llitu Ilia ll
iniimi itcletlcil lonccii.riiiidi).
                                                                                                           l'*ee I ol 2
                                                                                                      UTIKiW.SVA.XLS

-------
                                                                           Table  4

                                           CHEMICAL SUMMARY STATISTICS I?OR GROUNDWATER • SEMI-VOLATILE ORGANICS
                                                                              [ALL SAMPLES)
                                                                          GCL Tie and Treating Site
Compound
Peuuchloiophenol
PheuAMhreno
Aniliricene-
Di-n-buiylpliih»l«io
Fluonnlhene
Pyruw •
Butylbenzylphmilile
3,3'-Diclilorobenildine
Ocnzo(>]ullii»cene
Cliryune
bii|2-Bl>iyllieiyl)phil»ble
Di-n-oclylphlliilate
Deiuo|b|nuoi«J\(liene
Benzo|lEinuoruilhen6
BcnzoMpyrcflO
lnden6|t,2,3-cd)pyKn>
Dibenzo[ft.h)uiiliiicene
Denzo|g,h,Uperylei»
Valid
39
39
39
39
39
39
39
39
39
39
39
39
39
39
39
39
39
39
Occur
0
7
5

i
5
°i
0
1
3
5
0
1
1
1
1
0
1
Uodelecl
39 •
32
34
38
3-1
34
39
39
37
36
34
39
37
38
38
38
39
38
Kjllmiled
0
5
2
1
2
3
0
0
1
3
4
0
2
1
1
1
0
1
Reject
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
Frequency
DelecUd
0.00
0.18
0.13
0.03
0.13
0.13
0.00,
0.00
0.05
0.08
0,13
q.oo
q.os
0.03
q.03
o:o3:
0.00'
; 0.0,3-
Minimum
Concentration
Delected
0.00
2.00
0.80
0.30
0.70
0.40
0.60
0.00
2.00
0.30
0.70
0.00
0.20
2.00
2.00
0.70
0.00
0.60
Mulmum
Conccnlrillon
Delected
0.00
180.00
16.00
1.00
54.00
32.00
0.60
0.00
6.00
4.00
51.00
0.00
3.00
2.00
2.00
0.70
0.00
0.60
Medlili
10.00
2.50
2.50
2.50
2.50
2.50
2.50
2.50
• 2.50
2.50
2.50
2.50
2.50
2.50
2.50
2.50
2.50
2.50
Geometric
Mean
10.0469
3.5585
2.7439
2.4534
2.8967
2.7325
2.5117
2.5117
2.5541
2.3517
3.3364
2.5117
2.365}
2.4974
2.4974
2.43I|
2.5117
2.42IJ
Arllhmellc
Mem
10.0513
13.3205
3.1615
2.4744
4.5949
3.6385
2.5128
2.5128
2.5897
2.4564
8.3154
2.5128
2.4667
2.5000
2.5000
2.4667
2.5128 .
2.4641
Slindird
Uevldloit
0.3203
38.2965
2. 5908
0.2552
9.1268
5.2242
0.0801
0.0801
0.5721
0.5004
18.7803
0.0801
0.3889
0.1147
0.1147
0.3012
0.0801
0.3166
meon(y)
2.3073
1.2693
1.0094
0.8975
1.0636
1.0052
0.9210
0.9210
0.9377
0.8552
1.2049
0.9210
0.8609
0.9152
0.9152
0.8883
0.9210
0.8844
sldev(j)
0.0292
1.1227
0.4515
0.1504
0.6781
0.5963
0.0292
0.0292
0.1479
0.3785
1.0401
0.0292
0.4080
0.0467
0.0467
0.2067
0.0292
0.2311
"(T)
39
39
39
39
39
39
39
39
39
39
39
39
39
39
39
39
39
39
Loner
Qunrllle
9.8509
1.6684
2.0234
2.2167
1.8332
1.8275
2.4627
2.4627
2.3115
1.8218
1.6540
2.4627
1.7961
2.4199
2.4199
2.1146
2.4627
2.0718
Upper
Quarlllt
10.2467
7.5896
3.7211
2.7153
4.5770
4.0858
2.5617
2.5617
2.8221
3.0359
6.7301
2.5617
3.1148
2.5774
2.5774
2.7948
2.5617
2.8301
Upper 95
10.1310 it
10.4995
3.4817
2.5866 »
4.5575
3.9469 •
2.5327 >
2.5327 x
2.6901
2.8241
8.5728
2.5327 «
2.9019
2.5320 *
2.5320 ' »
2.6317 ' *
2.5327 * x
2.6546 i
Concenuittons uo given in ug/L (ppb).     .                            '
The ">" in lilt (« light column iiidiclla Iliil Ilio 95% Upper Confidence. Limit ii greater Mien ilio minimum drlecled concentration.
    't                                                               '
     I'ige 2 of 2
UTDOWSVAJCCS

-------
                                                                                   Table   4
                                                         CIHCMH :AI, SUMMARY STATISTICS FOR ttKOIJNDATKK - I'lCS
                                                                                        (AM. SAMI'l.luS|
                                                                                    (iCMlc nnil Trailing She

"ciiipouni!
alpln-DIIC
beta Bl 1C
delia-BlIC
gaiimia-nilC
llepuctilor
Aid; in
lleptadilorcnoxiile
pjidosulfaii I
Diel.tr in
1)1)0
Enilrln :
tndiJGulfan II
DI)I)
Utdoiulfui mlfate
DOT
ilclliujychlor
Undiln kclonc
•ndiin ildcliyde
alplu-Qifordane
gajiwna-Oilordane
Toxaphene
Aioclor-1016
Aioclor-1221
Aroctor-1232
Aioclui-1242
Aloclor-1248
Aioclor-1254
Arocloi-1260

Vs!!d
39
38
38
39
38
39
32
38
39
39
39
37
38
38
39
38
39
38
39
38
38
38
38
38
38
38
38
38

Oeee.
4
4
5
6
0
•1
8
0
8
4
7
1
2
5
1
|
1
8
7
5
0
0
0
0
0
0
0
0

Uadtice
35
34
.33
33
38
35
U
38
31
35
.32
36
36
33
38
il
38
30
32
33
38
38
38
38
38
38
38
38

