-------
TABLE 2. SAMPLING RESULTS (JANUARY 1988-APRIL 1990): NICHOLS ENGINEERING AND RESEARCH CORPORATION
(ConcwutMlm In ppto)
PAGE 10F5
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9
-------
TABLE 2. SAMPUMG RESULTS (JAMUARY 19ee-APR*L 1990V. WCSHOLS B4QMEBWQ ANO RESEARCH CORPORATION
MW-3
PAGE20F5
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PAGE 3 OF 5
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-------
TABLE 2. SAMPLING RESULTS (JANUARY 19M-APWL1890): NICHOLS ENGINEERING AND RESEARCH CORPORATION
MW-9
PAGE 4 6(" 5
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Nichols Engineering
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191
-------
Nichols Engineering
operation since January 22, 1988, and as a result
the CC14 concentration has been reduced by 80 to
90 percent in some wells. "The rate of CC14
removal has decreased significantly during the
course of operation. Furthermore, the addition of
three additional extraction wells to the system in
January 1989 has not significantly accelerated the
ground-water cleanup.
The presence of CC14 within the unsaturated zone
is of primary concern. Although CC14 was not
observed in the unsaturated zone in initial soil
surveys (U.S. EPA, 1989), CC14 contamination in
the ground water may be attributed to the leaching
of CC14 from the soil. There seems to be a
correlation between increased precipitation and
increased concentration of CC14 in monitoring
wells. The method of storing wastewater in
settling basins at the site might have contributed to
contamination in the unsaturated zone.
The unsaturated zone at NERC can logically be
seen as two different zones. The first zone is the
part of the unsaturated zone that occurs naturally
in the absence of pumping. This natural
unsaturated zone is bounded by the ground surface
and water-table surface, which occurs 20 to 40 feet
below the ground surface. The second, or
induced, unsaturated zone is that part of the zone
created by the drawdown of the operating recovery
well.
A technique that currently is being considered and
that may improve the recovery rate of CC14 within
the induced unsaturated zone is intermittent
pumping. By shutting off the recovery wells and
allowing the water table to resume its natural
position, the induced unsaturated zone will become
inundated and some dissolution of CC14 into the
ground water will occur. Continued pumping can
then remove the CC14 captured by this process.
Intermittent operation of the recovery well(s)
would increase the removal of CC14 from the
induced unsaturated zone to some degree, but
CC14 in the natural unsaturated zone would not be
affected.
affect the removal of CC14 from this zone.
Alternatively, the treated ground water could be
recharged to the surface of the site to infiltrate
through the unsaturated zone and leach out the
CC14. The apparent correlation between
precipitation and elevated levels of CC14 in the
ground-water suggests that this would be effective.
As of June 1991, site operators were in
negotiations with NJDEP to cease ground-water
recovery operations at the site. If approved,
ground-water monitoirng will continue at the site.
The system would then be restarted should
concentrations of contaminants exceed the
threshold levels that have yet to be specified.
SUMMARY OF NAPL-RELATED
ISSUES
The possibility that contaminants may be present
in NAPL form at the NERC site has been
considered by Storch Engineers. No direct
evidence of NAPLs has been found in the field.
The ground-water concentrations that have been
detected in monitoring wells are well below the
aqueous solubilities of the compounds, but this
does not rule out the presence of NAPLs because
of the great dilution potential associated with
ground-water sampling.. Storch Engineers
acknowledges the possibility of NAPL presence.
However, evaluation of concentration variations
with depth and th,e apparent correlation of
increased concentration with rainfall have led them
to suspect that the source of residual contamination
is in the vadose zone. It is unclear whether the
vadose zone contamination is in the form of
NAPLs or is limited to adsorbed contaminants.
The CC14 in the natural unsaturated zone will not
be affected by ground-water extraction unless other
actions are taken. Although the displacement of
ground water by intermittent pumping will create
air How through this zone, the impact this air flow
has on the removal of CC14 is probably minimal.
Implementation of a soil vapor extraction system
does, however, have the potential to significantly
192
-------
UPDATE BIBLIOGRAPHY/
REFERENCES
New Jersey Department of Environmental
Protection (NJDEP), December 20, 1990.
Personal communication with Steven Kehayes.
Javandel, I., and C.F. Tsang. 1986. Capture-Zone
Type Curves: A Tool for Aquifer Cleanup.
Ground-water. 24(5): 616-625.
Storch Engineers. June 2, 1987a. NERC Report
on Ground-water Sampling Analysis, Assessment,
and Conceptual Cleanup Plan.
Storch Engineers. September 28, 1987b. NERC
Ground-water Contaminant Recovery and
Treatment System Design: Interim Progress
Report.
Storch Engineers. February 8, 1988a. NERC
Ground-water Cleanup Plan.
Storch Engineers. September 28, 1988b. 'NERC
Ground-water Cleanup Progress Report-July
1988.
Storch Engineers. November 28, 1988c. Letter to
Mr. Steven Kehayes describing progress of
ground-water recovery activities.
Storch Engineers. February 1989a. Letter to Mr.
Steven Kehayes describing progress of ground-
water recovery activities;
Siorch Engineers. March 1989b. Letter to Mr.
Steven Kehayes describing progress of ground-
water recovery activities.
Storch Engineers. April 1989c. Letter to Mr.
Steven Kehayes describing progress of ground-
water recovery activities.
Storch Engineers. June 1989d. Letter to Mr.
Steven Kehayes describing progress of ground-
water recovery activities.
Storch Engineers. December 1989e. Letter to Mr.
Steven Kehayes describing progress of ground-
water recovery activities.
Storch Engineers. July, 1990. Letter to Mr.
Steven Kehayes describing progress of ground-
water recovery activities.
Nichols Engineering
Storch Engineers. January 4, 1991. Personal
communication with Keith Ryan.
U.S. Environmental Protection Agency (U.S.
EPA). October 1989. Evaluation of Ground-
water Extraction Remedies: Volume 2, Case
Studies 1-19. EPA/9355.4-03.
193
-------
UPDATE OF CASE STUDY 13
Olin Corporation
Brandenburg, Kentucky
Abstract
Five new pumping wells have been installed since 1988 near the three Ranney wells and
along the river to enhance containment and site cleanup. Most of the plume is contained by
this system. Despite substantial total pumping, the concentrations in the three Ranney wells
have stabilized at high levels through 1989 and 1990 after decreasing in the early 1980s.
Trends are also generally stable in the five new pumpings wells, but are decreasing in some
monitoring wells near the pumping wells.
Table of Background Data
Date of Problem Identification
Extraction Started
Types of Contaminants
Primary Aquifer Materials
Maximum Number of Extraction Wells
Maximum Total Extraction Rate
Estimated Plume Area
Estimated Plume Thickness
Maximum Reported Concentrations
Early 1970s
1974
Dichloroethyl ether
Dichloroisopropyl ether
Silt and sand with interbedded clay
10
6,200 gpm
240 acres
80 feet
Dichloroethyl ether 48,000 ppb
Dichloroisopropyl ether 632,000 ppb
194
W71
-------
CASE STUDY UPDATE
OLIN CORPORATION
BACKGROUND OF THE PROBLEM
INTRODUCTION
The original case study for Olin Chemical
Corporation (U.S. EPA, 1989, Case Study 13)
evaluated ground-water remediation activities
through October 1988 at the Doe Run Facility in
Brandenburg, Kentucky. The site location is
shown in Figure 1. Olin Chemical has used
ground water from three wells since 1952 in its
manufacturing process and as a coolant, in the
early 1970s, ground-water contamination by ether
compounds caused by onsite disposal practices was
identified. These practices included thermal
destruction in open burning pits and the use of
settling basins as receptacles for processing wastes.
The Kentucky Division of Waste Management
oversees the present remedial activities. Ground-
water pumping from the Ranney wells that are
now a component of the remediation system began
in 1952 with plant startup. Identification of the
ether contamination and the development of a
monitoring and management program for the
contaminated ground water began in 1974.
The site is situated within the Ohio River alluvial
valley, which is the natural discharge area for the
region. The valley is divided into two terraces.
The lower portion is a flood plain subject to
.frequent overflows of the Ohio River. The upper
section is where most of the Olin facility is
located. The upper 20 to 30 feet of material near
the river is predominantly fine-grained silt and
sand with interbedded layers of clay. A thick
sequence of sand and gravel underlies the upper
sand layer. The bedrock below these layers is
comprised of low porosity/low permeability
limestone. Ground water at the site generally
exists under unconfined .conditions. Recharge to
the aquifer is received from precipitation, leakage
from the bedrock valley walls, and leakage from
unlined ditches and streams that cross the flood
plain. The natural ground-water flow at the site is
north toward the Ohio River, however, at high
river levels, the Ohio River is also a source of
recharge to the aquifer.
Contaminants of concern are chloroethers,
primarily dichloroethyl ether (DCEE) and
dichloroisopropyl ether (DCIPE). An estimated
18,000 tons of propylene dichloride, DCEE, and
DCIPE were disposed of in a burning pit between
1952 and 1974. Additional wastes were
discharged to a settling lagoon and to the burner
area, which incinerated an estimated 10 tons of
off-gas. When ground-water contamination was
identified and monitoring began in 1974,
concentrations of DCEE ranged from 50 ppb to
approximately 3,000 ppb, and DCIPE
concentrations ranged from 100 ppb to 32,000 ppb.
UPDATE ON SITE
CHARACTERISTICS
This updated case study is based on 1989 and
1990 data provided by Olin Corporation. The
information includes monitoring-well sampling
results, a summary of ground-water extraction
rates, and average ether concentrations for the
Ranney Wells and new wells. Personal
communication with staff from the Olin
Corporation supplemented the documentation.
Olin Corporation continues to operate the
remediation system,, with oversight from the
Kentucky Division of Waste Management.
REMEDIATION
Design and Operational Features of
Remediation System
The goal of remediation at the time of the original
case study was to prevent contaminant migration
beyond the region currently affected. Aquifer
restoration is not a component of remedial
objectives. Human health standards based on a
10'6 excess lifetime cancer risk would be 0.03 ppb
for DCEE and 34.7 ppb for DCIPE (U.S. EPA,
1980). These standards, however, are not remedial
objectives at this site.
The remediation system used to implement these
goals includes three radial wells constructed in the
early 1950s (Ranney Wells 1, 2, and 3) and two
vertical wells installed in 1978 (Collector Wells 4
195
-------
Olin Corporation
196
-------
Olin Corporation
and 5). The three Ranney wells were installed and
operating prior to identification of an ether
contamination problem. The two vertical wells
installed in 1978 were installed to increase the
water supply of the manufacturing plant and were
not intended to contain the contamination.
After studies had been conducted to determine the
source's and the extent of contamination and to
characterize site geology and hydrogeology, the
responsible parties developed a management plan
in 1984 to contain the contaminant plumes. After
it was determined that contamination could be
contained onsite by the existing pumping wells,
optimum remedial pumping rates were established
in 1984. Ranney Well 3 is designed for rates
between 1,000 and 1,500 gpm. The combined
pumping rate of Ranney Wells 1 and 2 are
maintained at 100 gpm higher than that of Well 3,
and Well 1 is operated at a minimum rate of 500
gpm between July and October. The original case
study concluded that, under the above pumping
conditions, the ground-water flow beneath all
solid-waste management units is intercepted by the
Ranney and collector wells.
Thirty-three monitoring wells are onsite to evaluate
remedial progress. Three of the monitoring wells
(MW-7, BH-1, and MW-2) are located in the
contaminant plume and were used in the original
case study to indicate the progress of remediation.
Figure 2 shows the location of the Ranney wells,
the Collector wells, and the plume indicator wells
in relation to the source areas at the Doe Run
facility.
In the two years since the original case study was
published, the pumping rates for the Ranney wells
have not changed significantly. During 1989 and
1990, Ranney Well 3 was operated at or slightly
below its minimum design rate.
Major modifications to the system during 1989 and
1990 include the installation of five new pumping
wells (IW-1, IW-2, IW-3, IW-4, and IW-5) that
began operation in July and August 1989. Figure
2 shows the locations of these wells. The wells
provide additional water for plant needs, help
clean up the contamination in the Ranney wells,
and provide further assurance that contaminated
ground water does not migrate offsite. Table 1
presents the pumping rates of all the Olin wells.
The new wells, particularly IW-3, did not operate
continuously during 1989 and 1990. This
downtime is due to National Pollutant Discharge
Elimination System (NPDES) permitting
restrictions which limit the discharge of ethers to
the river. To avoid discharging quantities of
ethers above the permitted limits, certain wells
have needed to be shut down temporarily.
Typically, Well IW-3 is a swing well. If ether
concentrations approach the permit limits, then the
well (or wells) is taken offline.
EVALUATION OF SYSTEM
PERFORMANCE
Ground water was tested at the Doe Run facility
throughout 1989 and 1990. to determine the
concentrations of DCEE and DCIPE. Figures 3,4,
and 5 provide the time-series concentrations of
DCIPE and DCEE for the plume-indicator wells
(MW-7, BH-1, and MW-2) from 1984 to 1990.
DCIPE concentrations in ground-water samples
from Well MW-7, which is located directly
downgradient from the off-gas burners, have
decreased from an October 1986 high of almost
3,000 ppb to below detection levels by October
1990. DCEE concentrations have continued to
stabilize at or near the low levels achieved in
1987. The continuation of low detection levels in
MW-7 suggests that the contaminant plume
reached and passed this well.
In Well BH-1, DCIPE levels decreased from
concentrations of more than 6,000 ppb identified
in the earlier case study to 2 ppb in October 1989
and below detection levels in October 1990. The
reduced concentrations of both DCBPE and DCEE
during 1989 and 1990 are part of a contaminant-
reduction trend that began in 1986.
MW-2, which is located between Ranney Wells 2
and 3, has also undergone intermittent fluctuations
in concentration levels since the system began
operation. DCEE concentrations were as high as
6,000 ppb in 1985, and DCIPE levels were greater
than 1,000 ppb. Concentrations of both
contaminants, however, were markedly reduced by
October 1988 and were below detection levels by
October 1990.
Contaminant concentrations in the Ranney wells
have also decreased from levels identified in the
first case study. Ranney Well 1, which registered
the highest levels of DCIPE in the early 1980s
(15,000 to 30,000 ppb), has exhibited a decrease in
both DCIPE and DCEE since 1988. The highest
concentration detected during the 1989-1990
period was 9,160 ppb of DCIPE in September
197
-------
Olin Corporation
i
fill!
t
I
!
§
,'••»
198
-------
Olin Corporation
Table 1
OLIN CHEMICAL CORPORATION, DOE RUN PLANT
AVERAGE PUMPING RATES FOR RANNEY,
COLLECTOR, AND NEW WELLS
1989-1990
Well
Raimey Well 1*
Ranney Well 2*
Ranney Well 3
Collector Well 4
Collector Well 5
IW-1
IW-2
IW-3
IW-4
IW-5
Pumping Rate (gpm)
1000-1200
1000-1200
800-1000
1500
1000
300-400
200-400
Normally Offline
200-400
300
Source: Olin Chemical Corp., 1991a
* = Ranney Wells 1 and 2 are alternated.
199
-------
3000 T
500
JUIV84 Nov-84 Stp-85 Apr-86 Oct-86 Apr-87 Oet-87 Aftr-88 Od-88 Apf-«9 Oct-«9 Apr-90 Oct-90
Source: EPA, 1989; OBn Chemical Corp., 19913
ETHER CONCENTRATIONS IN MW-7
OL1N CHEMICALS GROUP
DCCRUNPUWT
O
o
•3
o
o
"3
-------
Uftmf;
DCJP6 *
DCEE O
Jun-84 Nw-M 8^85 Apr-86 Oet-86 Apr-87 Oct-87 Apr-88 Oct-88
Oct-89 Apr-90 Oct-90
Source: EPA, 1989; OBn Chemical C«p., 1991a
-4
ETHER CONCENTRATIONS Ml BH-1
OLfN CHEMICALS GROUP
DOE RUN PLANT
O
•3
O
O
a
-------
L*g*mf:
ware *
DCEE O
Jun-84 Nov-M
Apr-98 Oct-86 Apr-87 Oct-87 Apr-88 Oet-88 *pr-«
Apr-90 Oct-90
Source; EPA, 1989; OKn Chemical Corp., 1i91a
FfgureS
ETHER CONCENTRATIONS IN MW-2
OLIN CHEMICALS GROUP
DOE RUN PLANT
g
3"
O
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-------
Olin Corporation
1989. The average monthly concentration of
DCIPE for the 2-year period since publication of
the first case study was approximately 5,000 ppb.
The concentrations for DCEE and DCIPE in
Ranney Wells 2 and 3 are generally below those
levels detected in Ranney 1. Table 2 provides the
average concentrations of DCIPE and DCEE for
each of the Ranney Wells for 1989 and 1990 and
shows that although average concentrations have
declined from levels detected in the early 1980s,
no significant reductions have occurred during
1989 and 1990. Both DCIPE and DCEE are in
excess of health-based standards.
Table 3 provides the DCEE and DCIPE
concentrations for .the new wells for 1989 and
1990. DCEE and DCIPE concentrations in these .
wells also register above health-based standards.
DCIPE concentrations are greatest in IW-1 (21,350
ppb), but DCEE levels as high as 3,980 ppb have
been detected in IW-3.
SUMMARY OF REMEDIATION
Remediation objectives have not changed since
publication of the first case study; the goal at
Olin's Doe Run facility is to control further
migration of the plume. Although health-based
standards have been set for primary site
contaminants, these cleanup parameters have not
been incorporated into remedial goals.
Concentrations of DCIPE and DCEE continue to
decline from the elevated levels registered before
remediation began. In the three plume-definition
wells, concentrations are below or slightly above
detection levels. The high pumping rates
established at the start of remedial activities are
still in effect and continue to contribute to the
containment of site contamination.
Although contaminant concentrations have been
reduced in the Ranney wells since the early 1980s,
no significant declines have occurred during 1989
and 1990, and concentrations remain above
established health standards.
In the interim since the initial case study, five new
wells have been installed to provide additional
water for plant use, to accelerate cleanup of the
Ranney wells, and to ensure that contamination is
contained onsite. Contaminant concentrations in
these wells are in excess of the levels identified in
the monitoring and Ranney wells.
SUMMARY OF NAPL-RELATED
ISSUES
Efforts to determine the presence or absence of
nonaqueous phase liquids (NAPLs) at the Olin site
have not been undertaken since remediation began
in 1974. Plans, however, are pending to initiate
such investigations. Although contaminant
concentrations have been reduced in almost
20 years of recovery-system operation,
concentrations in Ranney Wells 1 and 3 appear to
have stabilized at levels 2 to 3 orders of magnitude
higher than health-based criteria. In addition,
ground-water samples from the new wells, which
are located south of Ranney Wells 1 and 2, show
contaminant concentrations above those detected in
the Ranney, Collector, and plume-definition
monitoring wells. The presence of a NAPL in the
aquifer could prevent aqueous concentrations of
ethers from decreasing further, despite
remediation.
The primary waste constituents at the site, DCIPE
and DCEE, have respective aqueous solubilities of
1,700,000 ppb and 10,200,000 ppb. Their specific
gravities are 1.103 and 1.22, respectively. To
date, the highest concentrations of contaminants
were recorded in a monitoring well during the
1975 annual sampling. Concentrations were
analyzed at 632,000 ppb for DCIPE (37 percent of
solubility) and 48,000 ppb for DCEE (0.5 percent
of solubility). Cbncentrations above 1 to
10 percent of solubility suggest that NAPLs might
be present in the aquifer. Although the
concentrations in Ranney Well 1 are less than
1 percent of solubility, the Ranney Collector
would be expected to dilute the sample due to its
geographical reach and subsequent extensive
recovery area.
Source characteristics of contaminants also suggest
that a NAPL may exist. Approximately 18,000
pounds of chloroethers were disposed of in a
burning pit between 1952 and the early 1970s in
the area of Ranney Well 1.
Site operators acknowledge that ether
contamination could be caused by NAPLs. At
present, they do not believe NAPLs exist due to
decreasing contaminant concentrations in the
ground water. However, system operators intend
to conduct geologic and hydrogeological studies to
determine the extent of vertical contamination.
Once these studies have been completed, they plan
to explore alternative remedial technologies.
203
-------
Olin Corporation
Table 2
OLIN CHEMICAL CORPORATION, DOE RUN FACILITY
AVERAGE CONCENTRATION (ppm) OF
CHLOROETHERS IN RANNEY WELLS*
1989-1990
Month/Year
Jan. 1989
Feb. 1989
Mar. 1989
Apr. 1989
May 1989
June 1989
July 1989
Aug. 1989
Sept.1989
Oct. 1989
Nov. 1989
Dec. 1989
Jan. 1990
Feb. 1990
Mar. 1990
Apr. 1990
May 1990
June 1990
July 1990
Aug. 1990
Sept.1990
Oct. 1990
Nov. 1990
Dec. 1990
Ranney Well No. 1
DCEE
DCIPE
Not Running
Not Running
Not Running
0.05
0.14
4.01
5.77
Not Running
0.24
6.87
Not Running
0.03
0.02
0.009
0.08
0.08
9.16
2.37
2.684
5.699
4.35
Not Running
0.04
0.08
0.17
0.52
0.08
0.12
0.06
0.04
0.28
0.20
1.10
3.88
5.38
4.24
3.67
4.89
5.53
5.24
6.96
6.65
Ranney Well No. 2
DCEE
0.12
0.112
0.051
DCIPE
2.83
3.10
1.99
Not Running
Not Running
0.14
0.06
0.16
3.33
2.01
2.04
Not Running
Not Running
0.025
2.01
Not Running
0.042
0.036
0.32
1.448
1.81
2.08
Not Running
Not Running
0.32
1.54
Not Running
Not Running
Not Running
Not Running
Not Running
Not Running
Ranney Well No. 3
DCEE
0.22
0.092
0.043
0.41
0.32
0.21
0.18
0.19
0.03
0.07
0.238
1.09
Q.176
0.27
0.33
0.15
0.17
0.18
0.16
0.26
0.13
0.13
0.14
0.17
DCIPE
0.22
0.088
0.081
0.31
0.23
0.26
0.19
0.22
0.05
0.11
0.306
1.83
0.503
0.13
0.45
0.20
0.33
0.29
0.25
0.29
0.21
0.21
0.30
0.27
Source: Olin Chemical Corp., 1991
"Operating practice of these wells: Combined flow of RW-1 and RW-2 will exceed RW-3 flow.
204
%f)\
-------
Olin Corporation
Table 3
OLIN CHEMICAL CORPORATION DOE RUN FACILITY
NEW WELL CHLOROETHER CONCENTRATIONS (ppm)
1989-1990
Month/Yr.