!£!!h!!*!>d
4
4
5
6
0
•1
8
0
8
•1
7
1
2
5
I
1
1
8
7
5
0
0
0
0
0
0
0
0

iltjte
0
1
1
0
1
0
7
1
0
0
0
2
I
1
0
I
0
1
0
1
1
1
1
1
1
1
1
1

Delected
0.10 '
0.11
0.13
0.15
o.on
0.10
0.25
0.00
0.21
0.10
0.18
0.03 .
0.05
0.13
0.03 ,
0.03
O.OJ .
0.2l'
O.lS
D.I3
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
Minimum
Delected
0.0006
0.0021
0.0004
0.0025
O.OflOO
(1.0(11)5
0.0009
0.0000
o.oooi
0.0006
0.0100
0.0006
0.00-16
0.0008
0.0052
0.0140
0.0092
0.0016
0.0006- •
0.0005
o.oooo
o.oooo
0.0000
0.0000
0.0000
0.0000
0.0000
o.oooo
Mnxlmiiin
Dtltelfd
0.0081
0.0130
0.0028
0.0520
0.0000
0.0048
0.0390
0.0000
0.2600
0.0046
0.1800
0.0006
0.0130
0.0620
0.0052
0.0140
0.0092
0.1400
0.1200
0.0330
0.0000
o.oooo
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000

Mtdlbi
0.01
0.01
0.01
0.01
O.OI
0.01
0.01
0.01
0.01
0.01
0.01
0.01
0.01
0.01
0.01
0.05
0.01
0.01
0.01 .
0.01
0.50
0.10
0.20
0.10
0.10
o.in
o.io
0.10

Menu
0.0052
0.0060
0.0045
0.0059
0.1)1)56
. (1.11052
0.0051
0.0056
0.1)1 10
0.0096
0.0128
. 0.0105 -
0.01 II
0.0102
: O.dlll
. 0.0546
0.0112
0.0118 .
0.6059
0.0051
0.564-1 •
0.1129
0.2258
0.1129
0.1129 :
0.1129
0.1129
0.1129

niton
0.0072
0.0079
0.0069
0.0088
. 0.0074
0.1107 1
0.0073
0.0074
0.0263
0.0139
0.0185
0.0146
0.0147
0.0161
0.0145
0.0727
0.01.16
0.0182
0.0107
0.0067
0.736B
0.1474
0.29-17
0.1474
0.1474
0.1474
0.1474
0.1474

Dtvlition
0.0101
0.0102
0.0104
0.0126
0.0102
0.0101
0.0101
0.0102
0.0556
0.020-1
0.0295
0.0208
0.0204
0.0224
0.0202
0.1022
0.0201
0.0271
0.0210
0.0086
1.0183
0.2037
0.4073
0.2037
0.2037
0.2037
0.2037
0.2037

mtin(j)
-5.2591
-5.1242
-5.3979
-5.1319
-5.1771
-5.2596
-5.2874
-5.1771
-4.5114
•4.6506
-4.3615
-4.5591
•4.4975
-4.5896
. -4.5039
•19080
-4.4892
-4.4373
-5.1361
-5.274J
-0.5720
-11814
-1.4882
-11814
•11814
•2.1814
•11814
•11814

ildtv(j)
0.7086
0.5799
0.8510
0.7026
0.5211
0.6606
0.7356
0.5211
I.IH-IO
0.7853
0.6502
0.7253
0.5411
0.9434
0.5289
0.5679
0.5152
0.7813
0.8718
0.6288
0.5211
0.5211
0.5211
0.5211
0.521 1
0.5211
0.5211
0.5211

n(T)
39
38
38
39
3E
39
32
38
39
39
3»
37
38
38
39
38
.39
38
39
38
38
38
38
38
38
38
38
38

Qimlllt
0.0032
0.0040
0.0025
0.0037
0.0040
0.0033
0.0031
0.00-10
0.0049
0.0056
0.0082
0.0064
0.0077
0.0054
0.0077
0.0372
0.0079
0.0070
0.0033
0.0033
0.3971
0.0794
0.1589
0.0794
0.0794
0.0794
0.0794
0.0794

Quirllle
0.0084
0.0088
0.0080
0.0095
0.0080
0.0081
0.0083
0.0080
0.0244
0.0162
0.0198
0.0171
0.0160
0.0192
0.0158
0.0801
0.0159
0.0200
0.0106
0.0078
0.8022
0.1604
0.3209
0.1604
0.1604
0.1004
0.1604
0.160-1

Upper 95
0.0085 x
0.0085
0.0088 A
0.0096
0.0076 x
0.0080 x
0.0088
0.0076 x
0.0366
0.0171 i
0.0195
0.0175 >
0.0153 X
0.022*6
0.0150 I
0.0769 >
0.0150 x
0.0211
0.01 18
0.0077
0.7617 x
0.1523 x
0.3047 x
0.1523 x
0.1523 x
0.1523 x
0.1523 x
0.1523 x
HOIES:
Concciilraltnm aic given in (mils of ug/1. (ppb).
MIC "x" In the fai right column indicates Uial die 95% l)|>t>cr l.'unliilcncc l.lniil Is grc.iltr I hen lite minimum dciccu-il cuitcnuntlixi.
      Page I of I
U'lllliWI'rA.Xl.S

-------
                                                                             Table  4

                                                   CHEMICAL SUMMARY STATISTICS FOR GROUNUWATEK - TOTAL METALS
                                                                                 [ALL SAMPLES]
                                                                              «CL Tie and Trcnllng Site
Tolil Mini Anilflci
Atuiniiimi
Antimony
Ancoic •
Barium .
Beryllium
Cedjnium
Calcium
Qiramium
Cobill
Copper
Iron
Lted
Magneiium
Manganese
Mercury
Nickel '
Potauiuin
S«lcruum .
Silver
Sodium
Tlullhim
Vanadium
Ziic .
Valid
39
40
40
40
40
40
40
26
40
40
17
27
40
39
40
37
40
39
40
40
40
40
21
Occur
39
6
30
40
0
0
40
14
10
14
37
11
40
39
0
31
36
2
2
40
7
20
25
Modeled
0
34
. 10
0
40
40
0
12
20
26
0
15
0
> 0
40
5
4
37
38
0
33
20
3
Eillmaled
11
1
8
5
0
0
6
8
4
4
13
4
5
7
0
8
6
2
2
5
2
5
8
Reject
1
0
0
0
0
0
0
14
0
0
3
13
0
1
0
3
0
1
0
0
0
o
12
Prefriiencj
Defected
1.00
0.15
0.75
1.00
0.00
0.00
1.00
0.54
0.50
0.35
1.00
0.44. .
1.00.
1.00
0.00.
0.86
0.90
0.05
0.05
1.00
0.18
O.SO .
0.89
Minimum
Concentration
Delected
48.50
9.50
1.20
. 7.20 .
0.00
0.00
1660.00
4.30
3.30
3.10
83.20
1.20
. 312.00
1.80
0.00
3.90
564.00
1.20
4.00
3260.00
. 1.70
2.80
8.60
Mailraum
Concentration
Delected
6210.00
44.30
51.10
1080.00
0.00
0.00
113000.00
166.00
79.10
25.60
37600.00
14.90
34400.00 '
17300.00
0.00
131.00
16000.00
2.40
4.60
98100.00
2.80
28.70
1360.00
Median
368.00
10.83
3.35
84.35
0.10.
0.50
36350.00
4.30
4.00
3.00
4510.00
1.45
4775.00
338.00
0.10
14.10
1605.00
1.40
1.85
12350.00
1.00
3.50
21.70
Geometric
Mean
412.0567
10.9869
3.5632
95.3896
0.2428
0.9809
30904.7310
7.5092
6.0806
3.5843
2739.8107
2.4226
4048.2UO
385.0584
0.1000
15.1292
1757.1517
1.1322
I.97IF
11877.0684
0.969'a
4.0811
26.5146
Arithmetic
Mean
968.7615
14.9738
7.9913
171.8515
0.3863
1.2800
43969.5000
. 26.1923
. 12.6725
5.5525
8928.2676
3.7463
7376.1750
3060.9811
0.1000
17.3689
2849.2000
1.2308
1.0150
18740.0000
1.0788
6.1900
111.9393
Standard
Deviation
1388.0310
11.1625
12.5409
241.0794
0.3726
0.9084
29422.4093
47.9610
17.6005
5.7557
10979.1419
3.8303
8415.9-123
5014.7572
0.0000
31.2903
3815.8931
0.4438
0.5429
20269.9099
0.5513
6.9601
342.8202
mein(r)
6.0212
2.3967
1.2707
4.5580
• 1.4154
•0.0193
10.3387
2.0161
1.8051
1.2766
7.9156
0.8848
8.3060
5.9534
•2.3026
2.7166
7.4715
0.1241
0.6788
9.4632
•0.0307
1.4066
3.2777
lldcv(j)
1.3433
0.8226
1.2508
1.0798
0.9825
0.7438
1.0351
I.SI24
1.1953
0.9091
1.9096
0.9228
1.2690
2.5593
0.0000
1.1463
0.8996
0.4543
0.1877
0.8382
0.4536
0.8621
1.3855
n(j)
39
40
40
. 40
40
40
40
26
40
40
37
27
40
39
40
37
40
39
40
40
40
40
28
l/mer
Quirllle
166.4818
6.3072
1.5313
46.0369
0.1151
0.5938
15371.3190
2.7068
1.7147
1.9410
755.4566
1.2999
1719.6593
68.4932
0.1000
6.9813
957.7164
0.8333
1.7371
7315.0641
0.7141
2.2818
10.4120
Upper
Quirllle
1019.8756
19.1387
8.2857
197.6498
0.4712
1.6202
62131.2747
20.8320
13.6199
6.6190
9936.4572
4.5149
9529.8160
2164.7415
0.1000
32.7863
3224.1333
1.5383
2.2376
22668.1391
1.3170
7.3028
67.5208
Upper 95
1849.9286
20.4753
13.1724
259.9124
0.5667 i
1.6578 i
78288.5710
61.8507
20.2637
7.5107
52648.78.76 «
5.6987.'
15498.7394
64477.2653 «
0.1000. >
47.43021
3633.0802
1.4400'.
2.1129:
24490/1049
1.2302 :
8.0151 •
151.6867
MQIES
Concenuillons are sivelt ill U|/l. (ppb).
The 'i"in the lu right column uidicilei (l»l llw 95% Upper Confidence Limit u gieiler then ilie Minimum dcieiltd cimitnuilion.