8/89
9/89
10/89
11/89
12/89
1/90
2/90
3/90
4/90
5/90
6/90
7/90
8/90
9/90
10/90
11/90
12/90
IW-l
DOPE
21.35
9.26
NS
6.24
6.66
4.20
6.75
13.96
6.17
5.23
6.84
2.98
3.30
4.75
4.24
5.57
5.73
DCEE
035
0.09
NS
0.09
0.16
0.07
0.07
0.16
0.06
0.05
0.04
0.03
0.05
0.02
0.03
0.03
0.02
IW-2
DOPE
0.15
0.14
NS
NS
NS
0.09
0.08
0.25
037
0.36
035
0.24
0.23
034
032
037
038
DCEE
0.03
0.03
NS
NS
NS
0.02
0.04
0.12
0.04
0.09
0.07
0.04
0.08
0.10
0.06
0.17
0.20
Source. Olin Chemical Corp., 1991
NS = Not sampled.
IW-3
DCIPE
0.09
0.12
NS
0.36
0.32
NS
NS
NS
0.80
NS
NS
0.21
1.17
032
NS
NS
NS
DCEE
0.03
0.15
NS
1.12
1.12
NS
NS
NS •
0.70
NS
NS
0.05
2.66
3.98
NS
NS
NS
IW-4
DCIPE
0.03
0.04
NS
0.10
0.27
0.08
0.13
0.57
0.19
0.22
0.14
0.14
0.22
0.44
0.48
0.49
0.50
DCEE
0.03
0.21
NS
0.64
0.42
0.44
0.49
0.91
0.89
1.10
1.03
1.07
1.01
1.63
0.95
1.16
1.30
IW-5
DCIPE
1.46
1.79
NS
NS
1.36
NS
NS
1.60
0.80
0.52
0.41
0.29
031
0.44
0.44
033
0.29
DCEE
0.47
0.03
NS
NS
1.34
NS
NS
0.26
0.19
0.15
0.10
0.06
0.08
0.08
0.07
0.08
0.18
205
-------
Olin Corporation
UPDATE BIBLIOGRAPHY/
REFERENCES
Olin Chemical Corp. September 1986. A
Ground-Water Assessment of Olin Chemicals
Group Doe Run Plant, Brandenburg, Kentucky.
Olin Chemical Corp. March 7, 1991a.
Correspondence from Danny M. Henderson,
Environmental Specialist, Olin Chemicals,
Charleston, Tennessee.
Olin Chemical Corp. February 1991b; March 28,
1991c. Personal communication with Danny M.
Henderson, Environmental Specialist, Olin
Chemicals, Charleston, Tennessee.
U.S. Environmental Protection Agency (U.S.
EPA). October 1989. Evaluation of Ground-
Water Extraction Remedies: Volume 1, Case
Studies 1-19. EPA/9355.4-03.
U.S. EPA. November 28, 1980. Federal Register.
45(231):793330.
206
-------
UPDATE OF CASE STUDY 14
Ponders Corner
Tacoma, Washington
Abstract
Pumping and wellhead treatment at water-supply Wells HI and H2 have continued since
1984. The system has continued to meet its primary objective of providing treated water
for public consumption. The zone of capture of HI and H2 has continued to include areas
of contamination, except for a small part of the plume that escaped before 1984. PCE
concentrations in HI and H2 and monitoring wells downgradient of the source area have
been stable since the end of 1985. This persistence of contamination is believed to be
caused by a residual source.
Table of Background Data
Date of Problem Identification
Extraction Started
Types of Contaminants
Primary Aquifer Materials
Maximum Number of Extraction Wells
Maximum Total Extraction Rate
Estimated Plume Area
Estimated Plume Thickness
Maximum Reported Concentrations
1981
September 1984
Tetrachloroethylene
Trichloroethylene
Trans- 1 ,2-Dichloroethylene
Glacial sand, silt, gravel, and clay
2
2,000 gpm
23 acres
80 feet
Tetrachloroethylene 4,866 ppb
207
-------
CASE STUDY UPDATE
PONDERS CORNER (LAKEWOOD)
BACKGROUND OF THE PROBLEM
INTRODUCTION
This case study update discusses recent
developments and progress in the ground-water
remediation at the Ponders Corner site (also known
as the Lakewood site) in Tacoma, Washington,
The original case study for this site (U.S. EPA,
1989, Case Study 14) presented background
information and data from the site ground-water
monitoring and remediation systems that were
current through March 1989.
The location of the Ponders Comer Site is shown
in Figure 1. It includes the property of Plaza
Cleaners and two water supply Wells, HI and H2,
belonging to the Lakewood Water District. In
1981, it was discovered that disposal of waste
solvents from the dry cleaning operations at Plaza.
Cleaners had resulted in contamination of the two
water supply wells. In August 1981, Wells HI
and H2 were taken out of service temporarily
while monitoring wells were installed and
contaminated surficial soil in the source area was
excavated. By September 26, 1984, air strippers
had been installed to treat the water produced from
the contaminated wells, and pumping was
resumed. Remedial activities at the Ponders'
Corner site were conducted under the U. S. EPA's
Superfund program.
The Ponders Corner site is underlain by glacial
deposits of sand, gravel, silt, clay, and till. The
four major geologic units underlying the site are,
in order of increasing depth: (1) the Steilacoom
gravel, a unit of sand and gravel, (2) the Vashon
till, consisting of low-permeability sediments, (3)
the Advance Outwash aquifer, an important
regional aquifer, and (4) the Colvos sand, a _ unit
consisting of silt, clay, and fine silty sand. Wells
HI and H2 are completed in the Advance Outwash
aquifer at a depth of approximately 110 feet. The
Advance Outwash is a highly permeable semi-
confined to confined aquifer. The natural direction
of ground-water flow is west-northwest toward
nearby Gravelly Lake. However, at the Ponders
Corner site, ground water in the Advance Outwash
flows to the south under the influence of pumping
from Wells HI and H2.
The main contaminants of concern are
tetrachloroethylene (PCE), trichloroethylene (TCE),
and trans-1,2-dichloroethylene, all of which are
solvents or by-products of solvents used in dry
cleaning. The dry cleaning wastes at Plaza
Cleaners were discharged to a septic tank system
consisting of three buried tanks with a total
volume of 4,250 gallons. The wastes were flushed
through the tanks to the septic system drain field
by 15,000 to 20,000 gallons of laundry wastewater
per day. Solvent-contaminated wastewater and
sludge was also poured onto the ground outside
the Plaza Cleaners building. These discharges
resulted in soil contamination in both the
unsaturated Steilacoom gravel and in the
underlying Vashon till, and represent a continuing
source of contaminant leaching to the ground
water.
When water supply Wells HI and H2 are in
operation, the contaminated ground water from the
' site is hydraulically contained, removed, and
treated. However, during the three years when the
wells were out of operation, a part of the
contaminant plume • in the Advance Outwash
aquifer was transported away from the site to the
west-northwest. This isolated contaminant plume,
with PCE concentrations of less than 10 ppb,
escaped the capture zone of the wells and
continued to move toward Gravelly Lake after
pumping resumed.
UPDATE ON SITE
CHARACTERISTICS
The Ponders Corner site continues to be
administered by the EPA. However, after
completion of the ongoing soil remediation study
in the first quarter of 1991, the Washington State
Department of Ecology is expected to take over
operations and maintenance activities at the site,
including ground-water monitoring.
No new information about the hydrogeologic
characteristics of the site has been generated since
the original case study. However, the operational
results of a soil vapor extraction system at Plaza
208
-------
LAKEWOOD
WATCH DtSTtllCT
WELL$
Bl80d OftCH2M HILL, 1987
LEGEND
• MONITORING WELL
• TEST OR PRODUCTION WELL
WASKIMOTON
Figure 1
SITE LOCATION MAP
PONDERS CORNER SITE
TACOMA, WASHINGTON
-4
"0
o
a
o
(0
O
O
-------
Ponders Corner
Cleaners has shown that the quantity of PCE
contamination in the unsaturated Steilacppm gravel
was much greater than had been expected during
the design stage.
It was initially estimated that the contaminated
soils in the upper portions of Steilacoom gravel at
Plaza cleaners contained approximately 4 to 5
pounds of PCE (U.S. EPA, 1985). (This in not to
be confused with the estimate of 10 pounds of
PCE in the saturated portions of the Steilacoom
gravel listed in Table 1 of the original case study.)
The 5-pound estimate was based on analysis of 82
soil samples collected from seven soil borings and
six shallow test pits installed on the Plaza Cleaners
property during the remedial investigation.
Beginning in March 1988, a soil vapor extraction
system was operated at Plaza Cleaners to
accelerate the cleanup of the unsaturated
Steilacoom gravel in that area. In approximately 1
year of intermittent operation an estimated 775
pounds of PCE were removed by soil vapor
extraction (CH2M HELL, I989a). No explanation
for this discrepancy has been given.
REMEDIATION
Design and Operational
Features of the Remediation
System
The primary objective of the wellhead treatment
system is to capture the plume of ground-water
contamination while providing potable water from
production Wells HI and H2. In addition, it is
expected that continued operation of the system
will lead to eventual restoration of ground-water
quality to health-based levels.
The ground-water remediation system consists of
continued pumping from water supply Wells HI
and H2 at a combined rate of approximately 2,000
gpm. There have been no significant changes in
the wellhead treatment system since it started
operating in 1984. However, the ground-water
monitoring system at the site has been modified,
and soil vapor extraction has been used to
remediate contaminated soils in the source area. A
study of final remedial actions is currently taking
place to determine whether additional soil
remediation activities are needed.
As described in the original case study, a total of
36 ground-water monitoring wells were installed
by the time the remedial investigation was
completed. In February 1987, six more wells were
installed, one in the area of the uncaptured plume
northwest of the site and five along the perimeter
of McChord Air Force Base. In April 1989, an
inventory of the site monitoring wells was
conducted to determine which ones needed repair
or abandonment. By that time, there were 51
monitoring wells at the site. As a result of the
inventory, it was recommended that 17 wells be
repaired, and that 23 be abandoned. Most of the
wells were found to be damaged or to have
deficiencies in surface completion that would make
them possible conduits for further contamination of
the subsurface. Much of the damage was caused
by vandalism (CH2M HILL, 1990b).
The soil vapor extraction system was installed
around the former septic tank and its associated
drain field system at Plaza Cleaners in December
1987. It consisted of ten 2-inch wells installed to
depths of approximately 18 feet, and three
horizontal vapor extraction headers installed within
the three abandoned septic tanks. The vapor
extraction system was equipped with activated
carbon filters large enough to adsorb an estimated
total of 40 pounds of PCE at the expected vapor
phase concentration of 25 ppm. The system was
put into operation on March 22, 1988, and
extracted vapor containing up to 170 ppm of PCE
on the first day. After one month of operation the
average vapor concentrations had been reduced to
about 14 ppm. An estimated 360 pounds of PCE
had been removed during the first month of
operation. Operation of the system continued
intermittently, with interruptions for replacement
of the activated carbon, until April 1989. During
this time, an estimated total of 775 pounds of PCE
was removed.
-iiii ''
EVALUATION OF PERFORMANCE
Six rounds of ground-water samples have been
collected from the network of monitoring wells
since July 1987, the date of the last sampling
reported in the original case study. The most
recent reported sampling occurred in April 1990.
Table 1 lists a cumulative summary of the PCE
concentrations measured in the monitoring wells
since 1985. The locations of the monitoring wells
are shown in Figure 2. In general, the
concentrations in contaminated wells that do not
lie between the source area and the production
wells have declined over the period of record.
Wells that are located between Plaza Cleaners and
210
-------
TiMtl
PCE CONCENTRATIONS MEASURED IN MONITORING WELLS
PONDERS CORNER SITE
Wfll
No.
IIA
1IB
12
13A
I3B
14
ISA
I5B
16A
16B
17A
17B
18
19A
19B
19C
20A
20B
21
22
24A
24R
25
2«
27
2SA
29
30
31
.12
MSB
VI4*S
6.2
NM
ND
ND
NM
NM
NM
NM
110
NM
ND
NM
ND
ND
NM
NM
NM
27
NM
8.5
NM
ND
ND
NO
ND
5.8
.18
ND
Nl)
Tte^l
JttOTS
5.6
NM
ND
ND
NM
NM
0.5
NM
70
15
ND
ND
ND
ND
NO
5.1
4,85*
2.2
NM
IS
9.5
ND
ND
NM
0.7
0.9
24.1
ND
4J
4OSOS
NM
NM
ND
ND
NM'
NM
NM
NM
NM'
NM
NM
NM
NM
NM
NM
NM
2,200
NM
NM
NM
NM
NM
NM
NM
NM
NM
NM
NM
5
stitas
Thrash
smuts
6.1
NM
ND
ND
NM
NM
Nl)
NM
46
13
ND
ND
ND
Nl)
ND
NM
570
1.1
NM
7.2
0.9
ND
NM
NM
ND
54
11.2
ND
6.9
units
6/21/tt
2.7
NM
ND
ND
NM
NM
Nl)
NM
33
5
ND
ND
ND
ND
ND
2.8
1220
11
NM
4.4
40
ND
NO
NO
Nl)
II
13
ND
3.3
MM*
«*»«•
4.3
2.4
ND
NM
NO
NM
ND
NM
12fllh
NM
ND
NO
D
ND
ND
4.0
1.060
10
NM
16
4.9
ND
Nl)
NO
NM
.14
NM
Nl)
.17
11/StS
1 Iff /IS*
2
NM
ND
NM
ND
NM
ND
NM
19
f
ND
ND
ND
ND
ND
ND
350
ND
NM
NM
ND
13
9
Nl)
Nl)
ND
10
ND
ND
W2S/M
ThmRk
ttunt
1.4
NM
ND
NM
ND
NM
ND
NM
16
4.5
NM
i
NM
ND
ND
ND
2.1
745
ND
NM
NM
2.9
ND
ND
ND
ND
2
5.3
ND
1
U/IW*
Ttmndi
tuntrr
NM
NM
NO
NM
ND
NM
NM
NM
17
NM
NM
NM
NM
NM
NM
IS
NM
4.6
NM
NM
NM
NM
NM
NM
NM
2.8
2J
NM
1.5
wi/n
TkfMCti
«8W»
NM
NM
ND
NM
ND
NM
NM
NM
49
NM
NM
NM
NM
ND
NM
ND
NM
4
NM
NM
NM
NM
NM
NM
NM
ND
ND
NM
2
7/7/17
NM
NM
ND
NM
ND
NM
NM
NM
NM
NM
NM
NM
NM
ND
NM
NM
NM
NM
NM
NM
NM
NM
NM
NM
NM
NM
NM
NM
NM
IWJW7
10WW7
NM
NM
ND
NM
ND
NM
NM
NM
8
NM
NM
NM
NM
ND
NM
NM
ND
ND
6
NM
NM
NM
NM
NM
NM
NM
ND
•5
NM
Nl)
V2WM
llHHtt
NM
NM
ND
NM
J
NM
NM
NM
NM
NM
NM
NM
NM
J
NM
J
NM
NM
NM
NM
NM
NM
NM
NM
NM
NM
NM
NM
NM
NM
vxat
Thrown
VUftt
NM
NM
ND
NM
ND
NM
NM
NM
7.3-8.0 "
NM
NM
NM
NM
. ND
NM
ND
1.2
NM
4.0
NM
NM
NM
NM
NM
NM
NM
1.8
3.8-4.7
NM
D
1V7M
ThnMth
II/2M*
NM
NM
NM
NM
NM
NM
NM
NM
NM
NM
NM
NM
NM
ND
NM
NM
NM
NM
NM
NM
NM
NM
NM
NM
NM
NM
ND
3J
NM
Nl)
smm
Thro*.
SWSW
NM
NM
NM
NM
NM
NM
NM
NM
5(IM
NM
NM
NM
NM
ND
NM
NM
ND
1,100 (880)
2J
NM
NM
NM
NM
NM
NM
NM
IJ
NM
NM
U
4/1YW
4/24/W
n
ND
0.6J
550 (1.300)
3
08J
1
T3
O
O
O
(D
-------
PCE CONCENTRATIONS MEASURED IN MONITORING WELLS
PONDKRS CORNER SITK
W
NM
NM
NM
NM
NM
NM
NM
NM
NM
NIJ
ND
ND
ND
ND
ND
NM
NM
NM
NM
HP
NO
ND
NU
ND
ND
NM
NM
NM
NM
Nil
NM
Ni)
NM
NM
ND
NM
NM
NM
NM
NM
J
NM
J
NM
NM
J
NM
NM
NM
NM
NM
ND
NM
D
ND
ND
NM
NM
NM
NM
NM
NM
ND
NR
NM
ND
NM
NM
NM
NM
NM
NIJ
NM
NM
ND
NM
ND
ND
NO
ND
*|ytcceup!ic»!e tiM^sts.
cli*ttraatcd viluc. Compound present but *t tec than the tpccitled detection limit.
dWclls cr«l>,lmc(cJ 2/S7 Ihnxifh 3/87.-
Hr*c%- Units fit |if>t>-
NM •> Not manual.
ND > Not daecied,
!> = Detected, CKX quawifmj
J * KuilnMa! value. Vitac not accurate.
TJ
o
a
to
O
o
-------
to
Souice: CH2M HILL. t9dQa.
•CAtCMHIT
• 40
(PoorQu««yOriglrwt)
Rgur*2
GROUND-WATER MCMttTORtNG
WELL LOCATIONS
PONDERS CORNER SITE
TJ
O
a.
o
o
<0
-------
Ponders Corner
the production wells include wells 20A, 20B, 16A,
16B, 24A, and 24B. All of these wells, except
20B, monitor the Advance Outwash aquifer. Well
20B is screened in the Vashon till, and the
concentrations measured in it are notably higher
than in the other wells. The concentrations in
these wells generally declined markedly only
during the early days of ground-water remediation.
In Well 20B, for instance, the latest measured PCE
concentrations are approximately the same as those
found in the well in mid-1985. (Two
concentrations are given for the same date when
split or duplicate analyses were run.)
Figures 3 and 4 are time-series graphs of the PCE
and TCE concentrations measured in flows from
production Wells HI and H2. Figure 3 shows that
the PCE concentration in well H2 peaked at 492
ppb in September 1984 and that, after an initial
sharp decrease, it has remained fairly stable at
between 30 and 100 ppb since early 1985. The
PCE concentration appears to have risen slightly
during 1989 and to have decreased slightly in
1990. This may have been due to increased
recharge during the rainy season of late 1989 and
early 1990. The PCE concentration in Well HI
seems to show a similar rise and fall during late
1989 and early 1990.
Figure 4 shows that the TCE concentration in both
wells has been consistently near or below detection
limits since late 1985. Small peaks in the TCE
concentration were observed in the first quarters of
1988, 1989, and 1990.
SUMMARY OF REMEDIATION
The ground-water remediation system continues to
meet its primary goal of treating the water
produced from Wells HI and H2 to levels suitable
for public consumption. The zone of capture
created by the two production wells encompasses
the areas of known contamination except for a
small portion of the plume that escaped before the
wellhead treatment system was put into operation.
The PCE concentrations in the production wells
and in the monitoring wells downgradient of the
source area have been essentially stable since the
end of 1985, This persistence of the PCE
contamination appears to confirm the conclusion
that a residual source of ground-water
contamination is impeding aquifer restoration.
This continuing source 9f PCE can probably be
attributed to adsorbed contaminants in the Vashon
till near the Plaza Cleaners, and perhaps also to
PCE that is present as a separate nonaqueous
phase liquid (NAPL) hi that vicinity.
SUMMARY OF NAPL-RELATED
ISSUES
The possibility that PCE or TCE may be present
in the subsurface as NAPLs at the Ponders Corner
site has not been mentioned in any of the site-
related documents. It has been generally
concluded that a residual source is present in the
vicinity of Plaza Cleaners that continues to leach
contamination into the Advance Outwash aquifer.
The source has been attributed to contaminants
adsorbed to the soil particles in the Vashon till.
However, if NAPLs were present in the Vashon
till, they would also represent a source of
continued leaching, and would have a. similar
prolonging effect on the ground-water remediation.
Site records indicate that wastes were discharged
to the ground at Plaza Cleaners in two different
ways. The greatest volume was discharged to the
septic disposal system, which consisted of three
septic tanks and the associated drain field. It is
not clear whether the liquids discharged to the
septic tanks contained nonaqueous solvents or only
dissolved solvents. During the remedial
investigation, both the supernatant liquids in the
septic tanks and the. sludges were sampled. The
maximum PCE concentrations detected were 550
ppb in the supernatant and 483 ppm in the sludge.
The aqueous solubility of PCE is approximately
200 ppm. It was not mentioned that NAPLs were
found in the tanks. However, it was suggested
that the bottoms of the tanks may not have been
impermeable. If no NAPLs were found, it could
be because they had already leaked through the
bottoms of the tanks.
The second means of waste disposal at Plaza
Cleaners was to pour solvent-contaminated sludges
and process waste water on the ground outside the
back door of the plant. Approximately 30 gallons
of liquid waste containing up to 100 ppm of
chlorinated solvents were poured on the ground
per week (U.S. EPA, 1984). Again, it is not clear
whether these wastes included nonaqueous
solvents, but it is likely that at least small amounts
were in NAPL form. It was reported in the record
of decision that a soil sample collected in the
dumping area had a PCE concentration of 3,460
ppm, which suggests that nonaqueous phase
214
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Ponders Comer
1 I §
S
I
I
8
215
-------
Ponders corner
(P
-------
Ponders Corner
liquids were present in the soil. However, the
maximum soil concentration reported from soil
borings and test pits in the area was 3,880 ppb of
PCE (CH2M HEX, 1989b). This level of soil
contamination is somewhat more ambiguous
regarding the likelihood of NAPLs.
The unexpectedly large quantity of PCE recovered
during operation of the soil vapor extraction
system indicates that reliance on soil sampling in
the Steilacoom gravel underestimates the presence
of contaminant This could be because
considerable quantities of solvents passed through
the unsaturated Steilacoom gravel as dense NAPLS
and collected either within lenses of fine sediments
in the Steilacoom or in the underlying Vashon till.
Because the upper portion of the Vashon till is
also unsaturated in this area, solvents in either fine
sediments in the Steilacoom gravel or in the
Vashon till could have contributed vapor to the
soil vapor extraction system. However, the same
could be said for solvents that were simply
adsorbed to the soil matrix in either unit and had
never been present as NAPLs.
Whether the residual source at Ponders Corner
includes NAPLs or is limited to adsorbed
contaminants, the result is to prolong the time
needed for aquifer remediation.
UPDATE BIBLIOGRAPHY/
REFERENCES
CH2M HILL.
EPA-62-ON22.
April 1987. Predesign Report.
CH2M HILL. April 25, 1989a. Draft
Memorandum to Janet O'Hara, EPA Region X, on
Lakewood SVES Summary.
CH2MHILL. December 1989b. Remedial Action
Work Plan, Lakewood RA, Pierce County
Washington.