     I'.ge I of I
UTnOWTMAJCI.S

-------
                                     Table  4
       CIIKMICAI. SUMMARY STATISTICS FOR GUOUNIWATKR - DISSOI.VKI) MI5TAI,S
                             .           I Al,l, SAMPLES)
                                     OCT.. Tie anil Treating Silo
ViiKliit Mail Aaiijils
Aluminum
Antimony
Ancitlc
Dkrium
DoyUiuiH
ddinlum
Ctlcbm
Chromium
Cobill :
Copper
lion
Lied '
tlitnciiuin
tltngineM
ktcrcury
Nlctd
'oluiium
Selenium
Sim
Sodium
TUlHum
Vkiudlum
ZlK '
VsB:!
19
40
40
40
40
40
40
IS
40
40
31
38
40
39 .
40
40
40
40
40
40
40
40
26
OC£U*
26
1
22
40
0
0
40
15
16
4
31
J
40 .
37
0
20
V,
3
|
40
9
6
19
L'ndsisi!
13
39
18
0
40
40
0
20
24
36
0
36
0
2
40
20
4
37
39
0
31
34
7
EsHi-M-d
8
0
7
7
0
0
10
10
3
3 .
»
0
7
9
0
4
7
1
1
7
3
3
8
RfjMl
1
0
0
0
0
0 .
0
5
0
0
9
2
0
1
0
0
0
0
0
0
0
0
14
Frcqutncj
p.l.cud
0.61
0.0]
0.55
1.00
000
0.00
1.00
0.4)
0.40
0.10
1.00
O.OS .
1.00
0.9S
0.00
0.50
0.90
0.08
0.03
1.00
0.23
0.15
0.73
Minimum
Concentrftllon
Delceled
17/10 •
18.30
2.00
«.30
0.00 '
0.00 •
1760.00
, 3.10
3.90
4.90
17.70
1.70
72.60
1.60
. 0.00
4.20
477.00
2.50
3.50
1140.00
1.60
J.70 •
9.10
Maximum
Concentration
Delected
3650.00
18.30 .
36.40
1060.00
0.00
0.00
116000.00
40.70
9110
24.50
36100.00
Z.90
34600.00
17600.00 .
0.00
73.50
15200.00
3.30
3.50
91500.00
3.40
27.90
74.00
Medlin
24.00
8.90
2.25
69 JO
0.10
0.65
36100.00
3.50
4.00
2.20
168.00
MS
4345.00
313.00
0.10 .
6.00
1465.00
1.40
1.85
12100.00
1.00
1.75
12.15
Geometric
Mctn
46.1812
10.1181
'2.4597 •..
84.5737
0.2346
1.0343
29824.4693
3.8421
4.9748
2.2388
514.9117
0.9326
3131.3196
175.9328
0.1000
6.9657
1611.3113
1.2491
1.8359
12810.3137
1.0S86.
2.6612
12.2732
Arithmetic
Mem
223.1577
. 13.1813
6.0588
159/1750
0.3513 '
1.3163
43733.0000
5.1700
12.7900
2.9113
7396.6419
1.0763
6922.1400
3055/4256
0.1000
13.9625 •
2651.8250
1.4225
• 1.8688
18546.2500
1.2313
3.3963
16.5596
Slindird
Diibllon.
654.9187
9.2515
9.8065
238.2946
0.3029
0.8878
30S84.I586
6.5707
20.3596
3.7193
12468.8819
0.5633
8572.8165
5144/4906
0.0000
19.5192
3627.7350
. 0.8242
0.3693
19565.3293
0.7740
4.4701
15.2686
memfy)
3J326
2.3143
0.9000
4/1376
-1.4499
0.0338
10.3031
1.3460
1.6044
0.8060
6.2440
•0.0698
B.M92
5.1701
•2.3026
1.9410
7.3854
0.2225
0.6076
9.45SO
0.0570
0,9788
2.5074
llde?(j)
1.4148
0.7467
1.3041
1.1000
0.9291
0.7103
1.0869
0.6763
1J26I
0.5984
2.6199
0.5552
I.S58I
3.3525
0.0000
1.1312
0.9028
0.5184
0.1900
0.8370
0.5291
0.6722
0.7670
n(|)
39
40
40
40
40
40
40
35
40
40
31
38
40
39
40
40
40
40
40
40
40
40
26
Lowir
Quirllle
17.5409
6.1137
1.0204
40,2652
0.1253
0.6405
14325.1059
2/4345
2.0334
M95I
87.9187
0.6412
1094.4642
18.3253
0.1000
3.2473
876.8297
0.8805
• 1.61 51
7282.8956
0.7407
1.690)
7.1151
Upptr .
Quitllle
' 121.5845
16.7453
5.9290
177*104
0.4391
1.6702
62093.7100
fi.0614
12.1710
3.3515
3015.6733
1.3564
8958.8705
1689.0468
0.1000
14.9420
2964.7120
1,7721
2.0870
22532.8I4«
1.5110
4.1891
20.5918
Upper 95
251.9726
17.1603'
10.0886
238,3523 .
0.5058 , i
1.6814 i
82230.8982
6.1317 '
2U247
3.2317
15661 5.94 M >
1.2988
21327.0473
I.044B«06 i
0.1000 i
20.7083
1148.5001
1.6731 '
1.9698
24125.9165
M3I8 !
4.M63
33.9177
                                                                                                                                                                  -•«*

                                                                                                                                                                  .-a
N01BS!
Conccntftlioiu ue |ivcn h unit) of u
Tlit •>' in ttic lit riila column indlciui dui dig j)5« Upper
l.iiuu ii |«iu> tlicu lie liiKuituin ilelecleil CMieenliilinn.
                                                                                                                                       Pip lot I
                                                                                                                                 u rnr,wi)MA-XUs

-------
                             Table  4                     \

CIIICMKJAI, SUMMARY STATISTICS FOR GROUNMVATEH >-  VOLATILE OUUANICS
             1                 | NO R8 WELL SAMPLES]      j
             1:                fiCL Tie nnd Treating Site      !
(Compound
Clilominediinc
UrimioiiKdiane
Vinyl cilia icte
ClitaroelluiK
Mciliykie chlwhk
Acetone
Cftibou disulfitle
l.l-l)iclilofoclhenc
I.l-Dicliloioel)iane
cn-l.l-DidikHoctlieiM
mm- 1,2-UiclilorocilKiK
Oiloiofonu
l.2-Dicliloioedian«
2-UlllWone
1,1.1-TlichlaiuelliilK
Cubou tetfaclilaride
llruliiodicliluiuuicdiane
1.2-Dichloropropane
cii-l.3-l>iciiliuo|uo|ieiie
Triclildruedicne
)ibromochJoruiiielliBne
1.1.2-Tiichlorocdiaiie
,2-Dibromuiiietliine
Jemeite •
Ham- l.3-l)ichli>tu|iioperie
Irottiofoiiii
4-MeUiyl-J iKlilanoiM
2-llcxanunc
tiliaclilotoelliene
HroillodiloroiiKlliane
, l.2,2-Tclr*i;liluruclliaiie
'ulueiK
Cldurubeiueiic
Hlliylbeiuene
SlyfClie
Xykiiei
1,2-Dklilorubonzeiie
1.3-nklilorobeti/ciie
l.4-l>Uliloiobcii/cnc
l,2'l)jhroiiiii-)-chluiu|irui>aiie
Villd
26
26
26
26
26
9
26
26
26
26
26
26
26
1
26
26
26
26
26
26
26
26
26
26
26
26
24
14
26
26
26
26
26
26
26
26
26
26
26
13
Otxur
1
0
J
1
0
4
0
6
7
10
1
4
I
1
6
P
0
0
0
9
0
0
0
5
0
0
4
0
0
0
0
7
0
7
4
4
4
0
0
0
Unduluc
25
' 26
11
25
26
5
26
20
19
16
25
22
25
0
20
26
26
26
26
17
26
26
26
21
26
26
20
14
26
26
26
19
26
19
22
22
22
26
26
15
Eillinilcil
1
0
2
0
0
4
0
3
3
5
1
4
0
|
2
0
0
0
0
3
0
0
a
I
0
0
3
0
0
0
0
5
0
1
1
0
1
0
0
0
lluj«.
0
a
0
0
0
17
0
a
0
' 0
0
0
0
25
n
0
0
0
0
a
0
a
a
0 '
0
a
2
12
0
0
n
0
n
n
0
0
0
u
0
M
'Kreipicncjr
IMi'clcil
0.04
0.00
0.12
0.04
0.00
0.44
0.00
0.2)
0.27
0.38
0.04
0.15
0.04
i.on
0.23
0.00
o.oa
0.00
o.no
0.3$
o.pa
fl.OO
0.00
0.19
O.IK)
o.oo
0.17
0.00
0.00
0.00
0.00
0.27
n.cx)
0.27
o.is
0.!5
0.15
0.00 .
0.00
0.00 '
Minimum
CoiKtiiilrallon
Dclrclcil
0.80
0.00
0.10
10.00
0.00
3.IH)
0.00
0.50
10.00
0.02
0.40
0.30
18.00
6.00
j.no
0.00
0.00
0.00
n.no
2.00
0.00
0.00
0.00
2.00
o.oo
0.00
2.01)
0.00
0.00
0.00
0.00
2.00
0.00
13.00
11.00
67.01)
0>30
o.mi
o.no
0110
Miilimini
ColKCIIlMlloll
Iteleeled
0.80
0.00
28.00
10.00
0.00
8.00
0.00
8.00
46.00
54.00
0.40
0.50
18.00
6.00
40.00
0.00
0.00
0.00
0.00
48.00
0.00
0.00
0.00
220.00
0.00
0.00
18.00
fl.OO
o.uo
0.00
0.00
180.0(1
0.00
580.00
130.00
2200.00
1200.00
0.00
0.00
0.00
MlMll.l
0.50
0.50
0.50
' 0.50
1.00
4.00
0.50
0.50
0.50
0.50
0.50
0.50
1.50
6.00
0.50
0.50
0.50
0.50
0.50
0.50
0.50
0.50
0.50
0.50
0.50
0.50
2.50
2.50
0.50
0.50
0.50
0.50
0.50
0.50
0.50
0.50
0.50
0.50
0.50
0.50
(•toniplrli
Mc,i,
0.7.^2
0.1118
e.sr,99
0.8212
2.074)
3.9442
0.7)18
1.0560
1.6266
1.5370
0.7255
0,7054
1.5784
6.00QO
1.4255
0.73 IjS
0.73 18
0.7318
0.7318
1.940-1
0.7318
0.7318
0.7318
1.4577
0.7318
0.7318
4.266)
3.8)5)
0.7318
0.7318
0.7)18
I-.5830
0.7318
1. 88118
I.I 105
1.6218
l.)080
0.7.118
0.7318
1). 74551
Arllhinelk
Mean
1.7231
I.7IIS
3.0231
2.0769
6.2115
4.3)3)
1.7115
2.4423
6.2308
10.0688
1.7077
1.6962
3.0000
6.0000
8.1346
1.71 15
1.7115 '
1.7115
1.7115
9.3462
. 1.71 15
1.7115
1.7115
23.3654
1.7115
1.71 15
9.9792
9.2857
1.7115
1.71 15
1.71 15
13.4615
1.7115
41.5769
9.8462
119.2500
60.5692
1.7115
1.7115
1.7667
Slimtird
Derlillon
3.3820
3.3858
6.2342
3.7435
14.9614
2.0616
3.3858
3.4852
10.2491
15.4814
3.3873
3.3918
4.4217
«D!V/DI
14.6973
3.3858
3.3858
3.3858
3.3858
16.0548.
3.3858
3.3858
3.3858
63.1760
3.3858
3.3858
17.2567
17.2490
3.3858
3.3858
3.3858
36.8369
3.3858
127.5335
29.1221
438.3157
239.3188
3.3858
3.3858
3.3-127
nieinfj
-0.2942
-0.3122
•0.1393
•0.1970
0.7296
1.3722
•0.3122
0.0545
0.4865
0.4298
•0.3208
-O.M9I
0.4564
1.79 IB
0.3545
-0.3122
-0.3122
•0.3122
•0.3122
0.6629
-0.3122
•0.3122
•0.3122
0.3769
-0.3122
•0.3122
1.4507
1.344)
•0.3122
•0.3122
-0.3122
0.4593
•0.3122
0.6317
0. 10-19
0.4835
0.2685
•0.3122
-0.3122
-0.2937
flllevfy
0.9974
1.0001
1.3685
1.1201
1.2515
0.4526
1.0004
1.2132
1.6744
2.2178
1.0047
1.0212
1.0335
nmv/oi
1.7697
1.0004
1. 000-1
1.0004
1.000.1
1.7916
1.0004
1. 0004
1. 000-1
2.0020
1.0004
1. 000-1
1.1062
1.0879
1. 0004
1.0004
1.0004
1.8956
I.OOIM
2.2785
1.6761
2.5212
2.1692
1. 000-1
I.OOIM
I.OSII
" Ihe far light column ilulicales dial die 95% U|>|>ei Timf itlenie I .huit is K
         i llicti die nunimiiiii iklculcil i
                                                                                                                           1'agc I of |
                                                                                                                      imimvnvi..xf.s