CH2M HILL. April" 1990a. Sampling and
Analysis Plan, Remedial Action, Lakewood RA.
CH2M HELL. May 21, 1990b. Memorandum to
Ann Williamson, EPA Region X, on Lakewood
RA Monitoring Well Inventory.
CH2M HILL. August 30, 1990c. Memorandum
to Ann Williamson, EPA Region X, on
Groundwater Sampling at Lakewood.
U.S. Environmental Protection Agency (U.S.
EPA). June 1984. Superfund Record of Decision,
Ponders Comer Site, WA (IRM), EPA/ROD/R10-
84/002.
O.S! EPA. September 30, 1985. Record of
De'cision, Remedial Alternative Selection, Ponders
Corner Site.
U.S. EPA. October 1989. Evaluation of Ground-
Water Extraction Remedies: Volume 2, Case
Studies 1-19. EPA/9355.4-03.
217
0*77
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UPDATE OF CASE STUDY 15
Savannah River Site
Aiken, South Carolina
Abstract
Remedial activities since the initial case study include: 1) an increase in the extraction rate
of the existing system; 2) hydrogeologic investigations and the installation of two new
extraction systems near the Savannah River Lab, and south of the main M-Area plume;
3) the installation of a soil vapor extraction system in the M-Area; and 4) further plume
characterization. Since the last case study, the concentration of TCE in the water table
aquifer and parts of the Upper Congaree has decreased, but increases have occurred in the
Lower Congaree and the deepest aquifer, the Black Creek. An additional 28,000 pounds of
solvents were removed in 1990. DNAPLs were identified in 1991. Some areas of the
plume remain beyond the capture zone.
Background Data
Date of Problem Identification
Extraction Started
Types of Contaminants
Primary Aquifer Materials
Maximum Number of Extraction Wells
Maximum Total Extraction Rate
Estimated Plume Area
Estimated Plume Thickness
Maximum Reported Concentrations
1981
September 1985
Tetrachloroethylene
Trichloroethylene
1,1,1-Trichloroethane
Layered sand, silt, and clay
12
550 gpm
1,030 acres
150 feet
Trichloroethylene 223,000 ppb
218
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CASE STUDY UPDATE
SAVANNAH RIVER SITE
BACKGROUND OF THE PROBLEM
INTRODUCTION
The original case study of the U.S. Department of
Energy's (U.S. DOE) Savannah River Nuclear
Weapons Facility in Aiken, South Carolina (U.S.
EPA 1989,"Case Study 15) described remedial
actions addressing contamination of an aquifer
system under the site's manufacturing (M-area)
and administrative areas (A-area) through
December 1988. Figure 1 shows the location of
these areas at the Savannah River site. The
Savannah River site (SIRS) is part of a network of
weapons plants that conducts research and
manufactures products in support of the nuclear
weapons Industry. Contamination was caused by
the disposal of approximately 2.1 million pounds
of volatile organic degreasing solvents into an
onsite settling basin between 1958 and 1982.
Contamination was first identified in June 1981.
Discharges to the settling basin were discontinued
In July 1985 and remedial action began in
September 1985. The plant is operated by
Westinghouse Savannah River Company under
contract to UJS, DOE. Remediation is regulated
by the South Carolina Department of Health and
Environmental Control (SCDHEC).
The formations of interest that underlie the site are
in order of increasing depth, the Bam well Group,
the McBean Formation, the Congaree Formation,
the Ellenton Formation, and the Black Creek
Formation. Before remediation began, the water
table was between 60 and 120 feet below the land
surface within the Bamwell Group and the
McBean Formation.
The Barn well Group is composed of the Upland
Unit, the Tobacco Road Formation,*and the Dry
Branch Formation. The Upland Unit is a poorly-
sorted mix of sand, cobbles, silt, and clay with a
thickness of approximately 57 feet. The Tobacco
Road Formation is a moderate- to well-sorted,
fine-to-medium sand containing some silt, pebbles,
and clay. The Tobacco Road Formation is up to
97 feet thick. The Dry Branch Formation is a
moderate- to well-sorted, medium sand containing
some clay. It is from 30 to 55 feet thick.
The McBean Formation is between 16 and 34 feet
thick, and characterized by moderate- to well-
sorted, fine sand with additional clay and silt
layers. Ground water in the McBean Formation
flows radially outward.
The Congaree Formation is divided into Upper and
Lower units by a clayey intermediate zone. The
Upper level is approximately 60 feet of fine to
medium sand and clay beds. Under natural
conditions, the A/M areas overlie a ground-water
ridge from which ground water flows away to the
east, west, and south. The Lower stratum ranges
from four to 44 feet of moderate- to weE-sorted
sand. Ground water in the lower zone flows in an
easterly and southerly direction.
The Ellenton Formation varies in thickness from
32 to 95 feet and is composed of two major clay
layers separated by poorly-sorted sand. The
bottom layer ranges from 10 to 56 feet thick and
is the principal confining unit for the underlying
Black Creek Formation. The direction of water
flow in the Ellenton is to the southeast.
The Black Creek Formation is composed of poor-
to well-sorted, medium to coarse sands and ranges
from 150 to 180 feet thick. The upper section is
an important production zone for water-supply
wells in the M-area.
Of the 2.1 million pounds of solvents discharged
to the HWMF, some fraction volatilized to the
atmosphere, but a substantial amount is believed to
have percolated downward to the saturated zone.
Using volume-averaging of concentration
information from monitoring wells, the total initial
amount of dissolved organic solvents in the aquifer
was estimated at 260,000 to 450,000 pounds, of
which 75 percent is 1,1,2-dichloroethytene (TCE).
Other major VOCs are tetrachloroethylene (PCE)
and 1,1,1-trichloroethane (TCA).
Before remediation began at Savannah River, TCE
levels as high as 223,000 ppb were detected in
219
-------
Savannah River Site
Savannah
Rh/tr Laboratory
Waatt Managtnwnt
Facility
Source: U.S. DOE, 1986
Figure 1
MAP OF A/HI-AREA
SRS A/M-AREA SITE
AIKEN, SOUTH CAROLINA
220
t,0le77
-------
Savannah River Site
ground water in the M-Area. TCE concentrations
above 100,000 ppb were also observed in the A-
014 outfall and the settling basin. Contamination
was centralized in the McBean and Congaree
Formations with the Ellenton clay layers forming a
partial barrier to downward migration of
contaminants. TCE levels of 756 ppb had also
been detected in the Black Creek Formation.
A contaminant plume beneath the settling basin in
the M-Area is migrating downward. Separate
plumes have been detected in the vicinity of the
Savannah River Laboratory (SRL) and in the
southern sector near the A-014 outfall (U.S. DOE,
1991).
UPDATE ON SITE
CHARACTERISTICS
The update of the case study is based on data
obtained from Westinghouse Savannah River
Company. Data obtained include 1990 permit
modifications to the M-Area Basin, the 1989 and
1990 Annual Corrective Action Reports, a 1990
third quarter summary, air-stripper summaries, and
internal memoranda summarizing site activity since
publication of the original case study. The basic
understanding of site characteristics remains as
described in the original case study.
At the time of the initial case study, site
contamination was not evaluated according to
health-based standards. Since that time, however,
Ground Water Protection Standards (GWPS) were
outlined in the M-Area Modification/Part B Permit
(U.S. DOE, 1990b). These goals, which are based
on EPA's maximum contaminant levels (MCLs)
for organic contaminants, are 5 ppb for TCE and
PCE and 200 ppb for TCA.
REMEDIATION
Design and Operational
Features of the Remediation
System
At the time of the original case study, the stated
contamination cleanup objectives at the A/M Areas
were to minimize horizontal and vertical migration
of contaminated ground water away from source
areas and to remove 99 percent of the
contamination in the aquifer over a 30-year period
(U.S. DOE, 1987). Current SRS operators explain
that this 90 percent figure has never been used as
the basis for a cleanup criterion. The criterion of
removal of 99 percent in 30 years was derived
mathematically to provide a removal curve that is
used as the basis of comparison of each year's
removal data (Westinghouse Savannah River
Company, 1991).
The full-scale remediation system that began
operation in September 1985 consisted of 236
monitoring wells, 11 recovery wells, and a large-
production air stripper near the M-Area buildings.
The locations of the recovery wells and the air
stripper are shown in Figure 2.
The monitoring wells are used to assess the extent
of the contamination and to monitor the
effectiveness of the remediation. These wells are
screened at different depths to track trends in the
potentiometric head and contaminant
concentrations throughout the entire multi-aquifer
system. During 1988, 165 monitoring wells were
sampled.
Four of the recovery wells (RWM-3, RWM-5,
RWM-9, R7/M-11) were designed to be pumped
at 55 gpm while the remaining seven were
designed to be pumped at 25 gpm. As of
December 1988, the average total withdrawal from
the recovery well system was 436 gpm. The
initial case study concluded that this rate could
increase to 725 gpm if the pumps were modified
to operate at full-formation capacity and that
pumping rates were limited only by the capacity of
the air-stripper discharge pump.
Since the original case study was presented, both
minor and major modifications' to the remediation
system have been proposed and elements of the
proposals have been implemented. Minor
modifications consist of increasing the flow of
influent to the air stripper. SRS system operators
have explained that the initial case-study statement
that extraction-well pumping rates were limited by
the capacity of the air-stripper discharge pump was
incorrect; they identify permit restrictions as the
factor responsible for not increasing flow to the air
stripper (Westinghouse Savannah River Company,
1991).
In December 1989, a performance test on the air
stripper system was conducted. System operators
determined that the air stripper could operate
effectively at 500 gpm (U.S. DOE 1990a). In
March 1990, the SCHEDC approved a permit
application allowing Savannah River site operators
to increase flow to the air stripper to as much as
221
9D7
-------
Savannah River Site
Source: U.S. DOE, 19iOa •
Figure 2
RECOVERY WELL LOCATIONS •
SEPTEMBER 19S9
SRS A/M-ARE6 SOT
222
•90fr M77
-------
Savannah River Site
610 gpm. The revised flow was intended to
increase the removal rate of the central plume in
the M-Area. System operators project that
increasing flows to this rate would result in an
atmospheric discharge rate'of 6.7 Ibs/hr (29.5
tons/year), which does not exceed the permitted
atmospheric-discharge limit. Minor design
changes to the system would be necessary to
achieve increased flow rates, including redesigning
distributor trays and improving packing materials.
During 1990, the air stripper removed approxi-
mately 28,000 pounds of solvent from the ground
water. Since September 1985, the system has
removed approximately 203,762 pounds of solvent.
The average inlet water feed rate to the air stripper
in 1990 was 454 gpm (U.S. DOE, 1991). In the
third quarter of 1990, the air stripper logged 446.9
hours of downtime due to stripper upgrade, repair,
and general maintenance. The air stripper was
sampled about once a week for TCE and PCE.
Of the four recovery wells designed to be pumped
at 55 gpm, three operated below capacity at an
average monthly flow during July, August, and
September 1990 of 46 gpm each (RWM 3, RWM
5, RWM 9), and one operated in excess of design
capacity at an average of 65 gpm (RWM 11).
Major modifications include: (1) installation of a
ground-water corrective-action system in the area
of the SRL, (2) further assessment of the geologic
and hydrogeologic conditions in the southern
sector of the M-Area in anticipation of the need
for a remediation system, (3) implementation of a
vadose-zone remediation program,
(4) implementation and completion of the Phase
IV Well Drilling Program, and (5) RCRA closure
of the M-Area Hazardous Waste Management
Facility QlWMF), completed during 1990.
Corrective Action System at SRL
Since the first case study, a separate contaminant
plume in the vicinity of the SRL in the
northeastern A/M Area was identified. This plume
may have been caused by spills or leaks from
solvent storage tanks. In 1990, the facility
conducted an investigation to define the extent of
contamination and institute a remedial system to
remove and treat contaminated ground water from
the SRL complex. Program elements include
source identification, plume definition, and a
remediation system. Source identification consists
of personnel interviews to identify former use
patterns involving degreasing solvents. Plume
definition is contingent on monitoring well data to
define the vertical and horizontal extent of the
plume.
The proposed system is expected to consist of 14
monitoring wells, two recovery wells, and an air
stripper that will discharge treated effluent to the
A-001 outfall. By mid-1990, the 14 monitoring
wells and one recovery well had been installed,
and by November 1990, the SRS had received a
construction permit to install a treatment facility in
the vicinity of the Savannah River Laboratory.
The system was scheduled to begin extraction at a
rate of 70 gpm in June 1991.
Southern Sector of M-Area
Plans are underway to conduct hydrogeological
studies of the southern boundary of the M-Area in
anticipation of additional remedial actions. The
30-year capture zone encompasses the north, east,
and western boundaries of the M-Area plume,
while the southern area remains outside the
influence of the existing recovery system. The
investigation will consist of hydrogeologic
investigation (including well installation, geologic
interpretation, and aquifer characterization), and
remedial action design (including consideration of
alternative technologies). The data derived from
these investigations will be used to implement a
remedial action plan in the southern sector of the
M-Area. The plan .will address recovery well
locations, screen intervals, flow rates, treatment
technology, and disposal methods (U.S. DOE,
1990b). In mid-1990, a recovery well was
installed in the southern sector. In March 1991,
plant operators conducted a 72-hour pump test.
The results of this test will be used to determine
the design requirements of the remediation system
in the area (Westinghouse Savannah River
Company, 1991).
Vacuum-Extraction in the
Vadose-Zone
Based on a pilot program that resulted in the
removal of 1,500 pounds of solvents over a period
of three weeks, SRS proposed a full-scale vacuum-
extraction system to SCDHEC; however, it has not
yet received approval on the RCRA permit
modification (Westinghouse Savannah River
Company, 1991). The remediation plan consists of
five parts: (1) site characterization, (2) well
drilling and installation, (3) system operation, (4)
223
-------
Savannah River Site
performance evaluation, and (5) permitting.
Throughout 1990, vacuum-extraction technologies
were implemented to reduce contaminant levels in
the vadose zone in the A/M Areas. As of
December 1990, 14 soil borings had been drilled,
monitoring wells had been installed in two of these
borings, and two clusters of vadose-zone
monitoring wells and four vadose zone vapor-
extraction wells had been installed.
Phase IV Well Drilling
On September 25, 1989, drilling of the Phase IV
monitoring wells was initiated. The purpose of the
drilling program was to complement the existing
well system in delineating the vertical and
horizontal extent of ground-water contamination
and to determine the potential need for additional
remedial measures. The project was completed in
May 1991. A total of 71 monitoring wells and
two recovery wells were installed (Westinghouse
Savannah River Company, 1991). Figure 3 shows
the location of the Phase II, III, and IV wells.
EVALUATION OF PERFORMANCE
Changes in water quality since the first case study
are evident from a trend analysis of data from 40
monitoring and 11 recovery wells that were tested
during the fourth quarter of 1990. Of the 40
monitoring wells tested, 14 concentrations
exhibited no trend, 24 showed an upward trend,
and 12 displayed a decreasing trend (U.S. DOE,
1991).
Based on analysis of samples from monitoring
wells, TCE is still the most prevalent onsite
contaminant. Both TCE and PCE contaminant
concentrations exceeded the GWPS in 1990.
Contaminant concentrations of TCE increased by
23 percent in the Lower Congaree between the
original case study and the third quarter of 1990.
TCE levels in the Black Creek showed an
increasing trend, averaging 583 ppb between the
last quarter of 1989 and the third quarter of 1990.
TCE concentrations as high as 20,000 ppb were
also detected in a new plume definition well
located west of the M-Area Facilities in the Upper
Congaree. PCE distribution is similar to that of
TCE, but concentrations are generally lower than
those of TCE.
Table 1 lists the concentrations of TCE, TCA, and
PCE for the point-of-compliance (POC)
monitoring wells from the last quarter of 1989 to
the third quarter of 1990. The point-of-compliance
is a vertical surface located at the hydraulically
downgradient limit of the waste management area
and extends down into the uppermost aquifer;
however, the POC wells are screened in the
Congaree. A comparison of these data shows con-
tinued high levels of TCE and PCE in the water
table unit (7,450 ppb TCE and 19,500 ppb PCE).
Although the concentrations of TCE and PCE in
the POC wells continue to decline since the start
of remediation in 1985, in most of the POC wells,
including the two hi the Congaree, concentrations
in excess of the health-based goals were detected.
In the fourth quarter of 1990, TCE was detected in
monitoring wells in the water table unit at a
maximum concentration of 57,000 ppb, in the
Upper Congaree at a maximum of 50,000 ppb, and
in the Lower Congaree at a maximum of 3,290
ppb. Although the Ellenton clay layer generally
impedes movement into the lower units, TCE
continues to migrate into the Black Creek
Formation where maximum concentrations in 1990
(1,980 ppb) were more than double what they
were when remediation began in 1985. These data
are displayed in Figures 4, 5, and 6.
Figure 7 displays the concentrations of TCE and
PCE in the ah stripper influent from September
1985 to December 1990. Since system startup,
plots of PCE and TCE concentrations show
decreasing trends. A review of the average
monthly chlorocarbon concentrations for the fourth
quarter of 1990 in the individual recovery wells in
Table 2 illustrates that the average monthly TCE
and PCE concentrations were highest in the
vicinity of the M-Area buildings (RWM-2 and
RWM-3) and the settling basin (RWM-1).
The expected 30-year zone of capture has not
changed since the original case study was
published. Analysis of monitoring well data,from
1990, however, revealed TCE levels as high as
18,300 ppb west of the acknowledged plume
boundary. Based on data from additional wells in
the vicinity of the SRL, the plume in this area is
greater than that identified in the original case.
The SRL plume extends into the Upper Congaree
where TCE levels as great as 14,800 ppb in this
area have been detected. Figure 8 shows the
location of the suspected source near the SRL and
the predominant ground-water flows from that
source to the southeast through the A/M Areas
(U.S. DOE 1990c). Because remedial action is
224
-------
Savannah River Site
NOTE: ALL UNOf «l***ttB W|UJ
' NflVt MM Mf Pit
Source: U.S. DOE, 1990S
FJgur»3
PHASE II, IH, AND IV MONITOR-WEIJL CLUSURS
(Poor Quality Original) S«s A/M-AREA SITE
225
-------
COMPARATIVE FAJUMETEM KHt CONTAMINANTS OF CONCERN-SAVANNAH HVBX POINT OF COMPLIANCE WELU (pf*>)
Wc«
MSB:
1A
2A
3A
4A
5A
6A
7A
8
13A
13B
ISC
22
Uatt
WtlcrTlbte
WderTibte
Water Title
WilerTible
Waer Trite
WMerTlMc
Water TiHe
WMer Tibte
Lower Conpree
Upper Coo|«ce
Water T»Mc
WcterTtMe
40»
IQW
X)»
3Q»0
DW
458
292
220
314
DW
DW
8
<1.0
10
54
<5.0
15
14
11
15
<1.0
4
50
<1.0
30
15
7450
20
<1.0
5
42
<1.0
22
DW
44
IQ*
JQ»
JQM
DW
20
32
26
22
4Q»
<100
8
DW
DW
4
<1.0
<5.0
<5.0
-------
Savannah River Site
«
\M
\\
' • \\
, 2.1 r
\
1
«'
ffi
^—•^
1
D
1
I
i
is.
227
-------
Savannah River Site
i,1
«• in
• fie
m
I
228
-------
Savannah River Site
229
9D5
-------
35000
I J I i IT F I I I I I I I JT I TT I I I ! I i I I I I I I I 1 I I I I i I I I [ I I I I I I
it II II I I I I I I I I I I I I I i i i
SONDJ FMAMJJA SONDJ FMA M J j AS ON 0J FM AM J J AS ON D J FMAMJJASOHDjFMAMJJASOND
1985 1988 1987 1988 1989 1990
9ourco: U.S. DOE, 1991
Flgurtr
TIME SERIES PLOT OF TCE AND PCE
CONCENTRATIONS IN THE Am STRIPPER INFLUENT,
SEPTEMBER 1985 TO DECEMBER 1990
SRSAAI-AREASITE
V)
§
to
0>
I
CO
-------
rv
Table 2
RECOVERY WELLS AVERAGE MONTHLY CHLOROCARBON CONCENTRATIONS (ppb)
FOURTH QUARTER 1990
Well
Number
RWM-1
RWM-2
RWM-3
RWM-4
RWM-5
RWM-6
RWM-7
RWM-8
RWM-9
RWM-10
RWM-11
October
Degreaser Solvent Concentrations
TCE
(W*)
41,100
25300
17,700
6,210
1,740
8,160
4,170
344
143
6310
4,790
PCE
(W*>
18,800
9,040
4300
686
1,230
7,040
4,890
164
59
15300
512
Total
(M*>
59,900 •
34340
22,000
6,896
2,970
15,200
9,060
508
202
21,610
5,302
November
Degreaser Solvent Concentrations
TCE
(PI*)
42,000
27,100
17,600
6,840
1,980
7^50
4,040
361
171
3,410
4,910
PCE
(PI*)
20300
10,600
5,130
847
1370
5,850
4,440
157
23
5,610
660
Total
(W*)
62300
37,700
22370
7,687
3,350
13,400
8,480
518
194
9,020
5,570
December
Degreaser Solvent Concentrations
TCE
(M*>
44,700
26,200
19,400
6370
1,830
8,540
4,420
416
162
2,930
4,380
PCE
(W*)
21,800
8,770
4,310
587
1,130
6,550
5,810
189
11
5310
329
Total
(PP*»)
66,500
34,970
23,710
6,957
2,960
15,090
10,230
605
173
8,240
4,709
Source: U.S. DOE, 1991
TCE = TricMoroethylene
PCE = Tetrachtoroethylene
to
0
CO
3
to
3"
5
-------
Savannah River Site
still in lue construction stage, it is too early to
assess the effectiveness of remediation in the
vicinity of the SRL. Developing a remediation
program to address this area is important due to
continued contaminant migration into the Black
Creek Formation.
Since September 1985, the system has removed
approximately 203,762 pounds of solvent. An
estimate of mass of solvent contaminants present
in the aquifers has been calculated using
concentration data for each year from startup
through the end of 1989. (To date, an estimate
was not made for 1990 due to the extensive
number of wells.) Estimated mass removed is
calculated as the difference between the estimate
of total mass present in the aquifer in 1989 from
that which was estimated at startup. The total
estimated mass removed through the fourth quarter
of 1989 was approximately 92,000 pounds. The
actual amount removed by the air stripper through
the fourth quarter of 1989 was 175,400 pounds.
The amount actually removed is nearly twice the
estimate of mass reduction. This discrepancy
could be caused by inaccuracy in volume
averaging of the monitoring well data or by the
presence of DNAPLs that were not accounted for
in the calculations.
SUMMARY OF REMEDIATION
Since the original case study, changes at the
Savannah River site include research into
alternative remediation technologies, exploratory
efforts to define the actual extent of site
contamination, and reductions of contaminant
concentrations. System operators acknowledge the
need to assess more completely the actual extent
of site contamination. During 1989 and 1990,
actions were initiated to evaluate the remedial
needs in the SRL and southern sector of the Mi-
Area. To date, preliminary construction has
begun, but it is too early to assess the
effectiveness of these efforts. It is clear from
preliminary data that the plume extends beyond the
zone of influence of the existing M-Area
remediation system.
Since the last case study, efforts, such as the Phase
IV drilling program, were initiated to provide a
better definition of the extent of ground-water
contamination at the site. Alternative in situ
techniques, such as soil vacuum extraction, are
being pursued to supplement the recovery rates of
the extraction wells. These efforts are in various
stages of completion and any evaluation of their
effectiveness at this time is premature.
Although such actions begin to address continued
high levels of contamination and insufficient
definition of the plume, significant progress toward
remedial objectives has not been made since the
original case study. Some reduction hi
contaminant concentrations is evident, particularly
in the Upper Congaree, but the contaminant trends
identified in 1988 were still evident in 1990.
Although contaminants appear to be decreasing in
the water table unit of the Solvent Storage area, in
all other units total concentrations are stabilized at
or increasing from 1988 levels. Plume
concentrations continue to migrate to the Black
Creek formation.
TCE concentrations in air-stripper influent
decreased significantly from approximately 9,000
ppb to below 2,000 ppb between January 1990 and
February 1990. The reason for this decrease was
unknown. TCE concentrations increased hi March
1990 above 12,000 ppb and then decreased and
stabilized to approximately 9,000 ppb by the end
of 1990. PCE influent concentrations stabilized
near 4,000 ppb during 1990. Since the first case
study, the total mass of solvents has decreased.
The mass-inventory reduction total, however, is
below that projected by the 30-year removal
schedule.
System operators defined zones of capture for the
11 recovery wells as that volume of aquifer that
contains all the ground-water flow paths with
travel times of 30 years or less. The original case
study concluded that the actual capture zone would
be smaller than projected due to retardation caused
by partitioning between solid and liquid phases.
In addition, even if the projected capture zone
were achieved, it would still fail to capture
contaminated ground water in the area southeast of
the A/M Area.
Given the low pumping rates, the distance between
wells, and the detection of contamination outside
the expected zone of capture, it is unlikely that
contaminant concentrations will be reduced to
below health-based levels in a 30-year period.
232
-------
Savannah River Site
MSMXt
\
Source: U.S. DOE, 1990s
Figures
(Poor Quality Original) SUSPECTED SOURCE NEAR THE SRL
COMPLEX. IMS
SRS AjM-AREA SITE
233
-------
Savannah River Site
SUMMARY OF MARL-RELATED
ISSUES
In April 1991, SRS operators confirmed the
presence of a DNAPL in one monitoring well,
MSB-3D, near the closed M-Area HWMF (DOE,
1991). The well is located near an abandoned
settling basin where solvents and electroplating
sludges had been discharged. Preliminary organics
analysis indicates that the DNAPL consists of
58 percent PCE, 2 percent TCE, and minor
amounts of chlorobenzene and 1,2-dichlorobenzene
(Westinghouse Savannah River Company, 1991).
The well was installed in September 1990, to
replace the Point of Compliance well, MSB-3A,
which had been dry since 1986. MSB-3D is from
128 to 148 feet deep, near the bottom of the water
table aquifer. In this area, the top of the water
table is at a depth of 130 feet, and a clay aquitard
is at a depth of 150 feet. It is possible that
DNAPLs might be pooling on this clay unit.
During sampling events prior to the discovery of
the DNAPL, maximum recorded concentrations of
570,0d0ppb PCE and 160,000 ppb TCE were
measured in bulk ground-water samples from well
MSB-3D (Westinghouse Savannah River
Company; 1991).
In addition to the direct observation of DNAPLs at
the site, other factors, such as the source
characteristics, the existence of contaminant
concentrations in ground water exceeding 1 to
10 percent of aqueous solubility, and the
persistence of high concentrations despite
remediation, all indicated the potential for DNAPL
contamination.
The highest solvent concentrations in ground water
are found in wells near the M-Area Basin, where
degreaser solvents were discharged in wastewater,
and in wells near the SRL complex, where tank
leaks are suspected (Westinghouse Savannah River
Company, 1991). From these sources, it is
possible that a separate DNAPL phase could have
migrated into the aquifer.
While concentrations of PCE and TCE have
decreased in the water table aquifer since system
startup, they remained high during 1990. In the
fourth quarter of 1990, the maximum concentration
of PCE was 96,000 ppb (64 percent of solubility).
Maximum TCE levels were measured at .57,000
ppb (5.1 percent of solubility). Both maximums
were recorded near the M-Area Basin in
monitoring well MSB-31C. Concentrations
exceeding 10 percent of solubility are another
indication that DNAPLs probably exist near the
M-Area Basin.
In the fourth quarter of 1990, concentrations of
contaminants were lower in aquifers beneath the
water table unit. In the Upper Congaree unit, a
maximum of 50,000 ppb TCE was reported
(4.5 percent of solubility). The high concentration
of TCE suggests that DNAPL might have migrated
to this unit. Concentrations of TCE decrease with
depth. In 1990, maximum reported concentrations
of TCE were 3,290 ppb in the Lower Congaree
unit, 1,820 ppb in the Ellenton Unit, and 1,980
ppb in the Black Creek unit.
Concentrations of TCE in the Black Creek Unit
have been increasing since monitoring began. In
1990, the maximum concentration was 1980 ppb
in well MSB-37. If DNAPLs migrate into this
unit, remediation of the site will become more
difficult. The SRL area has been suggested as the
source of contamination of the Black Creek (U.S.
DOE, 1991).
The SRS has formed a team to address the recent
discovery of DNAPLs at the site. The plan of
action developed by the team is based on three
elements: (1) confirmation of DNAPLs at suspect
locations, (2) development of a system to recover
DNAPLs, and (3) development of a method to
treat or dispose of reclaimed solvents
(Westinghouse Savannah River Company, 1991).
Because of the occurrence of DNAPLs, and the
extent of the contaminant plume, system operators
acknowledge that remediation will be more
extensive than originally estimated.
234
-------
Savannah River Site
UPDATE BIBLIOGRAPHY/
REFERENCES
Litherland, Susan T., and David W. Anderson.
November 1990. The Trouble with DNAPLs. In
Hazardous Materials Control Research Institute,
Proceedings of the llth National Conference.
Mercer, J. W., and R, tyt. Cohen. February 1990
in-press. Transport of Immiscible Fluid in the
Subsurface. Journal of Contam. Hydrol.
Schwille, F. 1984. Migration Organic Ruids
Immiscible with Water in the Unsaturated Zone,
Pollutants in Porous Media. In The Unsaturated
Zone Between Soil Surface and Ground Water.
New York: Springer-Verlag.
U.S. Department of Energy (U.S. DOE). July
1986. Application for a Post-Closure Permit, A/M
Area Hazardous Waste Management Facility,
Volume III, Revision No. 1, Savannah River Plant.
U.S. DOE. February 1987. Effectiveness of the
M-Area Ground-Water Remedial Action Program:
September 1985-Septernber 1986, Savannah River
.Plant.
U.S. DOE. March 1990a. Savannah River
Project. M-Area Hazardous Waste Management
Facility Post-Closure Care Permit, Ground-Water
Monitoring and Corrective Action Program, 1989
Annual Report.
U.S. DOE. September 1990b. Savannah River
Project. Modification of M-Area Basin and
Vicinity Hazardous Waste Management Facility
Post-Closure Care Part B Permit Application.
U.S. DOE. , November 1990c. Savannah River
Project. M-Area Hazardous Waste Management
Facility Post-Closure Care Permit, Ground-Water
Monitoring and Corrective Action Program, 1990
Third Quarter Report.
U.S. DOE. March 1991. Savannah River-Project.
M-Area Hazardous Waste Management Facility,
Post-Closure Permit, Groundwater Monitoring and
Corrective Action Program. 1990 Annual Report.
U.S. Environmental Protection Agency (U.S.
EPA). October 1989a. Evaluation of Ground-
Water Extraction Remedies: Volume 2, Case
Studies 1-19. EPA/9355.4-03.
U.S. fiPA. May 1989b. Dense Nonaqueous Phase
Liquids. Paper presented at Regional Superfund
Ground-Water Forum, Superfund Forum Issue.
Westinghouse Savannah River Company.
December 14, 1990; January 2, 1991; February 5,
1991; June 4, 1991; June 5, 1991. Personal
communication with Chris Bergren,
Hydrogeologist, Savannah River Plant, Aiken,
South Carolina.
Westinghouse Savannah River Company. May 13,
1991; May 24, 1991. Letters from Chris Bergren,
Hydrogeologist, Savannah River Plant, Aiken,
South Carolina.
Westinghouse Savannah River Company.
January 7, 1991. Update memorandum on A/M
Area Corrective Action Program from Charles C.
Sherman, Manager, Environmental Restoration and
Groundwater Section, Environmental Protection
Department.
235
0*77
-------
UPDATE OF CASE STUDY 16
Site A
South Florida
Abstract
During 1990 and 1991, extraction and air stripping of ground water has continued at the
site. Vinyl chloride, now the primary contaminant of concern, has remained at levels
exceeding health-based standards. In early 1991, the EPA initiated a remedial investigation
that included soil borings, the installation of additional monitoring wells along the southern
boundary of the site, and the sampling of all wells at the site.
Table of Background Data
Date of Problem Identification
Extraction Started
Types of Contaminants
Primary Aquifer Materials
Maximum Number of Extraction Wells
Maximum Total Extraction Rate
Estimated Plume Area
Estimated Plume Thickness
Maximum Reported Concentrations
1985
August 29, 1988
Benzene, chlorobenzene,
1 ,4-dichlorobenzene,
trans- 1,2-DCE, and vinyl chloride
Sand, limestone
1
50 gpm estimated, actual rates have been
around 38 gpm
0.7 acres
15-25 feet
benzene 36.0 ppb
chlorobenzene 370.0 ppb
vinyl chloride 86.0 ppb
1,4-dichlorobenzene 170.0 ppb
trans- 1,2-DCE 7200.0 ppb
236
-------
CASE STUDY UPDATE
SITE A
BACKGROUND OF THE PROBLEM
INTRODUCTION
The original case study of Site A1 in south
Florida (U.S. EPA, 1989, Case Study 16),
presented data about the onsite ground-water
extraction system through March 1989. The
company at the site has produced industrial
cleaning compounds since 1958. A map of the
site is shown in Figure 1. Contamination is
caused by chlorinated organics and aromatic
compounds that are concentrated in the south-
central area of the site. Investigation into the
extent of contamination began in 1985, and the
extraction system began operating in August 1988.
The site is managed by a potentially responsible
party (PRP), with administrative oversight from
the local county government.
Underlying Site A is the Biscayne Aquifer, the
sole source of potable water for the county. The
aquifer lies below a one-foot thickness of sandy
organic topsoil and is composed of four geologic
units. The first is a 15- to 25-foot-thick layer of
sandy oolitic limestone with high vertical and
horizontal conductivity from solution openings.
Below the limestone is a 20-foot layer of fine to
medium grained quartz sand. Underneath the sand
is the Fort Thompson Formation, a 45-foot thick
unit of limestone, which is the most productive
layer in the Biscayne aquifer. The base unit of the
aquifer is the Tamiami Formation, a regional
confining unit comprising sand, silt, clay, and
shell. Beneath the Biscayne aquifer lies the
Floridan aquifer, which in this area contains
brackish water.
The site is contaminated by trie organic
compounds benzene, chlorobenzene, 1,4-
dichlorobenzene, trans-l,2-dichloroethylene (trans-
1,2-DCE), and vinyl chloride. Figure 2 shows the
location of the monitoring wells and the
contaminant plume as originally designated by the
PRP. The PRP contended, that contamination was
confined to the upper 15 to 25 feet of the Biscayne
Aquifer and extended no more than 100 feet in
any direction from the extraction well. However,
the original case study identified two monitoring
wells (MWT-32 and MWS-09) outside the
boundaries of the designated plume that had
Contaminant concentrations above the aquifer
remediation goals.
As of March 1989, concentrations of benzene,
chlorobenzene, and vinyl chloride were still above
cleanup standards in the contaminant plume
identified by the PRP and in two monitoring wells
outside the northern boundary of the designated
plume.
The PRP also asserted that contamination is
limited to the upper 15 to 20 feet of the Biscayne
dquifer. Contamination levels above allowable
standards, however, were detected at depths of 55
feet in monitoring well CDM-03 located within the
designated plume.
UPDATE ON SITE
CHARACTERISTICS
Site data for this update included 1990 monthly
progress reports for the temporary air stripper and
monitoring wells. Personal communication with
the county oversight agency and EPA regional
staff supplemented the technical status reports. In
the interim since the initial case study, the PRP
remained responsible for site cleanup, while the
county agency continued to exercise oversight of
cleanup progress. In addition, the state District
Court granted a request from the EPA to conduct a
remedial investigation at the site.
As reported hi the original case study,
concentrations of benzene were still higher than
the cleanup goal of 1 ppb in monitoring Wells
CDM-02 and MWS-11 in mid-March 1989. Since
that date, ground-water sampling has been reported
for only five monitoring wells: CDM-02, MWS-
06, MWS-11, DERM-05, and DERM-06. All of
these wells are approximately 20 feet deep, except
Well DERM-05, which is only 10 feet deep. All
of 'the sampling results reported for these wells
since March 1989 have shown benzene
concentrations below the cleanup standard.
Vinyl chloride was detected at concentrations
above the 1 ppb cleanup goal in Wells CDM-02,
237
-------
Site A
V
f
/
ii
Hi
O i
i
I
O m
£ I
S *
238
-------
VO
MWS-tSA f MCW2ROUNOAT
WAUO-HMWC
-*- wet-
* MONTDNWELL
POSSOLECXTBH-OF
CONTAINMB4T PLUME
EXTENT OF CONTAHHA1KM
ESrUWTEDBYWIP
Source Private Contractor, 1987
Scale in Feet
Figure 2
fPoor Quality OrtalnalV SITE A MONITORWG WELL LOCATIONS
1 ^ ' AND CONTAMiNANT PLUME PROJECTIONS
CO
p7
-------
Site A
DERM-05, and DERM-06 in three of the four
sampling rounds reported in 1990. Concentration
levels were greatest in two monitoring wells
(DERM-05 and DERM-06) adjacent to the
extraction well. Table 1 lists the vinyl chloride
concentrations in these wells since the extraction
system began operation. The PRP believes that
the vinyl chloride in these wells is migrating from
offsite sources (Private Contractor, 1990a).
It should be noted that the ground-water sampling
has been conducted without regulatory oversight.
REMEDIATION
Design and Operational
Features of the Remediation
System
The original goal of remedial actions at Site A was
to reduce the concentrations of VOCs in the south-
central area of the site to levels meeting health-
based standards within 60 days. The remediation
system consists of monitoring wells, a single
extraction well in the center of the contaminated
area, and an air stripper that discharges to the city
.sewer system.
During the first three quarters of 1990, pump
malfunctions and maintenance of the air stripper
caused minor disruptions in remediation. The air
stripper was out of service several times between
January and October 1990. The first time
occurred between February 22 and March 23 when
the well pump and motor failed after the air
stripper underwent a routine cleaning. This
resulted in 674 inoperable hours during which the
air stripper influent and effluent were not tested
(Private Contractor, 1990a). A second shutdown
of 111 hours occurred between April 7 and April
11, 1990, and was caused by an inoperable pump
motor (Private Contractor, 1990c). Additional
shutdowns, lasting less than 8 hours each, occurred
in July and September, when the packing media in
the stripping tower were cleaned.
Having recently received authority to enter the
site, the ElPA has initiated a new remedial
investigation that will include soil borings at
documented onsite seepage pits, and the
installation of additional monitoring wells along
the southern, boundary of the site (U.S. EPA,
199Ib). The results of these field activities will be
used to determine the actual extent of the
contaminant plume, and the presence or absence of
dense nonaqueous phase liquids (DNAPLs) (U.S.
EPA, 1991a). As of May 1991, the data from the
studies had not been released. These studies may
result in future modifications to the remedial
system.
EVALUATION OF SYSTEM
PERFORMANCE
No water-level measurements have been reported
for this site that could be used to judge the
effectiveness of the extraction well in capturing the
contaminant plume. As mentioned in the original
case study, the extraction system operators
reported that the onset of pumping produced "no
measurable differences of water levels" in the
monitoring wells. No further information on the
hydraulic effectiveness of the extraction well has
been given in the periodic status reports submitted
by the operators.
All contaminants except for vinyl chlorine have
reached clean-up goals as measured in the influent
to the air stripper. During 1990, the
concentrations of benzene and chlorobenzene that
were detected in three monitoring wells in 1989
were brought within health-based standards.
Contaminant levels of vinyl chloride, however,
continue to appear in three of the five monitoring
wells in the area of the extraction well. Despite
substantial declines in concentrations since 1988,
vinyl chloride continues to be detected in levels
higher than the cleanup-goal of 1 ppb.
The air stripper continues to function effectively in
removing VOCs present in influent. Table 2 lists
the cumulative volume of ground water treated in
the first three quarters of 1990. Since system
start-up, the air stripper has removed
approximately 15 pounds of VOCs.
Figure 3 shows the variation in concentrations of
the five principle contaminants measured at the
influent sampling point of the air stripper over the
period of remediation.
In the original case study, total VOCs in air
stripper influent were reported to be at
concentrations above 10,000 ppb for the first 10
days after start-up. The highest total VOCs
concentration, 24,001 ppb, was recorded on
240
-------
Site A
Table 1
CONCENTRATIONS OF VINYL CHLORIDE IN THREE SITE A MONITORING WELLS
(Ppb)
t
Date
8-29-88
9-28-88
10-28-88
11-27-88
12-27-88
1-26-89
2-25-89
3-27-89
4-26-89
5-26-89
6-25-89
7-25-89
9-26-89
2-28-90
6-20-90
7-26-90
10-17-90
Days after
Startup
0
30
60
90
120
150
180
210
240
270
300
330
393
548
660
696
779
Monitoring Wells
CDM-02
6.70
13.00
12.00
19.00
6.00
BCG
BCG
1.10
BCG
BCG
BCG
BCG
BCG
BCG
5.80
6.40
1.40
DERM-05
100.00
94.00
8.70
14.00
5.00
27.00
18.00
BCG
15.00
27.00
44.00
28.00
NS
32.00
BCG
6.10
8.30
DERM-06
19.00
7.50
5.00
3.60
11.00
8.70
6.20
BCG
29.00
12.00
29.00
28.00
NS
25.00
BCG
5.70
7.80
Vinyl chloride contaminant goal reduction level = 1 ppb.
BCG = Below cleanup goals.
NS = Not sampled.
241
-------
Site A
1200
Sum of Rva Contaminants
Benzene
Chtorobenzene . '
1,4 Dfchtorobenzene
trans 1,2-DOE
Vinyl Chloride
8-88 12-88 3-89 6-89 1049 1-90
4-90 7-90 11-90 2-91
Source: Private Contractor, I990e
Figure 3
TEMPORARY AIR STWPPBt INFLUENT
CONTAMINANT CONCENTRATIONS AT SITE A
FROM AUGUST 1988 TO OCTOBER 17,1990
242
IQA3
-------
Site A
Table 2
TEMPORARY AIR STRIPPER DATA
Water Treated
(Cum. Gallons)
Treatment Rate
(gpm)
Well Discharge
Pressure (psig)
Blower Discharge
Static Pressure
(in. of water)
3-90
25,872,800
37.5
43
3.5
4-90
27,062,500
38.1
43
3.9
7-90
32,319,979
38.5
36
6.9
10-90
36,860,670
37.7
44
5.6
Source: Private Contractor, October 1990e
August 29, 1988, the date of start-up. However, in
more recent tables of contaminant conceritraBbns
at the air stripper, total VOCs were indicated to be
the sum of only 5 VOCs, and total VOCs
concentration at start-up was reported at just 7,692
ppb. No explanation has been given for this
change in the reported startup concentration.
However, examination of the early monitoring
records shows that the total VOC concentrations
were typically more than three times higher than
the sum of the concentrations for the five VOC
compounds listed individually. This seems to
indicate that other unidentified compounds were
present. In the more recent reports, the total VOC
concentrations listed are simply the sum of the five
compounds of concern.
As of October 1990, the concentrations of all
contaminants except benzene and vinyl chloride
had fallen below cleanup goals in the stripper
influent. The October benzene and vinyl chloride
concentrations were 2 ppb and 13 ppb,
respectively.
SUMMARY OF REMEDIATION
As of October 1990, the extraction system had
been in operation for approximately 800 days, and
reduction of vinyl chloride concentrations to the
cleanup goal had not been achieved. For other site
contaminants, the process of decreasing
concentrations to acceptable levels has taken as
much as 9 months since system startup. The
extraction system designers had expected to
remediate the site in 60 days using a model-based
pumping rate of 30 gpm. After startup, the
pumping rair* was increased to 50 gpm because the
model had shown that cleanup goals could be
achieved faster with higher pumping rates.
Ground-water restoration goals were not achieved
in the projected 60-day period. However, after
more than 2 years of extraction, the concentrations
of four of the five contaminants of concern have
apparently been reduced to meet cleanup goals in
the five monitoring wells being sampled. Vinyl
chloride was still above the cleanup goal in three
of the wells.
SUMMARY OF NAPL-RELATED
ISSUES
After further field investigations in the spring of
1991, the U.S. EPA has not confirmed the
presence of a DNAPL phase at the site. Recent
soil borings have identified on-site seepage pits as
a possible source of contamination (U.S. EPA
Staff, May 10, 1991b).
During earlier site investigations, the presence of
compounds such as TCE and trans-l,2-DCE
indicated the potential for DNAPLs. However, the
groundwater concentrations of these compounds
have been reduced to health-based standards
during 1989 and 1990:
243
-------
Site A
The EPA, however, speculates that these
reductions may be caused by dilution of
contaminated water with uncontaminated water,
and that decreases in contaminant levels do not
indicate that future remedial actions should not
include an assessment of DNAPLs (U.S. EPA
Staff, May 10, 1991b). The EPA has begun
preliminary fieldwork at Site A that will culminate
in a remedial investigation/feasibility study
characterizing the type and extent of contamination
in the source area, including possible remedial
actions that address DNAPLs. No data from the
study has been released as of May 1991.
UPDATE BIBLIOGRAPHY/
REFERENCES
County Environmental Agency Staff. November
1990, Personal communication.
Private Contractor. September 1987. Provisional
Remedial Action Plan, Site A.
Private Contractor. March 26, 1990a. Site A
Temporary Air Stripper Monthly Status Report.
Private Contractor. April 16, 1990b. Site A
Temporary Air Stripper Monthly Status Report.