-------
                                                                                     Table   4

                                                  (.'IIKMICAI.SIIMMAItY STATISTICS I'Olt (.KOIINDWATIUl - SUMI-Vdl.ATII.KOHCANICS
                                                                    ;                |NO 118 WICM.SAMI'l.KSI
                                                                   ;.:                 <;CI. Tie nnd Trtulltij! Sl.lc
Cs:r.pc!!::d
Ilicuol
bii|2 CMuiotUiyl|tilKi
2-Qiloiophciiul
2-McthylplKiiul
Z.I'-oiybii- l-Cliluia|iio|iaiK
4-Mtiliyl|ilKiiol
^'Nil/oiodi-ti-prupyUmine
IcjudilorocthaiK
Niliobenutw
lopiiorotie
2-Niiniplienol
2.4 DiiMlhylplKiiol
>il|2*Cliloroediaiy)inedurM
2,4 nichliifoplKiuil
.2.4-Tmlilorobtnzene
Naplilliilcne
•QilofointtuM
lexiclilorobuiailiene
•(liliiiu-)-tiielliyljiliciiiil
2-Metliylna|ilillulciic
cxaclilufocyclupciiUilieno
,4,6-Tiichltifoplieiiol
2,4.5'Tricliloroplienol ' .
.Qiloioiuplillialciie
2-Niuoinilim
Diinclliylphihalaic
AcenaphtliyleiK
.6*Dinitn)tolueiie
•Nilrouiiline
AcciuplillKiK
2,4-Duuui>|>licnol
4-NilioplKiiol
)ibeiuofufan
2,4-DiniUotoluenc
Diclhylphllialale
4-ClilofOpncnyl plicnyMier
riuorenc
4 Niuouiiliiie
•1.6 l)iniuo-2-iiiciliyl|'lKiiol
•Nilfosodiptieiiylauiuie
4-DfOiiiophenyl pltetiykilicr
lleucldoiobeiiuiie
VaU
25
25
25
25
21
25
25
25
25
25
25
25
25
25
25
25
25
25
25
95
IS
11
25
25
25
25
25
25
25
25
25
25
25
25
25
25
25
25
25
25
25
15
One*
}
0
0
3
0,
4.
0
0
Oi
0
0
1
0
0
0
10
0
0
0
7
0
0
0
0
0
0
7
0
0
7
0
0
7
0
1
0
7
0
0
0
0
0
llndtlet
22
25
25
22
25
21
25
25
25
25
25
24
25
25
25
15
25
25
25
IS
25
25
25
25
25
25
18
25
25
18
25
25
18
25
24
25
18
25
25
25
25
25
Kttlraale
1
0
0
3
0
2
0
0
0
0
0
1
0
0
0
3
0
0
0
6
0
0
0
0
0
0
0
0
0
4
0
0
2
0
1
0
4
0
0
0
0
0
RclM
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
Freqlienc
Mclfclei)
0.12 '
0.00
0.00
0:12 '
o.ob
o.ie
0.00
0.00
0.00
0.00
0.00
0.04
0.00
0.00
0.00
0.40
0.00
0.00
0.00
0.28
0.04
0.00
0.00
0.00
o.oq
0.00
0.28
0.00
0.00
0.28 '
0.00
0.00
0.28
0.00
0.04
o.oo
0.28
0.00
0.00
0.00
0.00 •
o.no
Minimum
Concentration
Octet led
. 2.00
0.00
o.on
0.70
0.00
i.no
u.uo
0.00
0.00
0.00
0.00
4.00
0.00
(UK)
0.00
0.70
0.00
0.00
O.IUI
92..00
0.00
0.00
0.00
0.00
0.00
0.00
8.00
0.00
o.on
25.00
0.00
0.00
3S.no
0.00
0.80
0.00
'2.00
0.00
o.no
n.no
0.00
0.00
Maximum
Concentration
Delected
42.00
0.00
0.00
3.00
0.00
26.00
0.00
0.00
0.00
0.00
0.00
4.00
0.00
0.00
0.00
12000.00
0.00
0.00
0.00
1400.00
0.00
0.00
0.00
0.00
0.00
0.00
25.00 .
0.00
0.00
310.00
o.no
0.00
180.00
0.00
0.80
. 0.00
140.00
o.oo
0.00
0.00
0.00
0.00
Media
1.50
1.50
1.50
1.50
1.50
2.50
1.50
1.50
2.50
2.50
2.50
2.5O
2.5O
2.50
2.50
2.50
2.50
2.50
2.50
2.50
2.50
2.50
10.00
2.50
10.00
2.50
2.50
2.50
10.00
2.50
10.00
10.00
2.50
2.50
2.50
2.50
1.50
10.00
10.01)
2.50
2.50
1.50
(jcbmelrl
Mean
3.0819
2.5183
2.5183
14284'
2.5183
2.7611
2.5183
2.5181
2.5183
2.518)
2.5183
2.5661
2.518)
2.518)
2.5183
16.7023
1SI83
2.518)
2.518):
8.7257
2.518)
2.518)
10.0732
2:5183-
10.0732.
2.5183
4.0638
2.5183
10.0732
6.5509
10.0732
10.0732
6.3445
2.5183
2.4061
2.518)
4:2339
10.0732
10.0732
15183
15183
2.518)
Arllhmcll
Mem
5.1400
2.5200
2.5200
2.4880
2.5200
3.8400
2.5200
2.5200
2.5200
3.5200
2.5200
2.5800
2.5200
2.5200
2.520(1
1257.6280
2.5200
2.5200
2.52(10
111.9000
2.5200
2.5200
10.0800
2.5200
10.08(10
15200
6.0200
2.5200
10.0800
)4.5400
10.0800
10.0800
24.1800
2.5200
2.4520
2.5200
16.5800
10.0800
10.0800 '
2.5200
15200
2.5200
Standard
Devlallo
9.3291
0.1000
0.1000
0.4076
0.1000
5.2772
0.1000
0.1000
0.1000
O.I 000
0.1000
0)122
0.1000
0.1000
0.1000
289).V549
0.101)0
0.1000
0.1000
311.9521
0.1000
0.1000
0.4000
0.1000
0.4000
0.1000
6.5962
0.1000
0.4000 •
77.9155.
0.4000
0.4000
44.5334
0.1000
0.3584
0.1000
38.6975
0.4000
0.4000
0.1000
0.1000
0.1000
meanly
1.1256
0.9136
0.9236
0.8873
0.9236
1.0156
0.9236
0.9236
0.9236
0.9236
0.9236
0.9424
0.9236
0.9236
0.9236
2.8155
0.9236
0.9236
0.9236
2.1663
0.92)6
0.9236
2.3099
0.9236
2.3099
0.9236
1.4021
0.9236
2.3099
1.8796
2.3099
23099
1.8476
0.9236
0.8780
0.9236
1. 4-131
2.3099
2.3099
0.9236
0.9236
0.9236
sldev(j^
0.7347
0.0365
0.0365
0.7661
0.0365
0.6506
0.0365
0.0365
0.0365
0.0365
0.0365
0.0994
0.0)65
0.0)65
0.0)65
3.4137
0.0)65
0.0)65
0.0365
2.IIM6
0.0365
0.0365
0.0365
0.0)65
0.0365
0.0365
0.8097
0.0365
0.0365
1.6392
0.0365
0.0365
1.5)66
0.0365
0.2323
0.0365
1.3133
0.0365
0.0)65
0.0365
1.0)65
(1.0365
"(;
25
25
25
25
25
25
25
25
25
25
25
25
25
25
25
25
25
25
25
25
25
25
25
25
25
25
25
25
25
25
25
25
25
25
25
25
IS
25
25
25
25
25
lx>wer
Quarllle
1.8773
2.4571
2.4571
2.0294
2.4571
1.7801
2.4571
1.4571
2.4571
1.4571
2.4571
2.3996
2.4571
2.4571
2.4571
1.6693
2.4571
2.4571
2.4571
2.1093
2.4571
2.4571
9.8284
2.4571
9.8284
2.4571
2.3534
2.4571
9.8284
2.1677
9.8284
9.8284
1.2499
2.4571
2.0571
2.4571
1.7456
9.8284
9.8284
2.4571
14571
2.4571
Upper
Quarlll
5.0594
2.5810
2.5810
2.9060
15810
4.2827
2.5810
15810
2.5810
15810
2.5810
2.7441
2.5810
2.5810
2.5810
167.1140
2.5810
2.5810
2.5810
36.0963
2.5810
2.5810
10.3241
2.5810
10.3241
2.5810
7.0174
2.5810
10.3241
19.7969
10.3241
10.1241
.17.8909
2.5810
2.8143
2.5810
10.2692
10.3241
10.3241
2.5810
2.5810
2.5810
Upper 95
5.6010
2.5519 x
15519 x
2.7732
2.5519 x
4.5077
2.5519 »
2.5519 <
2.5519 i
2.5519 i
2.5519 x
2.6699
2.5519 «
2.5519 i
15519 i
476660.2074 I
2.5519 x
2.5519 x
15519 »
474.6334
2.5519 x
2.5SI9 «
10.207-1, x
2.5519 i
10.2074 i
2.5519 *
8.2023
2.5519 x
10.2074 I
78.4969
10.2074 I
10.2074 x
57.2626
2.5519 x
2.6887 >
2.SSI9 x
21.9390
10.2074 x
10.2074 x
2.5519
2.5519
2.5519 .
Coiiccnlf altuni •» given in utiili of ug/l. (ppb).                                 ;
'I IK V in ilit lu light column indicate! dial Ihe 95% ll|i|Kt Condclcntc Limit li gtcalef Iliui il'ie Minimum ilclcclcilviiiiicntialiiiii.
     Page I of 2
UTII(iW8SV.XI.S