Private Contractor. April 27, 1990c. Site A
Temporary Air Stripper Monthly Status Report.
,',,„:' * ," ,i !
Private Contractor. August 16 1990d. Site A
Temporary Air Stripper Monthly Status Report.
Private Contractor. October 31, 1990e. Site A
Temporary Air Stripper Monthly Status Report.
U.S. Environmental Protection Agency (U.S.
EPA). October 1989. Evaluation of Groundwater
Extraction Remedies: Volume 2, Case Studies 1-
19. Document Number EPA/9355.4-03.
U.S. EPA Staff (Region IV). February 19, 199la.
Personal communication.
U.S. EPA Staff (Region IV). May 10, 1991b.
Personal communication.
l.The true identification of Site A will remain confidential because of continuing
controversy regarding site-management responsibility and its inclusion on the National
Priorities List (NPL).
244
IOC3
-------
UPDATE OF CASE STUDY 17
Utah Power & Light
Idaho Falls, Idaho
Abstract
Since the original case study, pumping and treatment of ground water at the site has
continued. Concentration of PAHs in the influent to the treatment system has decreased
substantially since remediation began. However, because of the presence of free phase
creosote, it is unlikely that the aquifer will be restored to health-based levels in the
foreseeable future using the current extraction system.
Table of Background Data
Date of Problem Identification
Extraction Started
Types of Contaminants
Primary Aquifer Materials
Maximum Number of Extraction Wells
Maximum Total Extraction Rate
Estimated Plume Area
Estimated Plume Thickness
Maximum Reported Concentrations
1983
October 1985
Creosote
Alluvium and fractured basalt
17
200 .gpm
8-10 acres
175 feet
Mean maximum concentrations
Pyrene 1,776 ppb
Naphthalene 8,600 ppb
Phenanthrene 4,522 ppb
245
IOD3
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CASE STUDY UPDATE
UTAH POWER & LIGHT POLE TREATMENT YARD
BACKGROUND OF THE PROBLEM
INTRODUCTION
This report describes progress in ground-water
remediation at the Utah, Power & Light (UP&L)
site from March ll 89 to 'March '"1990'. It is an
update of the original case study of site
remediation, which was based on information
through March 1989 (U.S. EPA, 1989, Case
'Study 17).
The UP&L pole treatment yard is located in Idaho
Falls, Idaho, near the east bank of the Snake River
(see Figure 1). The facility was used to treat
wooden poles with creosote from the early 1920s
through mid-1983. As a result of creosote leaks
from underground piping, the soil and bedrock
underlying the facility have become contaminated.
The site is administered by the Idaho Department
of Health and Welfare, Hazardous Materials,
Bureau, now that Idaho has become an RCRA-
authorized state.
The contamination was first detected in July 1983
when a creosote leak was found in the
underground piping between the treatment and
storage'vats at the facility. In response to this
discovery, soil and rock were excavated from a
large pit down to the surface of the basalt bedrock
to a depth of approximately 25 feet. However,
borings into the bedrock showed that the bedrock
was contaminated with free-phase creosote below
the bottom of the pit. The pit was backfilled with
compacted clay and clean gravel in 1984 and
1985, and was later classified as an RCRA
hazardous waste management facility (HWMF).
Additional soil and rock borings were drilled and
15 ground-water monitoring wells were installed in
1984 and 1985 to further 'assess the lateral and
vertical extent of die site contamination.
A preliminary piloVscale ground-water extraction
~and treatment system was operated at the site from
October 1985 through April 1986. More than
expected free-phase creosote was produced from
pumping the monitoring and recovery wells during
this first pilot test. As a result, starting in
February 1987, a second pilot test was conducted
that used an improved treatment system and wells
specifically designed for extraction. Since then,
the ground-water extraction and treatment system
has been operated continuously.
The site is near the eastern edge of the Snake
River Plain in a geologic region characterized by
basalt lava flows. The surface soils consist of 3 to
5 feet of loess underlain by 20 to 30 feet of sand
and gravel. These deposits are underlain by a
series of basalt lava flows separated by interflow
deposits of clay, gravel, and cinders. The
thickness of these basalt flows is known to exceed
1,600 feet near the site; however, borings extend
to a maximum depth of only 400 feet at the site
itself. The basalt flows at the site are referred to
as Basalt A through Basalt E in the site
documentation.
The three aquifer zones at the site occur within
interflow zones and within fractures in the basalt.
The uppermost aquifer zone at the site is
Aquifer No. 1, which occurs between depths of
approximately 110 to 160 feet below land surface,
and is most permeable between the water table and
160 feet. The transmissivity of Aquifer No. 1 has
•been measured at between 1,100 and
950,000 gallons per day per foot (gpd/ft). The
hydraulic properties of the aquifer are highly
direction-dependent and spatially non-uniform.
Aquifer No. 1 is unconflned.
Aquifer No. 2 is a confined aquifer that occurs
within the weathered basalt and interflow zone
near the bottom of Basalt B and the top of
Basalt C, between approximately 240 and 260 feet
below land surface. The transmissivity of Aquifer
No. 2 has been measured at between 20,400 and
30,400 gpd/ft. Hydraulic properties are spatially
and directionally more uniform in Aquifer No. 2
than in Aquifer No. 1. Aquifer No. 3 is within
interflow and fracture zones occurring at depths of
360 to 400 feet. The original case study reported
that Aquifer No. 3 was expected to be highly
transmissive, based on specific capacity results.
The water table is over 100 feet below land
surface. The water table elevation fluctuates
seasonally with an amplitude of approximately
246
IOC 2 60k 77
-------
Utah Power & Light
UPiL POLE YARD
Source: CH2M HILL, 1987
{poor Quality Original)
Figure 1
SITE LOCATION
UTAH POWER 4 LIGHT STO
IDAHO FALLS, IDAHO
247
1083
-------
25 feet. The hydraulic head in Aquifer No. 1 is
approximately 2 to 3 feet greater than the head in
Aquifer No. 2, which, in turn, is approximately 2
feet greater than the head in Aquifer No. 3. The
average downward seepage velocity between
Aquifer Nos. 1 and 2 has been estimated at
approximately 20 feet per year, based on an
effective porosity of 6.1. Within Aquifer Nos. 1
and 2, horizontal flow is generally towards the
southwest.
Creosote is the contaminant of concern at the
UP&L site. Creosote is a distillate of coal tar that
has been shown to contain up to 400 individual
compounds, most of which are classified as
polycyclic aromatic hydrocarbons (PAHs). The
viscosity of creosote is 50 to 70 times greater than
water. Most of its individual components have a
low solubility in water and a low mobility in
solution.
The contamination at the site is in the form of
both dissolved constituents and free-phase
creosote. Creosote was found in several borings
through the bedrock at the base of the pit
excavated in 1983. No creosote was found in the
surficial gravel overlying the bedrock. In general,
creosote contamination has been observed in wells
south and southwest of the former excavated pit.
Monitoring Wells MW-7, MW-8, and MW-13, and
recovery Wells R-4, R-5, and R-6 were considered
to be within the plume of contaminated ground
water in Aquifer No. 1 in 1986. Monitoring Well
MW-9 and recovery Well R-7 were near or within
the contaminant plume in Aquifer No. 2 in 1986.
No contamination was found within Aquifer No. 3
in 1986.
UPDATE ON SITE
CHARACTERISTICS
The information on the history, geology, waste
characteristics, and administration of the site
presented in the original case study remains
current. More specific estimates of the
transmissivity of Aquifer No. 3 are now available.
These estimates range from 1,500,000 to
11,200,000 gpd/ft based on aquifer pump tests and
an assumed aquifer thickness of 300 feet (Dames
& Moore, 1988). More complete information on
site characteristics can be found in the original
case study.
Utah Power & Light
REMEDIATION
Design and Operational
Features of the Remediation
System
The main objective of the UP&L remediation
system is to contain the contaminated ground
water vertically and horizontally using a system of
extraction wells. The system of monitoring and
recovery wells in place in March 1989 is shown in
Figure 2. A secondary objective is to remove
free-phase creosote where practical. The
extraction system was designed on the basis of
numerical modeling results and onsite performance
experience, and consists of 11 extraction wells in
Aquifer No. 1, and 6 extraction wells in
Aquifer No. 2. Each of the monitoring and
recovery wells in the extraction system has been
operated during select periods since late 1985.
The selection of pumping wells and the total rate
of extraction is constrained by limitations in the
productivity of Aquifer No. 1, and the desire to
limit the downward gradient induced by pumping
in Aquifer No. 2.
The recprd of recovery well operation from late
1985 through March 1990 is shown in Figure 3.
Figure 3 shows that 7 recovery wells in
Aquifer Nos. 1 and 6 recovery wells in
Aquifer No. 2 have operated intermittently since
March 1989. One change in the extraction system
is in the operation of recovery well RW-11, which
was installed before March 1989, but did not
operate until July 1989. No other system changes
were reported since the original case study. The
extraction system is currently in operation;
however, no specific operational data were
available for March 1990 through June 1991.
Figure 4 shows the combined average monthly
pumping rate of the extraction system from
January 1988 through March 1990. Since March
1989, the system has been pumped at an average
rate of approximately 139 gpm or 200,000 gallons
per day. The operational mix of individual wells
that made up the total pumping rate of 139 gpm
was quite variable during that period, as shown in
Figure 3. The selection of individual pumping
rates was based on initial computer modeling
results and the constraints mentioned above.
248
-------
Utah Power & Light
Source: Dames & Moors, 1989a
{Poor Quality Original)
EXTRACTION AND MONITOR INO
WELL SYSTEM, MARCH 1989
LfTAH POWER & UQHT SITE
249
-------
to
Ul
o
-4
-4
i
- i
1
M
d
MW-7
MW-8
R-1
R-4
R5
R-6
R-11
R-1 2
B-1
C-1
MW-9
R-2
R-7
R-8
R-9
R-10
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i 1 1 1 1 1 1 1 1 1 1 1 1 Ii 1 1 1 1 1 1 1
JFMAMJJ ASONIJFMAMJJ ASOND
1985 1988
I- " 1 P»riog op*raJtoo»t periods.
Br saks in tipsr alion of toss dun 4 days ara not shown.
Flour* 3
RECORD OF RECOVERY WELL OPERATION
NOVEMBER 1985 THROUGH MARCH 1890
UTAH POWER & LIGHT SITE
0
3"
13
O
I
-------
o
-4
IDAHO FALLS POLE YARD
Well Output
160
140
120
100
80
60
40
20
0
G.P.M.
JFMAMJJASONDJFMAMJJASONDJFM
I I 1988 I 1989 I 1990 I
Average Monthly Flow
Figure 4
COMBINED AVERAGE MONTHLY PUMPING
RATE OF EXTRACTION SYSTEM
JANUARY 1988 TO MARCH 1990
UTAH POWER AND LIGHT SITE
I
TJ
I
-------
EVALUATION OF PERFORMANCE
Since system startup in late 1985, the zones of
hydraulic capture within Aquifer No. 1 and
Aquifer No. 2 have varied because of changes in
the pumping rate and well locations. Figure 5
shows the potentiometric surface in Aquifer No. 1
on May 22, 1990. This figure shows a change in
the overall pattern of horizontal flow from that in
the original case study (not shown), but the limits
bf the zone of capture do not appear to differ
substantially. The system did appear to capture
ground water on the southern boundary of the site
near MW-16 more effectively in May 1990 than in
January 1989. Data on the distribution of
contamination in May 1990 were not available for
Comparison to the zone of capture. Only four
wells in Aquifer No. 1 were sampled in the first
quarter of 1990 (C-l, R-5, R-6, and R-ll). All
were within the zone of capture. Only R-5 arid
R-ll were found to be contaminated.
Figure 6 shows the potentiometric surface in
Aquifer No. 2 on May 22, 1990. This figure does
not show a substantial change in the limits of the
zone of capture created by the extraction well
network from that in the original case study (not
..shown). Water level data in Figure 6 suggest
some increase in the rate of ground-water flow to
the extraction wells, but the increase may be due
to variations in the graphical contouring of the
data. All the wells found to be contaminated in
the first quarter of 1990 were within the zone of
capture in Aquifer No. 2. However, the available
concentration data are from wells close to the
HWMF, so the extent to which the extraction
system captures all the contaminated ground water
cannot be estimated.
Figure 7 shows the time series concentration of
total PAHs in the influent to the treatment system
from February 1988* through March 1990. This
figure shows that influent concentrations have
decreased substantially since early 1989.
Concentration peaks, believed to be the result of
extracting slugs of free-product creosote, have
been less than 300 ppb since early 1989, in
contrast with peaks of greater than 50,000 ppb in
early 1986. The magnitude and variability of the
concentrations of total PAHs have decreased
substantially since the start of remediation in late
1985. The magnitude and variability of the
concentrations of total phenols (not shown) have
also been reduced.
Utah Power & Light
SUMMARY OF REMEDIATION
As stated hi the original case study, it is difficult
to evaluate the effectiveness of the remediation
system because of the complex fractured rock
aquifer system and the presence of free-product
creosote. In fractured rock aquifers, aquifer
properties such as hydraulic conductivity tend to
be anisotropic, making flow difficult to analyze.
The full extent of the plume is also difficult to
assess because of the limited number of offsite
monitoring wells. Piezometric surface maps of
Aquifer Nos. 1 and 2 suggest that dissolved
contaminants from the areas of known ground-
water contamination were being captured by the
extraction network hi Aquifer Nos. 1 and 2 in
mid-1990. However, hydraulic gradients may not
influence the movement of dense free-product
creosote. Pumping operations aimed at
minimizing downward flow gradients have not
been entirely successful. Creosote may tend to
migrate downward through bedrock fractures
because of its high density, even if hydraulic
gradients favor upward flow.
Since remediation began in 1985, the concentration
of total PAHs in the influent to the treatment
system has decreased substantially. There are still
strong concentration peaks of total PAHs, believed
to be caused by slugs of free-product creosote
being drawn into the extraction system, but the
magnitude of these peaks has decreased sub-
stantially since remediation began. The
remediation system is clearly removing both
dissolved constituents and free-product creosote
from the subsurface. However, because of the
presence of creosote, it appears unlikely that the
aquifer can be restored to health-based levels with
the current system. Because of the density of
creosote, it may also be difficult to achieve
vertical containment of the contamination.
SUMMARY OF NAPL-RELATED
ISSUES
The presence of dense nonaqueous phase liquid
(DNAPL) creosote at the UP&L site has been
proven by direct observation. During the drilling,
drilling rods smeared with creosote were pulled
from several boreholes. Slugs of creosote have
also been observed in wells. The total mass of
252
(OD7
-------
Utah Power & Light
N
f «*• \\ V V.
• AQUIFER HO. 1 LOCATION
ELEVATION CONTOUR OF POTENTOMETRIC
SURFACE ASSOCIATED WTO AQUIFER NO, 1
IDEALtZEaOROUNO WATER
*~ FLOW PATH
Source: Dames & Mobra, 1990
Figures
(Poor Quality Original) POTENTIOIIETRJC SURFACE IN
AQUIFER NO. 1 ON MAY 22, 1990
UTAH POWER * LIGHT SITE
253
-------
Utah Power & Light
N
V
V
\
\
A AQUIFER NO. 2 LOCATION
ELEVATION CONTOUR OF POTENTIOMETRIC
SURFACE ASSOCIATED WITH AQUIFER NO. 2
IDEALIZED GROUND WATER
*" FLOW PATH
M* • M*
' • • ' • ' ''
SCALE N FEET
Source: Dames & Moore, 1990
Flgurt 6
(Poor Quality Orlglral) POTENTIOIETRIC SURFACE IN
AQUIFER NO. 2 ON MAY 22,1990
UTAH POWER 4 UQHTSrrE
254
J0C7
-------
u»
€*•%
IDAHO FALLS POLE YARD
Total PAHs
2000
1500
1000
ug/l
500 -
Apr Jul Aug Jan Mar May Juh Jul Aug Oct Nov Jan Mar
II 1988 i 1989 I 1990 I
Influent
Effluent
Influent - Combined Input From Wells
Effluent - Treated Discharge From Plant
Figure 7
CONCENTRATE OF TOTAL PAHs IN THE
INFLUENT TO THE TREATMENT SYSTEM
FROM FEBRUARY 1988 TO MARCH 1990
UTAH POWER & LIGHT SITE
i
ea
3"
-------
creosote that was released to the subsurface
through the leak in the underground pipe and from
other sources is not known. Some residual
contamination was removed during excavation of
the soils overlying the bedrock, but it is possible
that a substantial portion of the total mass of
creosote is still present in the vadose zone and the
fractured rock. Because creosote is slightly denser
than water (its specific gravity is 1.05 to 1.09), it
is expected to sink into the subsurface. Because
capillary forces are reduced in fractures, where the
surface area to volume ratio is low, DNAPLs tend
not to adsorb onto fracture surfaces. Therefore,
most of the total mass of creosote probably would
not be left as a residual on the fracture surfaces
through which the creosote has migrated. This
lack of a loss of mass as the creosote migrates
would favor more distant migration. The high
viscosity of creosote would impede its migration,
but it would also make extraction of free-product
creosote more difficult. The physical properties of
creosote and the complexity of the fractured
subsurface both suggest that the final remediation
of the site to health-based standards may not be
achievable in the foreseeable future using the
current remediation system.
UPDATE BIBLIOGRAPHY/
REFERENCES
CH2M HILL. October 1987. Groundwater
Treatment Phase 2 Interim Report, UP&L Pole
Treatment Yard, Idaho Falls, Idaho.
Dames & Moore. January 1988. Installation of
Aquifer No. 3 Monitoring Wells, Pole Treatment
Yard, Idaho Falls, Idaho, for Utah Power & Light
Company.
Dames & Moore. March 7, 1989. Report of
Quarterly Ground Water Flow Rale and Direction
Calculations for Aquifer No. 3. Pole Treatment
Yard, Idaho Falls, Idaho. Letter from George
Condrat to L. E. Newland of Utah Power & Light.
Dames & Moore, May 1989a. Utah Power &
Light/Pacific Power & Light, Idaho Falls Pole
Yard, RCRA Post-closure Semi-annual Report for
October 1988 through March 1989.
Dames & Moore. November 1989b. Utah Power
& Light/Pacific Power & Light Idaho Falls Pole
Yard, RCRA Post-closure Semi-annual Report for
April through September 1989.
Utah Power & Light
Dames & Moore. June 1990. Utah Power &
Light/Pacific Power & Light Idaho Falls Pole
Yard, RCRA Post-closure Semi-annual Report for
October 1989 through March 1990.
256
io/n 4*77
-------
UPDATE OF CASE STUDY 18
Verona Well Field
Battle Creek, Michigan
Abstract
Ground-water remediation systems are operating in two separate parts of the Verona Well
Field project area. The barrier well system continues to control plume migration into the
well field. Since its implementation, high concentration regions have been reduce laterally,
but contamination remains high along the plume's centerline. The second system, a
combination of ground-water extraction and soil vapor extraction, has continued to
remediate VOC contamination at the TSRR facility. Ground-water contaminant levels
remain above clean-up goals at the facility. Remediation of the two remaining source areas,
the Thomas Solvent Annex and the GTWRR Paint Shop area, has not begun, although a
remedial investigation and a feasibility study for those areas have been completed.
Table of Background Data
Date of Problem Identification
Extraction Started
Types of Contaminants
Primary Aquifer Materials
Maximum Number of Extraction Wells
Maximum Total Extraction Rate
Estimated Plume Area
Estimated Plume Thickness
Maximum Reported Concentrations
1981
May 1984
VOCs
Glacial sand and gravel over fractured
sandstone
(TSRR) 9
(Blocking Wells) 6
(TSRR) 400 gpm
(Blocking Wells) 2,000 gpm
125 acres
120 feet
Total VOCs 85,960 ppb
257
10/1%
-------
CASE STUDY UPDATE
VERONA WELL FIELD
BACKGROUND OF THE PROBLEM
INTRODUCTION
The original case study for the Verona Well Field
Superfund site presented background information
and described the remedial progress made through
mid-1988 (U.S. EPA, 1989, Case Study 18). This
update discusses more recent developments at the
site and the progress that has been made through
early 1991.
Verona Well Field is located on both sides of the
Battle Creek River, approximately 3.5 miles
northeast of downtown Battle Creek, Michigan.
The location of the well field with respect to the
river and the contaminant source areas, is shown
in Figure 1. In 1^81, routine sampling of the
municipal water supply led to the discovery that
the well field was contaminated with volatile
organic compounds (VOCs), principally
chlorinated solvents. Further investigation showed
that the primary sources of the contamination were
the Thomas Solvent Company's Raymond Road
(TSRR) facility, the Thomas Solvent Annex on
Emmett Street, and the Grand Trunk Western
Railroad (GTWRR) marshalling yard (see Figure
1).
Verona Well Field was listed by the EPA as a
Superfund site in 1982. In May 1984, the EPA
issued a record of decision (ROD) specifying an
Interim Remedial Measure (IRM) for the well
field. The IRM consisted^ of the installation of
three new wells in the uncpntaminated northern
portion of the well field and the conversion of
several existing wells into a blocking system that
would halt the spread of the contaminant plume.
The IRM was implemented in 1984.
In 1985, a second ROD was signed for
remediation of the most heavily contaminated of
the three source areas, the Thomas Solvent
Raymond Road (TSRR) facility. The TSRR
remediation system included ground-water
extraction wells and a soil vapor extraction system.
•The' ground-water extraction system began
operating in March 1987. A pilot vapor extraction
system was also installed in 19871 ancl testing
began in November of that year. Construction of
the final system was initiated in January 1988.
Full-scale operation of the system began in March
1988. '
The geologic units of concern at the site are the
unconsolidated glacial till deposits and the
underlying sandstone of the Marshall Formation.
The thickness of the glacial deposits range from a
few feet to 100 feet. Near the TSRR facility, the
thickness is approximately 45 feet The glacial
deposits consist primarily of stratified and inter-
layered sand and gravel, with clay or clay-rich
glacial till layers occurring locally. The
underlying Marshall Formation consists of very
fine to medium sandstone with layers of shaley
sandstone. In the area of the well field, it is
approximately 150 feet thick. Both vertical and
horizontal fractures are frequent in the upper 60 to
80 feet as well as from 100 to 135 feet in the
sandstone. In its lower reaches, it is interbedded
with siltstone, shale, and limestone. The sandstone
is underlain by a shale layer that appears to be an
effective aquiclude.
Both the sandstone and the glacial deposits
function as aquifers, and in most areas there
appears to be little or no hydraulic separation
between the two zones. The water table to the
vicinity of the TSRR facility is 16 to 25 feet
below ground surface. The natural flow of ground
water is toward the Battle Creek River.
Superimposed on the natural hydraulic gradients
are those imposed by pumping in the well field.
At the TSRR facility, the effects of the well field
reinforce the natural gradients, which produce
ground-water flow to the north-northwest.