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                                                                              Table 4
                                             CIIKMICALSIJMMAKYSTATISTICS FOR «ROUNDWATER
                                                                              |NO 118 WELLSAMPLKSI
                                                                              OCL Tie and Treating Site
SBMI-VOLATILK OROANICS
Compound
PcnUcbloioplienol
Phciunlliieiie
AnihiiceiK
Di-n-butylphdiibie
l*1uoiandtene
Pyieno
lluiylbeiuylididiilale
).y-Dlchloiabeiuidine
Beiuo|a|inlhtacene
CluyKM-
bu|2-EdiyOKiyl|phduliu
[)i-ivoclylplilli»!ile
Dciuo|b|niioi»uilMi»
Uenzo|k|nuoiaiiihene
Beiuolllpyienc
lndcno|l,2.3-cd|pyrene
Dibenxo[»,h]indiricene
lleiuolt.h^lpcfykiK
Villd
2$
25
25
25
25
25
25
25
2$
25
25
21
25
25
25
25
25
25
Occur
0
7
5
0
5
5
0
0
2
3
3,
0
2
1
|
1
0
1
Undclccl
25
18
20
25
20
20
25
25
23
22
22
25
23
24
24
24
25
24
Killmiltd
0
5
2
0 '
2
3
0
0
I
3
2
0
2
1
1
1
0
1
Reject
0
0
0
0
0
0
0
0
0
. 0
0
0
0
0
0
0
0
0
Frequency
Delected
0.00
a*
0.20
0.00
0.20
0.20
o.op
0.00
0.08
0.12-
0:12
0.00
0.08
0.04
0.04
• 0.04
o.ot
•0.0-


Minimum
Concentration
Delected
0.00
2:00
0.80
0.00
0.70
0.40
0.00
0.00
2.00
0.30
0.70
0.00
0.20
2.00
2.00
0.-70
0.00
0.60
Maximum
Concentration
Delected
0.00
180.00
16.00
0.00
54.00
32.00
0.00
0.00
6.00
. 4.00
51.00
0.00
3.00
. -2.00
2.00
0.70
0.00
0.60
Median
10.00
2.50
2.50
2.50
2.50
2.50
2.50
2.50
2.50
2.50
2.50
2.50
2.50
2.50
2.50
2.50
2.50
2.50
Cnmefrlc
Mean
10.0732
4.3363
2.8908;
2.5183
3.1457
2.8721
2.5183
2.5183
2.5849
2.2726
3.8182
2.5183
2.2930
2.4959
2.4959
2.3933
2..SI83'
4.3786'
Arithmetic
Mean
10.0800
19.3800
3.5320
2.S200
5.7680
4.2760
2.5200
2.5200
2.6400
2.4320
11.1480
2.5200
2.4480
2.5000
2.5000
2.4480
2.5200
2.4440
Standard
Deviation
0.4000
47.0703
3.1984
0.1000
i 1.3091
6.4833
0.1000
0.1000
0.7147
0.6283
23.0566
6.1000
0.4883
0.1443
0.1443
0.3776
0.1000
0.3969
mcan(j)
2.3099
1.4670
1.0615
0.9236
1.1460
1.0550
0.9236
0.9236
0.9497
0.8209
1.3398
0.9236
0.8298
0.9147
0.9147
0.8727
0.9236
0.8665
•lde»(j)
0.0365
1.3720
0.5612
0.0365
0.8416.
0.7455
0.0365
0.0365
0.1850
0.4727
1.1886
0.0365
0.5107
0.0588
0.0588
0.2587
0.0365
0.2892
n(>)
25
15
25
25
25
25
25
25
25
25
25
25
25
25
25
25
25
25.
Ijairtr
Quarllle
9.8284
1.7184
1.9797
2.4571
1.7829
1.7368
2.4571
2.4571
2.2815
1 16521
1.7123
2.4571
1.6247
2.3989
2.3989
2.0100
2.4571
1.9569
Upper
Quarlllo
10.3241
10.9424
4.2213
2.5810
5.5501
4.7493
2.5810
2.5810
2.9285
3.1262
8.5139
2.5810
3.2361
2.5969
2.5969
2.8496
2.5810
2.8911
Upper »5
10.2074 >
25.7833
4.2609
2.5519 <
6.6570
5.2960:
2.5519 i
2.5519 x
2.8090
3.0633
15.0616
2.5519 »
3.2072 i
2.5517 i
2.5517- x
2.7198 »
2.5519 I
2.7593 • *
MU1ES:
Concentrtlioiu ue liven in unill ol ug/1. (p|)b).
tin "«' in die lu rl|hi column Indicant dial ihe 95% (l|juei Confidence l.iinil it gieilef llitn I|K Minimum delected conceiiuiiion.
                                                               Pige2of2
                                                           uninwasvjcLS

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                                                                             Table  4              .


                                                    CIIKMICAI. SUMMARY STATISTICS FOIl OKOUNDWATHIl - I'I!STICID1!S
                                                                              |N(> R8 WELLSAMl'UiSI
                                                               '               G(JL Tie amnYeallne Site     '
Compound
•Iplu-BIIC
bcia-DlIC
ufug/l.(|vl>)'              '            -             '
Hie "i" In llie (u iltlii column Indicates ihti UK 95% I'lv" Confidence l.lniii Is gicuici then ilic mnxhiuim iiriccieil c«u:ciiiiaiUii.
Pojc I nljl

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                                                                                 Table  4

                                                     CIIICM1CAI,SUMMARY STATISTICS Will OROUNDWATER - TOTAL MMTAl-S
                                                                               |NO R8 WELL SAMPLES)
                                                                                (JCL Tie and Treating Slle
Total Metal Analilei
Aluminum
Antimony
Anenic
Blrhun '
Ueryllhiin
Caorniuin
Calcium
QuomUun
Cob.ll
Copper
Iron
l.ied '
Matneiium
Manganese
Mercury
Nickel '
Poluiiuin
Selenium
Silver
Sodium
TlullMra
Vanadium
ZBIC
Valid
25
26
26
26
26
26
26
17
26
26
25
15
26
25
26
26
26
2)
26
26
26
26
Ifr
Occur
25
3
17
26
0
0
26
t.
12
II
25
8
26
25
0
22
22
2
2
26
)
II
15
UndelKt
0
2)
9
0
26
• 26
a
9
14
15
! 0
. 7
0
. 0 '
26
. 4
4
2)
24
0
23
15
1
Eillmiltd
4
1
2
1
0
a
2
5
2
4
10
2
1
2
a
4
2
2
2
I
1
4
)
Reject
1
0
. 0
0
0
0
0
9
0
0
1
II
0
1
0
0
0
1
0
0
0
0
to
Frequency
Detected
1.00
0.12
0.65
1.00
O.OD
0.00
1.00
0.47
0.46
0.42
1.00
0.1)
1.06
1.00
0.06
0.8i
0.85
0.08
0.08
1.00
0.12
0.42
0.94

Minimum
Concentration
Delected
51.10
10.00
1.20
7.20
0.00
0.00
1660.00
7.20
6.00
3.10
83.20
1.20
222.00
2.80
0.00
3.90
' 564.00
2.20
4.00
3260.00
1.90
3.60
8.60
Miilmum
Concentration
Delected
6210.00
44.30
7.80
192.00
0.00
0.00
84400.00
166,00
79.10
25.60
37600.00
14.90
13500.00 .
17300.00
0.00
131.00
16000.00
2.40
4.60
98100.00
2.80
28.70
55.50
Median
383.00
25.50
2.25
72.55
0.50
1.98
42400.00
3.50
4.00
3.00
1220.00
1.45
4845.00
518.00
0.10
21.90
1715.00
1.00
2.00
12250.00
1.00
3.50
16.90
(ieomelrlc
Mem
456.7848
15.9860
2.0241
59.5281
0.3915
1.4099
30257.2)10
9.2521
6.9288
4.5510
1958.8044
2.4819
3518.6312
519.9522
0.1000
19.7564
2025.9305
1.0053
2.0402
12295.7921
0.9402
4.97'JS
18.2276

Arithmetic
Mean
937.0200
19.8904
2.8423
76.9962
0.5404
1.7000
42456.1538
35.6088
14.4769
6.4519
9441.8360
4.1233
5774.1923
4194.3600
0.1000
34.5808
3610.0000
1.1)60 .
2.1038
18619.6154
1.0558
7.6115
21.7563
Standard
Deviation
1310.8667
10.9227
2.2175
49.3756
0.3821
0.8735
24770.7665
57.1847
20.2464
6.0162
12978.8596
4.2990
4215.3013
5920.1028
0,0000
34.6814
•4568.6184
0.5345
0.6606
2)202.0221
0.5710
8.1)41
13.4530
m««n(j)
6.1242
2.7717
0.7051
4.0864
•0.9)77
0.34)5
10.3175
2.2248
1.9357
1.5153
7.5801
0.9090
8.1658
6.2537
•2.3026
2.98)5
7.6138
0.0052
0.7130
9.4170
•0.0617
1,6041
2.9029
ildcv(j)
1.2441
0.7582
0.8877
0.8309
0.9097
0.6870
1.0685
1.7182
1.1896
0.8227
2.1258
1.0537
1.2705
2.8163
0.0000
1.1905
1.0610
0.5346
0.2268
0.8445
0.4792
0.8890
0.6279
n(i)
25
26
26
26
26
26
26
17
26
26
25
15
26
25
26
26
26
25
26
26
26
26
16
Lower
Quirllle
197.3201
9.5848
I.I 120
33.9822
0.2119
0.8870
14715.0725
2.9027
3.1052
2.6125
466.7799
1.2191
1493.1461
77.7651
0.1000
8.8486
990.2224
0.7009
1.7507
6955.1566
0.6804
2.7302
11.9334
Upper
Quirllle
1057.4305
26.6621
3.6841
104.2782
0.7233
2.2412
62215.1217
29.4903
15.4605
7.9278
8219.9664
5.0527
8291.7308
3476.4991
0.1000
44.1103
4144.9216
1.4418
2.3776
21737.3256
1.2990
9.0600
27.8418
Upper 95
2027.9584
29.7422
4.5509
122.7801
0.9116 t
• 2.3903 x.
92709.3092 x
2D.5797 x
26.9110
9.2733
115169.5709 t
9.5954
16230/1205 >
589338.6180 x
0.1000 x
76.8764
6122.7012
1.4497
2.268" 1
25877,1747
1,2696
11.2042
31.6778
i
UQIB&                                                     '• .
Concentrations ire liven In uniu of ug/l.fj>pb).                            •
The "x" ill tlK fu rfgll! column Indicate! dial UK 9Sft Upper Confidence Limit i) greater ilieii die maximum delected concentration.
Page I of I

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                                                                                               Table
                                                              CllliMICAI.SIIMMAItVS-l ATISTICS I'OII (JltOllNDWA I Kit  -  I)I.SS(II.VKI) MKTAI.S
                                                                                              INOHfl WEIJ.SAMri.HS)
                                                                                               I aCI, Tie Riitl Trcnllny Sllc
Illuolvtd MtKI 
1.4536
52.7082
0.3713
1.4255
30I58.MI9
3.9027
6.1080
3.5981
565.8455
0.7607
2722.1184
264.7784
0.1000
9.5039
1921.0640
1.1053
2.0106
12144.3582
0.9490
3.1989
II.37M

AillluiKlIc
Mem
197.6380
16.8481
2.2692
69.0692
0.4865
1.7154
42085.3846
5.4563
16.0808
3.3596
9169.3183
0.9038
5289.1769
4225.3400
0.1000
18.5115
J417.5385
1.3038
2.0269
18176.5385
1.0558
4.4423
14.6300
Standard
lltvlillon
409.5587
9.3273
2.2449
47.0617
0.2978
0.8678
25075.1098
7.7821
23.6162
4.3903
14082.0306
0.6096
4146.7830
6078.2413
0.0000
22.7849
4324.5141
' 0.9035
0.3099
22128.5439
0.5529
5.3619
11.0131
intindr)
4.0098
2.6077
0.3740
3.9648
-0.9907
0.3545
10.3142
1.3617
1.91 81
0.9548
6.3383
4.2735
7.9092
5.5789
•2.3026
2.2517
7.5606
0.1001
0.6984
9.4016
-0.0524
1.1628
2.4315
il
2.4161 >
89569.1536
6.5355
33.2046
3.8558
1.087006 ,
I.I 201
23874/4389 >
2.760G«07 I
0.1000 «
34.8626
5757.1 109
I.&454
2.1100
25288.678 1
1.2541
5,69>l
23.7948
•'•
Concciitfilioiu »ie given etutult of iit/t. b).      -                          '
Hie '»" in OK far rigtri column inJicMci dial die 95% t'n*1 Catifiileiicc Ijiuitu gretlei IlKfi (lie maxuitimi ileleclc.l cirfltcn:i tllon.
          I of I
111 11OW8MD.XI.S

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                  RECORD OF DECISION FACT  SHEET
                          EPA REGION II
Site;
Site name:  GCL Tie & Treating, Operable Unit 2
Site location:  Sidney, Delaware County, New York
HRS score:  48.54   (10/14/93)
Listed on the NPL:  5/94
Site ID #:  NYD981566417
Record of Decision. Operable Unit 2;
Date signed:  March 31, 1995
Selected remedy:  Extraction and on-site treatment of
contaminated groundwater, with a contingency for containment
and/or natural attenuation; excavation and on-site treatment of
PAH-contaminated sediments on-site along the GCL-property soils
(OU-1) via a thermal desorption system.
Estimated Construction Completion:  2 years
Capital cost:  $1.9 - $2.1 million for groundwater portion
               $0.3 million for surface-water & sediment portion
O & M cost:    $0.6 million a year
Present-worth: $9.4 - $9.8 million for groundwater portion
               $0.3 million for the sediment portion
Lead;  EPA, remedial
Primary Contact:  Damian Duda, (212) 637-4269
Secondary Contact:  Doug Garbarini, (212) 637-4263
Main PRPs:  Harris Goldman
Waste;
Waste type:  PAHs
Waste origin:  On-site spills
Estimated waste quantity:  Approx. 10 million gallons of
contaminated groundwater; 125 cy of sediments.
Contaminated medium:  groundwater, sediments

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