Ground-water quality investigations conducted
since the discovery of contamination at Verona
Well Field have identified two plumes of VOCs
approaching the well field from the south and
southeast. The southern plume originates from the
TSRR facility and the Thomas Solvent Annex.
The smaller and more easterly plume comes
primarily from the paint shop in the Railroad Car
Department next to the GTWRR marshalling yard.
258
1085
-------
Verona Well Field
MAW
TWHKWWmt,
IUIWOAO
MAMMALLWa
YAM>
4000 tL
ModHMtram: CH2M HILL, 1»68
srre LOCATION MAP
VERONA WEa FIELD SITE
259
-------
Verona Well Field
The contaminants that have been regularly detected
in groundwater sampling at the well field are:
Tetrachloroethylene (PCE)
• Trichloroethylene (TCE)
1,2-Dichloroethylene (1,2-DCE) (cis and
trans)
1,1-Dichloroethylene (1,1-DCE)
1,1,1-Trichloroethane (1,1,1-TCA)
1,2-Dichloroethane (1,2-DCA)
• 1,1 -Dichloroethane (1,1 -DCA)
At the TSRR facility, the contaminants found in
the ground water include all of the above plus
chloroform, methylene chloride, and the
characteristic constituents of petroleum
hydrocarbons, toluene, xylene, and ethylbenzene.
UPDATE ON SITE
CHARACTERISTICS
The remediation at Verona Well Field continues to
be administered by the EPA under the Superfund
program. The operation of the blocking wells in
the well field continues as specified in the 1984
ROD. At the TSRR facility, the remediation is
proceeding as established by the 1985 ROD. In
1990, a remedial investigation was completed for
the remaining primary source areas at the Thomas
Solvent Annex and trie GTWRR Paint Shop (U.S.
EPA, 1990). this investigation included data
collected from the entke site, but focused on the
two remaining source areas. This was followed, in
1991, by a feasibility study of remedial
alternatives addressing the two remaining source
areas (U.S. EPA, 1991).
New information gathered in the site investigations
since mid-1988 has added some detail, but has not
significantly altered the description of site
hydrogeology given in the original case study.
The site-wide data collected during the remedial
investigation in 1989 show that the highest
concentrations of VOCs are still found in the three
primary source areas. The highest total VOC
concentrations detected in ground-water samples
from each of the three areas in 1989 were:
TSRR Facility: Well B18 - 85,960 ppb
• Thomas Solvent Annex: Well B8 - 49,800
ppb
• GTWRR Paint Shop: Well CH106I
64,510 ppb
In each case, these maximum VOC concentrations
were found in ground-water samples taken at or
near the water table. It was noted that the
contaminants are generally found at or near the
water table in the source areas and in the middle
and lower portions of the aquifer as the plumes
approach the well field. High pumping rates in
the well field produce strong vertical gradients,
which appear to pull the contamination downward
through the sandstone aquifer.
Thomas Solvent Annex Source Area: The
Thomas Solvent Annex property is owned by the
GTWRR, and was leased to Thomas Solvent
Company from 1939 to the mid-1980s. The site
was used as a railroad siding for shipping the
chemicals handled by the company, primarily
solvents and fuels. The site facilities included a
solvent pumping and transfer station for loading
and unloading railroad cars, two underground
storage tanks, and one aboveground storage tank.
Soil and ground-water contamination at the annex
is thought to have arisen from leaking drums and
surface spills.
Table 1 lists the maximum concentrations of the
primary contaminants found in ground-water
samples taken from the Thomas Solvent Annex
during the 1989 remedial investigation. The listed
concentrations were not all detected in the same
well. The PCE concentration of 2,100 ppb is
approximately 1 percent of the aqueous solubility
of that compound. The concentration of 7,900 ppb
listed for ethylbenzene is about 5 percent of
solubility. These relatively high concentrations
provide some indication that VOCs may be present
as nonaqueous phase liquids (NAPLs).
A much stronger indication of NAPLs was
obtained from the program of soil sampling
conducted during the remedial investigation.
Three soil samples were taken from each of
16 borings drilled at the Thomas Solvent Annex.
Each of the top two samples taken from every
boring was a composite representing average
conditions over a 6-foot interval. The third sample
was composited over whatever interval remained
from a depth of 12 feet down to the water table,
which was generally located between 14 and
18 feet below ground. Table 2 provides a
summary of the analytical results for the resulting
48 samples. The most prevalent contaminant
found above the water table was PCE. The
maximum PCE concentration of 42,000,000 ppb
was detected in a composite sample taken from
260
/005
-------
Verona Well Field
just above the water table. Because the aqueous
solubility of PCE is approximately 150,000 ppb,
this high concentration indicates that the sample
contained more PCE than could be held in the
dissolved and adsorbed phases alone. It is a
strong indication that NAPLs were also present.
GTWRR Paint Shop Area: The paint shop and
other maintenance shops of the GTWRR Railroad
Car Department used solvent chemicals for
degreasing and cleaning from the mid-1960s until
the 1980s. Until the late 1970s, spent solvents
were disposed of on the ground outside the shops
or in a pit adjacent to the paint shop (U.S. EPA,
1990).
A summary of the maximum concentrations of the
primary VOCs found in ground-water samples
taken from the paint shop area in 1989 is given in
Table 1. The highest concentration found, both in
absolute terms and relative to aqueous solubility,
was the 32,000 ppb detected for PCE. This is
approximately 21 percent of the solubility limit for
that compound.
Ten soil borings were drilled in the paint shop
area, with composite samples again being collected
over 6-foot intervals. The water table at this site
was below the top of the consolidated sandstone
unit, so the borings were terminated at the
sandstone rather than at the water table. The
thickness of the glacial deposits to this area was
between 12 and 22 feet, so three samples were
obtained from some of the borings and four from
others. The total number of samples was 34. The
analytical results for the soil samples are listed in
Table 3. Again, PCE was detected most
frequently and in the highest concentrations.
Thomas Solvent Raymond Road Facility: The
Thomas Solvent Company conducted business
under various names at the Raymond Road
location between 1939 and 1984. The activities at
the site over these years included purchasing,
storing, blending, and selling virgin industrial
solvents. Used solvents were also accepted and
stored before being transported offsite for disposal
or recycling.
Figure 2 shows the site plan of the TSRR facility
in its current configuration. The warehouse and
loading dock, shown cross-hatched in the figure
were demolished during the installation of the
ground-water extraction system.
Also shown in Figure 2 are the locations of
21 underground storage tanks, which were
removed from the site in January 1991. In 1984,
each of the tanks was tested for leakage. The tank
sizes, contents, and leakage test results are listed in
Table 4. The tank contents and leakage rates give
some indication of the kinds of soil and
ground-water contaminants that might be expected,
but do not provide an estimate of the total
contaminant mass. In addition to leakage from
some of the tanks, direct discharge of solvents to
the ground during cleaning of tanks and drums has
been reported.
The maximum concentrations of the primary
contaminants detected in ground-water samples
taken from the TSRR facility in. 1989 are listed in
Table 1. Toluene was the compound found in
highest concentration. TCE and PCE
concentrations were also quite high.
Table 5 gives a summary of the soil concentrations
detected at the TSRR facility in 1989. A total of
75 soil samples were taken from 25 borings.
Again, PCE was the most frequently detected
contaminant and had the highest mean
concentration. A greater variety of compounds
was detected in this source area than in the two
others. In general, the concentrations in soils were
higher than at the GTWRR paint shop, but not as
high as at the Thomas Solvent Annex. However,
it should be pointed out that both ground-water
and soil vapor extraction systems had been
operating at the TSRR facility for approximately
two years at the time these samples were taken
whereas, at the other two source areas, there had
not yet been any remediation.
A floating NAPL layer had been observed at the
TSRR site. The NAPL was first detected in
monitoring Well B-18 in 1984. The thickness of
the free product layer in the well was reported to
be 2.5 to 3.5 feet. The NAPL was sampled and
found to have a specific gravity of 0.93.
The NAPL consisted primarily of petroleum
hydrocarbon products and hexanes which
contained lesser amounts of trichloroethane,
trichloroethylene, and tetrachloroethylene.
Analytical results are shown in Table 6 for a
NAPL sample taken from Well B-18, and water
samples taken from Wells B-18 and B-18I. Well
261
100%
-------
Verona Well Field
Table 1
MAXIMUM 1989 CONCENTRATIONS
IN SOURCE AREA GROUND- WATER SAMPLES
(Concentrations in ppb)
Compound
1,2-DCE
1,1,1-TCA
TCE
PCE
Toluene
Ethylbenzene '
Total Xylene
Thomas Solvent
Annex
13,000
12,000
970
2,100
4,200
7,900
24,000
GTWRR Paint Shop
17,000
13,000
280
32,000
4,900
11,000
28,000
TSSR
Facility
3,700
6,900
17,000
17,000
34,000
2,000
660
Note: The maximum concentrations were not all measured in the same monitoring well.
B-18 is screened at the water table, and 6-181 is
screened below it at the top of the sandstone. The
NAPL layer has not been observed since October
1988 (CH2M HILL, 1991b).
REMEDIATION
Design and Operational
Features of the Remediation
Systems
The design and operational features of the active
remediation systems at the Verona Well Field site
have not changed substantially since the original
case study. Three remediation systems have been
implemented: the barrier system in the well field
itself, and the ground-water and soil vapor
extraction systems at the TSRR facility.
Barrier Well System: As stated in the original
case study, wells of the 20-series, in the
south-central portion of the well field, have been
designated as blocking wells. The objectives of
the blocking system are to intercept the
contaminant plume and to protect the water supply
wells in the northern part of the well field.
Operation of the blocking system started in May
1984 using Wells V-20, V-22, V-25, V-27, and
V-28. Since that time, the blocking wells have
continued to operate, sometimes with five and
sometimes with six wells pumping. As of 1990,
six of the 20-series wells (V-22, V-24, V-25, V-
26, V-27, V-28) were being used, with a total
extraction rite of 1,500 gallons per minute (gpm).
The selection of the wells to be pumped and the
pumping rates were guided by water level and
water quality monitoring in the well field. The
water pumped from the blocking wells is
combined with the discharge of the TSRR
extraction system, which is pumped to the well
field through a force main from the TSRR facility.
The combined flow.s are then treated by air
stripping and discharged to the Battle Creek River.
TSRR Remediation Systems: As reported in the
original case study, the remedial activities at the
TSRR facility include both ground-water extraction
and soil vapor extraction.
The ground-water extraction system consists of
nine extraction wells screened in the glacial
deposits on the TSRR site and directly
downgradient from it. The locations of the
extraction wells are shown in Figure 3. All of the
wells, except Well EW-8, are 8 inches in diameter.
From startup until October 1988, Well EW-8 had
been used as a free product recovery well. The
well has a diameter of 24 inches and had been
provided with both a standard well pump and a
skimmer pump for the floating NAPL. However,
after free product had not been observed in the
well for several months, the skimmer pump was
262
/OC5
-------
to
a
o
Table 2
SUMMARY OF CHEMCIALS DETECTED IN ANNEX SUBSURFACE SOIL BORINGS
Chemical
Bis(2-e(hylhexylphthalate)
1 ,2-Dichioroethane
1,2-Dichloroethene
Ethylbenzene
MethyJene Chloride
Tetrachloroethene
Toluene
1 , 1 , 1 -Trichloroethane
Trichloroethene
Xylenes (mixed)
Number of
Detections
2
3
7
5
3
47
14
6
28
7
Detection
Frequency
(%)
67
6
15
10
6
98
29
13
58
15
Mean
Concentration
0*g/kg)'
61.5
191
212
31,641
161
949393
71,160
37,761
120,308
250,250
SD"
9.2
407
427
216,457
283
6,061,021
490,700
259,769
679,107
1,732,014
95%
UCL
71.9
306
333
92,880
241
2,664,000
210,000
111,300
312,400
740,200
Range of Detected
Concentrations
55-68
260-2,400
150-2,700
180-1,500,000
650-1,400
140-42,000,000
140-3,400,000
210-1,800,000
• 160-4,600,000
380-12,000,000
aCalculation using V4 the detection limit for samples where compound was undetected.
SD = Standard deviation.
UCL =• Upper confidence limits.
r
&
r
SL
o.
-------
Table 3
SUMMARY OF CHEMICALS DETECTED IN PAINT SHOP SUBSURFACE SOIL BORINGS
Chemical
Bis(2-ethylhexylphthalate)
Bromodichloromethane
Tetrachloroethene
Toluene
1 , 1 , 1 -Trichloroelha ne
Number of
Detections
2
2
28
6
5
Detection
Frequency
(%)
67
6
82
18
15
Mean
Concentration
(Hg/kg)'
216
284
3,376
294
294
SD"
232
774
6,364
767
770
95%
UCL
479
534
5,515
552
553
Range of
Detected
Concentrations
52-380
440-630
150-35,(KK)
77-430
150-620
"Calculation using 1A the detection limit for samples where compound was undetected.
SD = Standard deviation.
UCL = Upper confidence limits.
o
I
o
to
i
-------
Verona Well Field
LOAMNQDOCK
(DEMOLISHED)
UNDERGROUND
STORAGE
TANK
(APPROXIMATE LOCATIONS)
QflOUNDWATER
MOHITOMNQ lllUXNa
Not*:
• T«vK numbar; oorraspgrxii wKft unk numbw* on Tabto 4
Source: CH2M HILL, 19918
265
Figure 2
TSRR STtl PLAN SHOW»«S
BURIED SOLVENT TANKS
VERONA WELL FIELD Sfti
ft* 7 7
-------
Verona Well Field
Table 4
UNDERGROUND STORAGE TANKS
THOMAS SOLVENT RAYMOND ROAD SITE
Tank Number*
1
2
3
4
5
6
7
8
9
10
11
12
13
14
15
16
17
18
19
20
21
Contents*
Hi-purity hexane
99 percent ethyl acetate
Xylene
Acetone
Toluene
Trichloroethylene (TCE)
Perchloroethylene (PCE)
1,1, 1-trichloroethane
TS-100 solvent
Methyl ethyl ketone
Methanol
VMP naptha
310-66 mineral spirits
Ethyl alcohol 903-200
140 F solvent
Active thinner (Heptane)
N-propyl acetate
#300 mineral spirits
(isopropyl alcohol 99%)
Mineral spirits
Diesel fuel
Reclaimed acetone
Tank Volume
(gallons)
15,000
6,000
8,000
8,000
10,000
6,000
4,000
6,000
4,000
4,000
4,000
4,000
4,000
4,000
4,000
6,000
6,000
6,000
15,000
6,000
12,000
Leakage Rate0
(gal/hr)
0.556
0.179
<0.053
<0.05
0.073
0.067
<0.05
0.232
<0.05
<0.05
0.069
<0.05
<0.05
<0.05
<0.05
0.066
<0.05
0.086
<0.05
0.181
<0.05
"Tank number corresponds to tank numbers shown in Figure 2.
•"Reflects contents at time of testing.
Tank tests by Homer Creative Metals, Inc., for Thomas Solvent Company. Rates
under test conditions may or may not be representative of leakage rates under
actual conditions.
266
60k 77
-------
Table 5
SUMMARY OF CHEMICALS DETECTED IN RAYMOND ROAD SUBSURFACE SOIL BORINGS
Page 1 of 2
Chemical
Number of
Detections
Detection
Frequency
(%)
Mean
Concentration
(Mg/kg)'
SD"
95%
UCL
Range of Detected
Concentrations
Volatltes
Acetone
Benzene
Bromomethane
2-Butanone
Carbon Disulfide
Carbon Tetrachloride
Chlorobenzene
Chloroform
1,1-Dichloroethane
1,1-Dichloroethene
1,2-Dichloroethene
Ethylbenzene
Methylene Chloride
Tetrachloroethene
Toluene
1,1,1 -Trichloroethane
Trichloroethene
Xylene
11
6
4
5
5
4
9
16
4
9
4
34
36
63
67
22
36
41
15
8
5
7
7
5
12
21
5
12
5
45
48
84
89
29
48
55
743
14.8
29.2
35.6
35
24.5
22.4
20.2
16.6
87.6
19.1
2,713
3,048
9,607
7,855
235
1,193
13,483
4,052
8.1
14.9
33.6
31
95.5
32.4
20.6
16.9
545
31.9
20,774
5,940
62,042
52,346
1,174
5,661
97,036
1,660
16.6
32.6
43.2
96
46.1
29.7
24.9
20.4
211
26.3
7,415
4,392
23,650
19,700
501
2,474
35,440
120-32,000
8-72
16-130
98-200
4-71
6-840
13-180
14-140
12-130
5-4,700
6-230
6-180,000
77-21,000
40-530,000
160-450,000
7-9,300
4-43,000
10-840,000
-s-
I
0
I
•n
•5T
a
-------
oo
O
TableS
SUMMARY OF CHEMICALS DETECTED IN RAYMOND ROAD SUBSURFACE SOIL BORINGS
Page 2 of 2
Chemical
Number of
Detections
Detection
Frequency
<*)
Mean
Concentration
(Mgftg)*
SD*
95%
UCL
Range of Detected
Concentrations
Semivolatiles
Benzoic Acid
Benzylhutylphthalate
Bis(2-ethylhe)ryl)phthalate
Di-n-butylphthalate
Naphthalene
Tetrahydrofuran
2
2
10
6
4
12
8
8
42
25
17
16
882
173
983
200
518
145
297
49.8 .
2,034
142
988
101
1,001
193
1,197
257
913
343
37-690
43-72
40^9,300
35-770
120-4,000
30-300
"Calculation using ¥i the detection limit for samples where compound was undetected.
SD = Standard deviation.
UCL = Upper confidence limits.
I
O
tt
I
-------
Verona Well Field
Table 6
CONTAMINANT ANALYSIS FOR WELLS B-18 AND B-18I
THOMAS SOLVENT RAYMOND ROAD SITE
Volatile Organic
Acrolcin
Acrylonitrile
Benzene
Carbon Tetrachloride
Chloro benzene
1,2-Dichloroethane
1,1,1-TrichIoroethane
1,1-Dichlorocthanc
1,1,2,2-Tetrachloroethane
Chlorocthanc
Chloroform
1,1-Dichlorocthenc
1,2-Dichloroethene
1,2-Dichloropropane
Trans-l,3-Dichloropropene
Cis-1 ,3-Dichloropropene
Ethylbenzene
Methylenc Chloride
Chlorometnane
Bromomethane
Bromoform
Bromodichloromethanc
Fluorotrichloromethane
Chlorodibromomethane
Tetrachloroethene
Toluene
Trichloroethene
Vinyl Chloride
Acetone
2-Butanone
Carbon Disulfide
2-Hexanone
4-Methyl-2-Pentanone
Styrene
Vinyl Acetate
O-Xylene
Total Volatile*
B-18 (Water)
5,000
29,000
LT
6,000
27,000
40,000
45,000
1,000,000
8,000
1,160,000
B-18 (NAPL)
1,000,000
600,000
1,300,000
3,200,000
42,000
60.000
1,400,000
280,000
3,000,000
600,000
6,500,000
44,000,000
12.000,000
LT
5,000.000
78,982,000
B-18I
4
4
13
93
7
11
27
13
172
.Notes: All values in ppb.
B-18 is a shallow well screened at the water table.
B-18I is an intermediate well screened at the sandstone surface.
LT = less than detection limit.
Samples collected in 1984.
269
tot 7 7
-------
Verona Well Field
A
EW2
A
em
A
EW4
AJFVWATER
SEPARATOR'
VE-20
Ugtndi
$ SOU VAPOR EXTRACTION (SVE)WEU.
A QROUNOWMTER EXTRACTION WELL
• TYPtCALSaLBOHlNQ
EWi BA DUAL EXTRACTION WELL
Source: CHm HILL, 1iila
Rgur»3
TSRR SITE MAP SHOWING
REMEDIATION SYSTEMS
VERONA WELL FIELD STC
270
-------
Verona Well Field
removed in October 1988. No floating NAPLs
have been observed in the wells at the site since
this time.
Extraction Wells EW-2 through EW-9 typically
produce between 30 and 70 gpm each. Well
EW-1 was never able to produce more than 5 to
7 gpm, and in 1989 it was removed from service.
The total flow rate of the ground-water extraction
system ranges between 300 and 350 gpm. It is
estimated (CH2M HELL, 1991a) that the system
directly affects approximately the top 20 feet of
the saturated zone over an area of 65,000 square
feet. This represents a saturated pore volume of
approximately 260,000 cubic feet. The extraction
system is estimated to remove one pore volume
approximately every 4 days.
There have been no major modifications in the
operation of the extraction system. However, it
has been found that continuous pumping of the
wells caused well-screen fouling with iron-related
and sulfur-related bacteria. To keep the
productivity of the wells up to design standards it
was necessary to institute a program of regular
well chlorination. This process required one of the
wells to be shut down for chlorine treatment nearly
every working day, so that every well could be
treated two or three times a month. In May 1990,
the practice of chlorinating wells was discontinued.
Since then, site operators have reported that there
has been no bacteria buildup on well screens and
that well productivity has not decreased.
The objective of the ground-water extraction
system is to reduce the concentrations of VOCs in
the ground water to specified health-based levels.
In the initial case study it was reported that the
target cleanup levels corresponded to the EPA's
maximum contaminant levels (MCLs) and that
MCLs had only been" established for three of the
compounds of concern. In the 1991 feasibility
study (U.S. EPA, 1991), a more comprehensive set
of compound-specific remedial objectives was
established for the proposed remedial actions at the
two remaining source areas. These cleanup goals
have also been adopted for the TSRR remediation.
Table 7 lists the new remediation goals together
with the constituent concentrations measured in the
active extraction wells in March 1990.
To enhance the effectiveness of the ground-water
extraction system, a soil vapor extraction system
has also been operating at the TSRR facility since
1988. The original vapor extraction network
consisted of 23 PVC wells of 2- and 4-inch
diameter. The well locations of the original
system are shown in Figure 3. The wells were
screened from approximately 5 feet below ground
to 3 feet below the water table. It was estimated
that this system directly affected the full 20-foot
thickness of the vadose zone over an area of
approximately 36,000 square feet. The volume of
gas-filled pores affected was approximately
144,000 cubic feet. At the typical system flow
rate of 1,400 cubic feet per minute, approximately
14 pore volumes of vapor were removed per day.
In January 1991, 21 underground storage tanks and
part of the SVE system were removed from the
site. A new system, consisting of 21 wells instead
of 23, was installed in February 1991. The wells
are screened in the lower 6 feet of the vadose
zone," approximately 14 to 20 feet below the land
surface. Well screens are approximately 10 feet in
length. The new system (not shown) covers the
same general area as the old system. Flow rates
of the new system are approximately the same as
for those of the previous system (CH2M HILL,
1991b).
Both activated carbon adsorption and catalytic
oxidation have been used to treat extracted vapor
before it has been released to the atmosphere.
Carbon adsorption system was used from system
startup through December 1989, and from
February 1991 to the present. During 1990, the
carbon adsorption system was replaced with a
catalytic oxidation unit, which oxidized the VOCs
in the soil vapor at temperatures of 780 to 820
degrees Fahrenheit in the presence of a catalyst.
The catalytic oxidation system was used at the
time because it had been determined to be more
cost effective than the carbon system. However,
when the new SVE system was installed in 1991,
operators switched back to carbon adsorption,
which proved to be the more economical method.
In the original case study, the performance
objectives for the vapor extraction system were
described as reduction of total VOC concentrations
in the soil to less than 1 mg/kg. However, the
1991 feasibility study has set more stringent soil
cleanup criteria for the Thomas Solvent Annex and
GTWRR Paint Shop areas. These new soil
remediation objectives are considered to be
applicable to the TSRR site also. Table 8 lists the
new criteria along with some representative VOC
concentrations remaining in the soil at the TSRR
location.
271
-------
-4
Contaminant
Acetone
Benzene
Chlorobenzene
Chloroform
U-Dtchloroethane
1,2-Dichloroethane
1,1-Dichloroclhene
l,2-Dichk)roethene (cfe)
1 ,2-Dichloroelhene (tram)
Ethyl benzene
Methylene Chloride
Tclrachloroethene
Toluene
1,1,1 -Trichloroethane
1,1,2-Trichloroelhane
Trichloroethene
Vinyl Chloride
Xylene
TcbfeT
GROUND-WATER CONCENTRATIONS AMD CLEANUP OBJECTIVES
THOMAS SOLVENT RAYMOND ROAD SITE
BATTLE CREEK, MICHIGAN
Extraction Well
(3/15/90 (fatal)
2
48
1.6
15
2,5
29
59
,1-6
1.9 '
22
3
8
99
170
66
410
«30
310
500
290
4
6.5
1.4
5
6
27
11
IS
380
33
430
380
200
370
'390
7
1.1
S
11
35
99
100
400
310
470
420
380
9
25
17
3.1
10
2.3
Notes: EW-1 is not operated.
All units in ppt>.
Blank spaces indicate that the compound was not detected.
Extraction wetl concentrations represent contaminant levels averaged over the entire screened zone of the aquifer.
aRemedial objectives for the site are developed in the feasibility study for the other two source areas (U.S. EPA, 1991).
Remedial
Objective"
3400
1
100
6
0.3,1
OH
0.058
1
100
30
5
0.7
40
200
0.6
3
0.015
20
f
o
B>
I
•n
S"
_
-------
Verona Weil Field
Table 8
SOIL-CLEANUP OBJECTIVES
THOMAS SOLVENT RAYMOND ROAD SITE
BATTLE CREEK, MICHIGAN
Contaminant
1,1-Dichloroethane
1,1-Dichloroethene
1,2-Dichloroethane
1,2-Dichloroethene (cis)
1,2-Dichlorethene (trans)
Ethylbenzene
Methylene Chloride
Tetrachloroethene
Toluene
1,1,1-Trichloroethane
Trichloroethene
Xylenes
Average Soil
Concentration in
August 1988
(Hg/kg)
3
70
1
6
6
2,800
2,700
12,000
8,000
570
1,400
7,500
Estimated Soil
Concentration in
January 1991*
(H8/kg)
—
10
-
—
—
420
490
1,800
1,200
90
210
1,100
Remedial Objective1*
(eg/kg)
6.6
1.2
6.6
20
2,000
600
100
14
800
4,000
60
400
'Based on an 85 percent contaminant removal since August 1988. This assumes identical rates of
contaminant removal from the vadose zone.
''Remedial objectives for the site are developed in the feasibility study for the other two source
areas (U.S. EPA, 1991).
Notes: - indicates not detected.
273
110-3
-------
Verona Well Field
EVALUATION OF PERFORMANCE
Barrier Well System: In the original case study
It was stated that, as of mid-1988, the barrier well
system was successful in blocking plume migration
to the water supply wells in the northern part of
the, well field. ^ More recent performance
information indicates that the system continues to
capture both of the contaminant plumes that
approach the well field from the south" and
southeast.
Figures 4 and 5 show water level contours in the
glacial deposits and in the underlying sandstone,
based on measurements taken in April 1$>8§, In
the glacial overburden aquifer, the hydraulic
effects of the 20-series blocking wells are quite
clearly seen. In the sandstone aquifer, the
influence of the blocking wells is combined with
that of the operating water supply wells farther
north in the well field. However, the ground-water
flow pattern is well defined by the water level
contours, and the blocking wells are located
between the contaminant source areas and the
production wells. The northernmost wells, V-55
through V-53, were installed as part of the IRM to
replace the production capacity lost "when the
20-series wells were converted for plume control.
The contaminant plumes in the glacial overburden
and sandstone aquifers are shown in Figures 6 and
7. The total VOC concentration contours are
based on ground-water samples taken during the
remedial investigation in April 1989. Comparison
of these plume maps with the 1984 plume map
presented in the original case study shows that the
plumes have been stabilized and that migration
into the northern part of the well field has been cut
off. There has been a general reduction in the
extent of the high concentration regions around the
source area's. Concentrations in the area between
the TSRR facility and me Thomas Solvent Annex
have been reduced by approximately two orders of
magnitude. However, total VOC concentrations of
more than 1000 ppb' persist around, and
immediately downgradient of, all three source
areas.
Figure 8 shows contours of total VOC
concentration in a vertical cross section taken
through the main body of the contaminant plume
originating at the TSRR facility. It shows that the
highest concentrations in the TSRR source area are
found near the water table, but farther
downgradient they are deeper in the sandstone.
Comparison with a similar cross sectional plot in
the original case study shows that there has been
little change in concentrations along the centerline
of the plume since 1984.
TSRR Remediation Systems: Through December
1950, approximately 645 million gallons of ground
water containing approximately 14,000 pounds of
VOCs had been removed by the ground-water
extraction system at the TSRR facility.
Figure 9 shows the historical record of total VOC
concentrations in Well EW-8, which is of
particular interest because it is located in the
central part of the floating NAPL layer. After
approximately the first 500 days of operation, the
concentrations in this well have been relatively
stable in the 4,000'to 5,000 ppb range, with an
apparent slow declining trend. In addition to
ground-water extraction, Well EW-8 is also a free
product recovery well. Between March 1987 and
October 1988, more than 150 gallons, or roughly
1,200 pounds, of free product were skimmed from
the well. The NAPL layer has not been recorded
at the site since October 1988.
Figure 10 shows the record of total VOC
concentrations in the combined flow stream from
the extraction well system. The concentrations,
which were originally as high as 19,000 ppb,
showed a rapid decline in the first half of the year
and have stabilized at less than 3,000 ppb. Over
the last two years a very slow declining trend can
be observed.
Approximately 45,000 pounds of VOCs have been
removed by the soil vapor extraction system since
it began operating in November 1987. Figure 11
shows the record of cumulative VOC removal for
the vapor extraction system. Approximately 95
percent of the contaminant removal was achieved
during the first 200 days of the 400-day operating
record shown. During the second half of 1990 the
system's production rate was consistently less than
10 pounds per day. This is in contrast to the first
half year of system operation, when production
rates were commonly between 600 and
1000 pounds per day. In late 1990, it was
estimated mat approximately 1000 pounds of VOC
remained in the vadose zone soils.
274
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HORIZONTAL nsTAHCE M ncr
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OF 5UBSURTACE COHDinoNS BE
,
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HELLS.
a CONCENTRATION IMS ACETONE. W«CH WAS ALSO
A LAB CONTAMMANT. DATA PONT IS TO IE
CONSIDERED PRELIMINARY.
-10 tSOCONCEMTRATION CONTOUR. CONCENTRATION
IS|XJA
2 QUESTS MAR1
-------
TolalVOCs
15.000
10.000
5,000
200 Days - 475
365 Days - 667
302 Days « 717
Source: CH2M HILL, 1991a
1989
1990
200
400 800 800
Operating Days Since March 4.1987
1.000
1,200
ffl
O
OJ
Flguni
RECORD OF TOTAL VOC
CONCENTRATIONS IN EXTRACTION
WELLEW-a
V6«»IA WELL FI1LO SITE
-------
to
oo
50.000
45.000
40.000
35.000
30,000
ToMVOCs
1987
1988
1989
200
400 800 800
Operating Days Sfnct March 4.1987,
1990
1.000
1.200
I
-n
5'
a
Source: CH2M HILL, 1991a
Figure 10
RECORD OF TOTAL VOC
CONCENTRATIONS IN COMBINED
EXTRACTION WELL FLOW
VERONA WELL FIELD SITE
-------
CO
SHOW
45000
40000
35000
30000
CumtAMMl
VOC« 25000
(poonds)
20000
15000
10000
5000
0
100
150 200 250
Cumutetfv* Days of Operation
300
350
400
ffl
O
18
£.
3
5"
a
Source: CH2M HILL, 1991 a
Flour* 11
RECORD OF CUMULATW VOC
REMOVAL BY THE SOJL VAPOR
EXTRACTION SYSTEM
VETONA WELL FIELD SfTC
-------
Verona Well Field
SUMMARY OF REMEDIATION
Ground-water remediations are in progress in two
separate parts of the Verona Well Field project
area. The first system to go into operation was the
barrier well system, which is intended to control
plume migration in the well field. In addition, a
combination of ground-water extraction and soil
vapor extraction are being used to remediate VOC
contamination at the TSRR facility. The TSRR
facility is one of three primary contaminant source
areas that are jointly responsible for most of the
well field contamination. Remediation of the two
remaining source areas, the Thomas Solvent
Annex and the GTWRR Paint Shop area, has not
yet begun, although a remedial investigation and a
feasibility study for those areas have been
completed.
The barrier well system is protecting the remaining
production wells in the Verona Well Field from
the contaminant plumes emanating from the three
primary source areas. However, VOCs have been
detected in the first row of wells behind the barrier
wells. In August 1988 and periodically during
1989 and 1990, VOC concentrations ranging from
0.5 ppb to 7 ppb have been measured in several of
those wells. Detections are sporadic, usually
appearing in nonconsecutive sampling rounds
(Public Works Department, City of Battle Creek,
Michigan, 1991). The contaminant plumes them-
selves have remained fairly stable since the barrier
system began operating in 1984. The high
concentration regions of the plumes have been
reduced somewhat in lateral extent, but there has
been little reduction along the centerlines of the
individual plumes. Continued operation of the
barrier well system will probably be necessary for
a long time.
At the TSRR facility, the ground-water and soil
vapor extraction systems continue to operate.
Approximately 19,000 pounds of VOCs have been
removed by ground-water extraction and 45,000
pounds by soil vapor extraction. An additional
1,200 pounds have been removed by free product
skimming in the NAPL recovery well. However,
the production rates have declined, in all three
categories, to such low levels that further remedial
progress is expected to be very slow. Contaminant
concentrations are" still well above the health-based
cleanup goals.
SUMMARY OF NAPL-RELATED
ISSUES
A layer of NAPL was discovered floating on the
water table at the TSRR facility in 1984. The
NAPL was tested and found to be a mixture
consisting mainly of chlorinated solvents and BTX
(benzene, toluene, and xylene) compounds. Even
though the chlorinated solvents were stored at the
site in separate leaking underground tanks,
extensive monitoring has not shown evidence of
independent dense NAPL (DNAPL) plumes.
Instead, the dense chlorinated solvents seem to be
present only near the water table in conjunction
with the floating NAPL mixture. The NAPL has
not been observed since October 1988.
The remediation systems have addressed the
NAPL problem at the TSRR facility in conjunction
with the ground-water and soil contamination
problems. Most of the contaminant mass has been
recovered in the vapor phase by the soil vapor
extraction system and in the dissolved phase by
the ground-water extraction system. Less than
2 percent of the contaminant mass that has been
removed was recovered as a NAPL by the free
product skimming system.
The recovery rates of both the ground-water and
the soil vapor extraction systems have fallen off
greatly with continued operation, even though a
substantial mass of contamination is thought to
remain in the subsurface. Studies suggest that a
portion of the NAPL might have been retained in
the soil pore space and is contributing to the con-
tamination at the site (CH2M HILL, 199 Ib).
Subsurface investigations at the Thomas Solvent
Annex and the GTWRR paint shop have provided
information suggesting that NAPLs may be present
in those source areas also. The evidence at the
Thomas Solvent Annex is particularly strong, with
several soil samples showing extremely high
concentrations of chlorinated solvents.
Contaminants have not been directly observed at
these sites in nonaqueous phase. This is not
surprising because the dense chlorinated solvents
are potentially present as DNAPLs, which are
considerably more elusive than floating NAPLs.
283
-------
Verona Well Field
UPDATE BIBLIOGRAPHY/
REFERENCES
CH2M HILL. May 1988. Verona Well Field
Final RI/FS Work Plan.
CH2M HILL. January 1990. Technical
memorandum 5, Verona Well Reid, Remedial
Investigation/Feasibility Study.
McCann, Michael, Paul M. Boersma and
Patricia V. Cline. May 1991. Effects of
Nonaqueous Phase Liquids on a Superfund
Remediation. Proceedings from HAZTECH Inter-
national, Pittsburgh, Pennsylvania.
CH2M HELL. January 199 la. Draft Performance
Evaluation Report, Thomas Solvent Raymond Road
Operable Unit, Verona Well Field Site.
CH2M HILL. June 13, 1991b. Personal com-
munication with Mike McCann, Project Manager.
Public Works Department, City of Battle Creek,
Michigan. June 18, 1991. Personal communication
with John P. O'Brien, Public Utilities Manager.
U.S. Environmental Protection Agency (U.S.
EPA). October 1989. Evaluation of
Ground-Water Extraction Remedies: Volume 2,
Case Studies 1-19. Document Number
EPA/9355.4-03.
U.S. EPA. August 1990. Remedial Investigation
Report, Verona Well Field, Volume 1.
U.S. EPA. February 1991, Public Comment Draft
Feasibility Study, Verona Well Field.
284 IID7 60k 77
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CASE STUDY 19
Ville Mercier
Quebec, Canada
Abstract
The Ville Mercier site is located along the south shore of the St. Lawrence River, 20 km
southwest of Montreal, Quebec. From 1968 to 1972, a waste-oil carrier disposed of an
estimated 40,000 m3 of liquid petroleum and petrochemical wastes in an abandoned gravel
pit near Ville Mercier. By 1972, removal of liquid wastes and remediation by incineration
was initiated. Through 1975, most liquid wastes had been removed and incinerated.
Removal and incineration of sludges did not begin until 1981.
By 1981, it was estimated that ground-water contamination extended over an area of
30 km2. Following a 1982 feasibility study, pumping and treatment of the most heavily
contaminated zones was chosen as the site remedy. The system consists of three extraction
wells within a combined extraction rate of 47 I/sec. As of 1988, only a minimal amount of
contaminants (20 tons) had been extracted from the ground water. Dense nonaqueous phase
liquids (DNAPLs) have been observed at the site. Site operators have had to address
clogging problems in the treatment system caused by bacteria fouling, precipitation of
metals, and DNAPLs. Pumping and treatment is expected to extend some time into the
future. An update of this case study was not written because new data were not available.
See the original case study for more complete information on the site (U.S. EPA, 1989).
Table of Background Data
Date of Problem Identification
Extraction Started
Types of Contaminants
Primary Aquifer Materials
Maximum Number of Extraction Wells
Maximum Total Extraction Rate
Estimated Plume Area
Estimated Plume Thickness
Maximum Reported Concentrations
Early 1970s
1983
Organics
Glacial sand, gravel, and clay over fractured
sandstone
3
750 gpm
7,600 acres
80 feet
Not given
285
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CASE STUDY 20
Mid-South Wood Products
Mana, Arkansas
Abstract
Soils and ground water have been contaminated at the Mid-South Woods site as a result of
spills of wood treatment liquids and onsite disposal of wastes into unlined ponds. The
contamination has been remediated using a system of French drains and drilled recovery
wells. An interim 3-well system was operated from early 1985 to mid-1989. The full 15-
well recovery system has been operated since mid-1989. Available data from 1984, 1985,
1989, and 1990 show that concentrations in ground water decreased significantly from 1985
to 1989. In addition to the operation of the remediation system, this reduction may also be
due to natural attenuation and downward lateral migration of contaminants. Both LNAPLS
and DNAPLS have been observed at the site. There is evidence of DNAPLS down to 172
feet in one well.
Table of Background Data
Date of Problem Identification
Extraction Started
Types of Contaminants
Primary Aquifer Materials
Maximum Number of Extraction Wells
Maximum Total Extraction Rate
Estimated Plume Area
Estimated Plume Thickness
Maximum Reported Concentrations
1976
early 1985
pentachlorophenol (PCP)
chromium
arsenic
polynuclear aromatic hydrocarbons (PANs)
Fractured sandstone and shale
15 (most with French drains)
approximately 42 gpm
10-20 acres
as much as 172 feet
40,000,000 PCP
286
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CASE STUDY
MID-SOUTH WOOD PRODUCTS SITE
BACKGROUND OF THE PROBLEM
This case study summarizes ground-water
remediation efforts at the Mid-South Wood
Products Superfund site in Mena, Arkansas. The
site is a 57-acre wood-treating facility located in
western Arkansas, a short distance north of
Highway 71. Figure 1 shows the site location.
The site is divided into two areas—the abandoned
plant area, where pentachlorophenol (PCP) and
creosote formerly were used to pressure-treat
wood, and the currently active wood treatment
facility, where chromated copper arsenate (CCA)
is used.
The abandoned plant area includes an old
treatment plant, two waste ponds, a landfill, the
north and south landfarms, and Clear Lake.
Figure 2 shows the location of these features. The
active treatment plant, located near the old plant in
the northeastern quadrant of the site, consists of a
pressure-treating cylinder, several elevated storage
tanks for treatment solution, a concrete drip pad,
and a wood-drying kiln.
The ground water at the site is contaminated with
PCP, chromium, arsenic, and derivatives of
creosote, primarily polynuclear aromatic
hydrocarbons (PAHs). The current plant owner,
Mid-South Wood Products, and the previous
owner, Mines Lumber Company, are the two
potentially responsible parties (PRPs) at the site.
The U.S. EPA oversees site remediation activities
under the Superfund program.
SITE HISTORY
The plant site was originally developed in the
1930s to produce untreated wood posts. The
production of creosote-treated timber began at the
site in 1955. In 1967, Hines Lumber Company
purchased the plant and continued to operate it as
a wood treatment plant using both creosote and
PCP in carrier oils as treatment liquids (U.S. EPA,
1986b). These treatment liquids were used until
1977, when the old PCP and creosote treatment
areas were abandoned and Hines converted the
facility to a chromated copper arsenate (CCA)
treating plant (U.S. EPA, 1984). Mid-South Wood
Products purchased the plant in September 1978
and continued using the CCA wood treatment
process. In 1978, Mid-South attempted to close
the Old Pond by spraying the liquid and sludge
from Old Pond onto the north and south landfarm
areas, mixing these wastes Into the soil at the
landfarms, and then filling up Old Pond with part
of the resulting sludge-soil mixture.
The contamination problem was first discovered in
1976, when a, large fishkill in a nearby river was
traced to the site. In 1980, an oily material was
detected in a stream, approximately 1,000 feet
west-northwest of the two waste ponds (B&F
Engineering, 1990c). A landowner adjacent to the
site also complained about contamination in runoff
from the landfill in 1980. In response to this
complaint, ground water samples were collected in
late 1980. These samples revealed low levels of
PCP, arsenic, and chromium in the ground water
west and northwest of the site (U.S. EPA, 1986c).
The Mid-South Wood site was added to the
Superfund National Priorities List in 1982.
Between 1980 and 1986, the Arkansas Department
of Pollution Control .and Ecology (ADPCE), the
EPA, and Hine's consultants (B&F Engineering
and Law Engineering) conducted a series of
remedial investigations to characterize the type and
extent of contamination at the Mid-South site.
Activities included collecting and analyzing
samples of surface water, ground water, surface
soils, and sediments. These investigations showed
contamination by semivolatile organics (PCP and
primary creosote compounds) and metals (arsenic
and chromium) both onsite and offsite. The record
of decision (ROD) specifying the approach to
remediation of the site was signed by the EPA in
1986. A temporary ground-water extraction and
treatment system consisting of Wells RW-1, RW-
2, RW-3, and their associated French drains was
constructed in late 1984 and began operating in
early 1985. The ground-water recovery system
specified in the ROD began operating in the
summer of 1989.
287
)\f\1
-------
KJ
oo
oo
o
-J
%S'^
;uisra
Source: EPA, I986c
LOCATION OF MID-SOUTH WOOD SITE
(Poor Quality Original) M RELATION TO MEHA, ARKANSAS
MID-SOUTH WOOD, MENA. ARKANSAS
S
a
I
a
I
I
-------
s>
oo
MOON CMBEK
MIO-SOUTH -•
WOOD MOOUCT8
•OUNDAHY
\
Source: U.S. EPA, 1986c
Figure 2
MID-SOUTM WOOD SrrH MAP
MO-SOUTH WOOD PRODUCTS SITE
o
I
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Mid-South Wood Products
GEOLOGY
The Mid-South Wood site is located in the
Ouachita Mountains physiographic province in an
area of consolidated sedimentary rocks. It is
situated on the northern flank of a syncline of
shale and sandstone beds that dips to the
southwest. A broad anticline forms the mountains
north of the site. A fault zone passes through the
site underneath the Old Pond area. The zone runs
west to east along the east fork of Moon Creek.
This fault zone is characterized by highly fractured
shales.
The stratigraphic units at the site are the
Mississippian age Stanley Group and Jackfork
Group and consist of sandstone, shale, and
sandstone iriterbedded with shales, Jhe sandstone
contains hairline fractures dipping at angles of 30
to 70 degrees. The fractures in the shale are both
horizontal and vertical but are more abundant
along the bedding plane surfaces. The interbedded
sandstone and shale unit is fractured also. Figure
3 illustrates the site geology, including the fault
zone and the bedding structure.
The soils overlying the rock consist of weathered
rock, residual soils, and fill material. The residual
soil cover on the site is thin and consists of clayey
sands, clayey silts, and silty to sandy clay with
gravel. The gravel consists primarily of angular
rock fragments. The average soil depth is 3 feet,
and soil depth ranges from less than 2 feet to
6 feet deep.
HYDROGEOLOGY
The ground water at the site is unconfmed and
occurs primarily within the weathered surface and
the deep fractures of the sandstone and shale
•bedrock. The depth to water ranges from 3 to
3D feet below land surface and is generally
shallowest along topographic highs. The saturated
zone within the soil and weathered rock is 1, to 9
feet thick above the bedrock. The primary
porosity of the sandstone and shale is limited;
most of the ground water occurs in secondary
openings such as joints, fractures, and bedding
planes.
Ground-water flow at the site generally follows the
surface topography. The general direction of
horizontal ground-water flow is to the southeast in
the eastern third of the site and to the west and
southwest in the western two-thirds of the site. In
general, hydraulic head decreases with depth over
most of the site, indicating that there is the
potential for downward ground-water flow. The
actual direction of flow within fractures is a
function of both the orientation of the fracture and
the. direction of the prevailing hydraulic gradient.
The ground-water elevation contours are illustrated
in Figure 4, which shows that ground-water
divides occur along a north-south line near the old
plant and along an east-west line between She
north and south landfarms. Water level data
shown in Figure 4 also suggest that the east fork
of Moon Creek is a gaining stream that receives
direct ground-water discharge. Although shallow
ground-water gradients and flow directions within
the weathered rock are believed to mimic the slope
of the surface topography, the direction of ground-
water flow is controlled by the orientation of the
fractures within the unweathered rock.
Ground-water recharge is controlled by the
thickness of the soil cover and the abundance of
bedrock fractures; areas with thin soil cover and
highly fractured rocks respond quickly to
precipitation and account for most of the ground-
water recharge.
Soils at the site have a lower hydraulic
conductivity than the fractured bedrock. Ground-
water velocities are approximately 20 feet per year
along the fault zone -paralleling the east fork of
Moon Creek, 30 feet per year along the railroad
tracks, and 30 to 60 feet per year along slopes.
The average ground-water flow velocity is 35 feet
per year.
WASTE CHARACTERISTICS AND
POTENTIAL SOURCES
The site is contaminated with organic and
inorganic wastes associated with wood-treating
processes. The organic wastes consist of PCP and
a suite of creosote compounds, most of which are
PAHs. Inorganic contaminants include arsenic and
chromium.
Onsite contamination was evident during early
investigations both in the old areas and at the
currently operating CCA plant. In 1984, the
highest concentrations of contaminants were in the
surface soils and stream sediments (0 to 12 inches)
and in the subsurface soils (see Table 1).
However, substantial contamination was also found
290
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K)
-
90UTHEW •»«<«« t~i _,..._
OF ANOMALOUsTbi* U SHALE
FROM LAW'S PH4PEI
HtPOfiT
SI SANDSTONE
AND SHALE
tow (1964) Phase II Gtology
Source: U.S. EPA. 1986b
(Anomalous Zone = Fault Line)
O
O
Q.
Figures
SITE GEOLOGY
MHJ-SOUTH WOOD PRODUCTS SITE
-------
VO
M - MHVSOUTH WOOD PRODUCTS
PROPERTY BOUNDARY
DIRECTION OF
QROUNDWATER
FLOW.
WATER TABLE
CONTOURS.
FAULT ZONE
Source: U.S. EPA, I986a
Figure 4
GROUND-WATER CONTOURS AND FLOW DIRECTION
PRIOR TO GROUND-WATER RECOVERY
MID-SOUTH WOOD PRODUCTS SITE
Q.
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10
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o
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-4
Table!
ARITHMETIC MEAN CONCENTRATIONS OF CONTAMINANTS IN VARIOUS MEDIA IN 1984 PRIOR TO REMEDIATION (ppb)
Arsenic
Chromium, Total
Ftaonnthene
Pentachlorophenol
Pyrene
Aceiuphihene
Acensphlhylene
Anthracene
Benzo(a)anthracenc
Benzo(a)|!yrene
Benzo(b)fl«oranthene
Benzo(lc)fluoranihene
Chiyscne
Dibenzofuran
Fluorcne
2-Methylnaphthatene
Naphthalene
Phenmnthrene
Sarfece Water
Onslte
124
341
11
267
7
7
ND
ND
1
ND
2
2
1
ND
ND
ND
ND
ND
OfbHe
28
14
358
260
231
i49
Tr
129
57
Tr
38
38
56
94
185
2
ND
514
G round W«ttr
Onslfe
26*
27*
2,400
3,240
2,000
3,410
Tr
2,670
445
ND
259
1
429
905
2370
5,480
9,140
6,130
OflMte
7
8
3
195
3
6
9
Tr
Tr
ND
Tr
Tr
Tr
2
3
2
2
6
SartKt Soils (0 to IT)
Onslte
5,450
18,100
1310,000
2,820,000
1,010,000
514,000
21,000
239,000
221,000
23,500
180,000
180,000
231,000
125,000
336,000
3,000
4^00
1,140,000
Offelle
3,290
11,400
4^00
417
5,170
100
Tr
467
867
Tr
1,100
317
1,580
ND
Tr
ND
ND
333
Sob»urf»« Sotte
OnHe
3,360
12,000
126,000
155,000
96,100
91,500
2,740
42,000
18,600
Tr
9,360
9,400
16,400
75,200
94,600
109,000
188,000
251,000
OfUte
3,880*
200*
1350
211
967
314
ND
157
306
49
189
89
343
343
183
2320
31
1450
Straim
Sediments
Onstte
16300
22,900
189,000
116,000
146,000
27,800
48
15,500
29,400
905
37,200
35,600
39,700
662
13,700
824
1,290
59,100
Offitte
20,300*
24,600*
4310
3,040
4,660
313
20
301
981
264
1,180
761
1,080
51
103
879
24
1,080
Source: U.S. EPA, 1986c
Data do not include A* and Cr samples from the vicinity of the CCA plant.
'Median value
ND - No! detected
Tr - Trace amount
z
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Mid-South Wood Products
in the ground water during 1984. The
distributions of PCP, arsenic, chromium, and PAH
compounds in onsite soils during initial
investigations are shown in Figures 5, 6, 7, and 8,
respectively. Some amount of the contaminant
mass is believed to remain as pools or residuals of
free phase liquid contaminants in the soil, the
soil/sludge mixture, and the ground water.
The old plant, the two old ponds, and the two
landfarms are the primary areas of contamination
in the abandoned area. The geologic materials
underlying the old plant and the small old pond
were, and may still be, heavily contaminated with
PQP, several creosote constituents, chromium, and
arsenic. Waste oils appear to have migrated from
these areas to Moon Springs via the geologic fault.
Concentrations of PCP ranging from 260 to 4,200
ppb, and concentrations of several PAH
constituents as high as 17,000 ppb were detected
in surface water at or near Moon Creek. Analysis
of soil samples in the Moon Creek area also
revealed elevated concentrations of chromium
(118,000 ppb) and arsenic (7,600 ppb).
Before remediation began, PCP levels in the old
plant and old waste pond source areas ranged from
200,000 to 11,000,000 ppb in the soil and from
2,000 to 40,000 ppb in the shallow ground water.
Chromium levels ranging from 8,000 to 15,000
ppb and arsenic levels from 2,000 to 8,000 ppb
were detected in the soil in most areas of the site
before remediation began; however, chromium
levels as high as 450,000 ppb and arsenic levels as
high as 270,000 ppb have been found in the soils
in the small old pond area. Concentrations of
arsenic and chromium in surface water in the area
of the old plant and the two waste ponds ranged
from 10,000 to 20,000 ppb. No arsenic and
chromium were' detected in water samples
collected from test pits excavated in the source
area. The 1984 arithmetic means of organic and
inorganic contaminant concentrations in the old
plant and waste pond areas are presented in
Table 1. "
Contamination in the area of the CCA plant was
detected on the surface, in subsurface soils, and in
ground water. The soils within 200 feet of the
CCA plant contain the highest concentrations of
chromium and arsenic contamination of the onsite
soils and are a substantial source of these
contaminant metals. Arsenic concentrations as
high as 1,435,000 ppb have been detected in soils
in the CCA plant area. Shallow soils are more
contaminated than deeper soils, particularly with
copper, chromium, and arsenic. The 1985
arithmetic means of organic and inorganic
contaminant concentrations in the vicinity of the
CCA plant are presented in Table 2. Both Tables
1 and 2 confirm that contamination of onsite
ground water, particularly with organic
compounds, was substantial in 1984 and 1985.
The concentration of organic contaminants in soils
decreases with depth from the ground surface to
the water table.
Table 3 lists the chemical properties of several
contaminants found at the Mid-South Wood site.
All constituents listed in Table 3 have pure phase
densities that are greater than water, however, PCP
is typically dissolved in light carrier oils as part of
the wood treatment process. The aqueous
solubility of these constituents is below 20 ppb
with the exceptions of PCP, which has a solubility
of 14,000 ppb (U.S. EPA, 1982). Reference to
Table 1 shows that the average onsite ground-
water concentrations of chrysene (429 ppb),
benzo(b) fluoranthene (259 ppb), and benzo(a)
anthracene (445 ppb) were considerably greater
than the solubility in water of these contaminants.
Average onsite ground-water concentrations of
PCP and benzo(k) fluoranthene were both 23
percent of solubility. These 1984 concentrations
were extremely high, especially considering that
the in situ concentrations may be even higher due
to sample dilution over the 10-foot screen length.
Table 1 provides strong evidence that nonaqueous
phase liquid contamination existed at the site in
1984.
The CCA stormwater sump, which collects surface
water that flows from the CCA plant working area,
is a second source of inorganic contaminants. The
sump is unlined, allowing contaminated water
from the sump to infiltrate directly into the
shallow subsurface. Samples of sump water
revealed concentrations of copper (2,320 ppb),
chromium (29,600 ppb), and arsenic (18,220 ppb)
(U.S. EPA, 1986).
Offsite contamination was found during initial
investigations in an area 75 to 100 feet in diameter
southwest of the railroad tracks at the site's
southern border. Contaminant levels of benzo(a)
pyrene, were detected in soils at concentrations as
high as 1,700 ppb. This offsite soil contamination
is thought to be the result of ground-water
discharge to the surface. Nonaqueous phase
liquids (NAPLs) were observed in the drainage
294
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Table 2
ARITHMETIC MEANS OF CONTAMINANT CONCENTRATIONS (ppb)
CCA PLANT SITE AREA, 1985 SAMPLES
MID-SOUTH WOOD PRODUCTS SITE
Arsenic
Chromium, Total
Fluoranthene
Pcntachlorophenol
Pyrene
Acenaphthene
Acenaphthylene
Benzo(a)antliracene
Benzo(b)pyrene
Benzo(b)fluoranthene
Benzo(k)flttoranthene
Chrysene
Dibenzofuran
Fluorene
2-Methylnaphthalene
Naphthalene
Phenanthrene
Anthracene
Ground Water
Well M-14, M-15,
M-16, M-17
18
183
263
10,230
194
437
ND
35
ND
ND
ND
37
300
280
730
2,585
617
127
Surface Soils
(0 to 12")
198
22
33,513
187,627
29,078
.5,136
ND
3372
1,215
10^79
1,801
5,527
3,709
4,845
12,091
2,200
10,007
1,462
Subsurface
Soils
<>12")
2
104
20,439
47,387
14,545
23,511
ND
2,602
786
941
770
2,985
17,410
18,488
33,953
44,912
38,264
9,187
Source: U.S. EPA, 1986c
ND - Not detected
299
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Mid-South Wood Products
Table 3
CHEMICAL PROPERTIES OF SELECT CONTAMINANTS
MID-SOUTH WOOD SITE
Creosote*
PCP
Density
(g/cm3)
1.05
2.0
Solubility in
Water (ppb)
-
14,000
Sediment-Water
Partition
Constant, K^.
-
5.3 x 104
Polynuclear Aromatic Hydrocarbons (PAHs)
Benzo(a) Anthracene
Benzo(b) Flubranthene
Benzo(k) Fluoranthene
Benzo(a) Pyrene
Chrysene
1.17
-
-
1.35
1.27
5.7
14
4.3
3.8
1.8
2.0 x 10s
5.5 x 105
5.5 x 10s
5.5 x 106
2.0 x 105
Source: U.S. EPA, 1982
*Creosote is a complex mix of 300 to 400 individual chemical constituents, most of
which are PAHs.
300
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Mid-South Wood Products
ditch in this area. PCP concentrations ranging
from 1,000 to 4,000 ppb were identified in both
soil and water samples. Although metals were not
detected in water samples, chromium (lO.fJOO to
25,000 ppb) and arsenic (1,000 to 5,000 ppb) were
detected in soils.
REMEDIATION
Selection and Design of the
Remedy
Objectives of Remediation
The objective of remedial activities at the Mid-
South Wood site is to reduce potential health risks
so that the threat to human health and the
environment is decreased to acceptable levels.
System designers assumed that exposure of
humans to contaminants by wind or erosion would
be eliminated by capping contaminated soils. The
remaining pathways of potential contaminant
migration are: 1) surface-water flows to ground-
water supplies, and 2) direct infiltration from
source areas down to the water table; therefore,
cleanup goals were based on potential ingestion of
contaminated ground water.
Standards for total carcinogenic PAHs and for
metals were set by estimating the excess cancer
risk that would result from consumption of the
contaminated water over a lifetime. Because most
carcinogens do not have a simple concentration
promulgated as a standard, EPA selected a cleanup
level for PAHs relative to a specified excess
lifetime cancer-risk level. Using a model to
calculate the excess risk, the EPA and Mines
Lumber Company negotiated a 1 x 10"5 risk level
for total PAH cpmpounds of 3,000 ppb (U.S. EPA,
1986c). The cleanup level for PCP was not
specified. The action levels for cleanup of arsenic
and chromium were established as the upper limit
of the range of naturally occurring background
levels of these metals. Using this criterion, the
cleanup standard for soils is 5,600 ppb for arsenic
and 19,400 ppb for chromium (U.S. EPA, 1986c).
National Pollutant Discharge Elimination System
(NPDES) permits were also required to discharge
treated ground water to surface drains. Daily
maximum discharge levels we're set for arsenic (50
ppb), chromium (50 ppb), and for two of the PAH
compounds (naphthalene, 2,300 ppb; fluoranthene,
3,980 ppb)'.
System Configuration
Remedial actions at the Mid-South Wood site
consist of a combination of technologies, including
soil excavation and capping, ground-water
recovery and treatment, and ground-water
monitoring. Ground-water recovery is
accomplished using a system of French drains and
extraction wells. Figure 9 illustrates the major
components of the current remediation and
monitoring system, which began operating in the
summer of 1989. An earlier remediation system,
consisting of extraction Wells RW-l, RW-2, and
RW-3, installed in three French drains, was
constructed in late 1984 and began operating in
early 1985.
Contaminated soils from the old pond, the small
old pond, and the old plant areas were excavated,
stabilized, and consolidated in the old pond. All
other contaminated soils were consolidated in the
north landform area (B&F Engineering 1991b).The
old pond and the north landfarm were then capped
with clay, sand, and topsoil to prevent further
contamination of ground water.
The final ground-water recovery system, which
began operating hi the summer of 1989, was
designed to remove contaminated ground water
from several locations throughout the site and treat
the contaminated water to NPDES permit
concentrations. To recover contaminated ground
water, eight French drains and 15 recovery wells
were installed. Nine of the recovery wells are
within the sumps of the French drains, and six
others are isolated, deep extraction wells. French
drains were chosen to recover contaminated
ground water because the fractured nature of the
bedrock below the site would result, in low yields
from a system composed only of drilled extraction
wells. The French drains are located at the CCA
plant, around the tanks and pressure chamber of
the old plant, along the perimeter of the old pond,
and in line with the northwest-southeast fault zone.
The French drain trenches were excavated to the
depth of backhoe refusal at the top of the bedrock-
-a depth of approximately 15 feet. The system
was designed to collect contaminated ground water
from shallow depths where flow and contaminant
concentrations were expected to be greatest.
Figure 10 is a cross section of a typical drain.
301
-------
Mid-South Wood Products
§ti
Hi Hi
302
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-------
SELECT CLAY
a,Qk ?:r>*J^ £ K ircoiW••» kCsi:ori&JC IjfiK'2? rs'
FABtttC WRAPPED
PCffFORATEO OflAfff
WPE
TOP OF BEDROCK Off MAXIMUM
DEPTH OF PQSStBLE EXCA VA TIOH
Source: U.S. EPA,
Flguraio
CROSS SECTION OF GROUND-WATER
RECOVERY SYSTEM
MIO-SCMJTH WOOD PRODUCTS SITE
s
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Mid-South Wood Products
After the contaminated ground water has been
intercepted by French drains, it is collected by the
recovery-well system. The annual average flow
rate from the recovery wells is estimated to be
about 30 gpm, with an average peak weekly flow
of 42 gpm. If the flow from the wells does not
contain NAPLs, it is pumped through force mains
to a storage tank and is later treated by carbon
adsorption to remove organics (B&F Engineering,
1991b). Once treated, effluent is discharged to
surface drains.
If the water from the recovery wells contains
NAPLs, it is channeled through the oil/water
separator to remove oils or sludges prior to carbon
treatment. Figure 11 illustrates the oil-recovery
system. Ground water contaminated with NAPLs
is removed from the recovery well by installing a
recirculation pipe to break up the phasing in the
well. Oils and sludges are then pumped into a
retention tank above the oil/water separator. After
NAPLs have been transferred to the retention tank,
the recovery well is removed from service for 1
week before it Resumes a normal operating
schedule. The NAPLs remain in the retention tank
for the same period of time and are then drained
into the separator, where the free oils are
recovered and disposed of in compliance with
current Federal and state regulations. According
to the Operations and Maintenance (O&M) plan
for Mid-South Wood (B&F Engineering, 1990c),
the expected amount of free oils and sludges is
estimated to be less than 50 gallons per year.
Monitoring wells were installed at three onsite
areas—along the perimeter of the two capped areas,
near the various French drains, and along the
geologic fault zone-to assess contaminant
movement and evaluate the effectiveness of
contaminant recovery. Most of the monitoring
wells were installed to depths betweem 30 and
60 feet; however, one Well-IWB-170-was drilled
to 172 feet (B&F Engineering, 1989). Figure 9"
shows the location of the monitoring wells.
EVALUATION OF PERFORMANCE
The final ground-water extraction and treatment
system at the Mid-South Wood site has been
operating since the summer of 1989; a smaller
temporary system began operating in early 1985.
The monitoring system has been sampled quarterly
since the system began operation. Tables 4 and 5
show contaminant concentrations in nine
monitoring wells and in 15 recovery wells over
four quarterly sampling events beginning in the
fourth quarter of 1989 and ending in the third
quarter of 1990. Most of the monitoring wells are
located near Moon Spring and are north-northwest
of the north landfarm. MW-10 is between the
north landfarm and the old pond, and MW-20 and
IWB-170 are along the western border of the old
pond area. The recovery wells are distributed
throughout the site. The ground water in the
Moon Springs area is downgradient of the north
landfarm and the old pond. Ground water is
believed to flow relatively efficiently from the
main old plant/old pond area to the Moon Springs
area along the fracture zone.
In general terms, the concentrations in the
recovery and monitoring wells listed in Tables 4
and 5 are considerably lower than the
concentrations in onsite monitoring wells measured
in 1984 and 1985. None of the wells had any of
the three listed PAH compounds at concentrations
above detection limits during the four quarterly
sampling events in 1989 and 1990. However, the
aqueous solubility of benzo(a) anthracene and
benzo(a) pyrene is below the detection limit, and
the aqueous solubility of benzo(b&k) fluoranthene
is only slightly higher than the detection limit, so
the data of Tables 4 and 5 should not be inferred
as precluding the existence of these contaminants
in either dissolved or DNAPL form. These three
PAH compounds are not necessarily the most
abundant of the PAHs present at the site, and their
total mass relative to all PAHs is unknown. The
combined concentration of PAHs was not reported,
so a comparison of PAH contamination to the
cancer-related cleanup standard of 3,000 ppb of
total PAHs established for the site is not possible.
The concentration of PCP generally has decreased
since 1984 and 1985. The concentration of PCP
in the nine monitoring wells was below detection
in all wells except for MW-15, located northwest
of the north landfarm, and in MW-20 and IWB-
170 on the western boundary of the old pond.
Ground water hi MW-15 is downgradient of the
north landfarm and may have been contaminated
by the wastes deposited there; however, the PCP
concentrations in MW-15 were only slightly higher
than the detection limit. Concentrations of PCP in
MW-20 (110 to 4,400 ppb) and in IWB-170 (140
to 1,900 ppb) are quite high and are quite variable
over time. Concentrations increased after
remediation began, but did decrease in the third
304
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8
FLOW
; HORIZONTAL
MANIFOLD
HEADER -
2" GATE VALVE
3N EACH LINE
1
OIL STORAGE
DRUMS
flOOD GALLON OIL/HjO "\
\ RETENTION TANK }
3-WAY
BALL
GRAVITY OIL
DRAIN
OIL/WATER
SEPARATOR
O
£
>
u. o
2 O
o:
TO 10,000 GALLON
STORAGE TANK
(TANK CAR)
LEGEND
IX! GATE VALVE
IX] GLOBE VALVE
1X1 BALL VALVE
Source: B & F Engineering, 1990
Q.
0)
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OIL RECOVERY SYSTEM
MID-SOUTH WOOD PRODUCTS STO
-------
Ul
Table 4
CONCENTRATIONS OF CONTAMINANTS IN MONITORING WELLS
FOURTH QUARTER 1»S» TO THIRD QUARTER 1990
MID-SOUTH WOODS SITE
Page 1 of 2
MW-10
MW-12
MW-14
MW-15
MW-16
MW-17
MW-18
MW-20
IWB-170
Arsenic (ppb)
4Q89
<2
2.1
<2
<2
<2
4,8
10
5.1
<2
1090
9.3
<2
<2
2,4
3.2
5.9
16
2.7
3.3
2Q90
7.4
2.5
<2
2.7
<2
3.6
9.6
6.2
3.0
3Q90
6.9
,<2
<2
2.1
<2
2.4
7.7
11
<2
Chromium (ppb)
4Q89
<50
<50
<50
<50
<50
<50
<50
<50
<50
IQ90
<50
<50
<50
<50
<50
<50
<50
<50
<50
2Q90
<50
<50
52
80
<50
<50
<50
<50
<50
3Q90
<50
<50
<50
<50
<50
<50
<50
<50
<50
PCP (ppb)
4Q89
<1
<1
<1
2.2
<1
<1
<1
110.
140
1Q90
<1
<1
<1
<1
<1
<1
<1
320
1,700
2Q90
<1
<1
<1
<1
<1
<1
<1
4,400
1,900
3Q90
<1
<1
<1
2.1
<1
<1
<1
<1.
370
Sources: B&F Engineering, 1989, 1990a, 1990bt 199W, 1990e
Screened intervals (ft): .MW-10, 29 to 39; MW-12, 47 to 57; MW-14, 48 to 58; MW-15, 49 to 59; MW-16, 25 to 35; MW-17, 25 to 35; MW-
18, 26 to 36; MW-20, 30 to 40; IWB-170, 162 to 172
o
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Table 4
CONCENTRATIONS OF CONTAMINANTS IN MONITORING WELLS
FOURTH QUARTER 1989 TO THIRD QUARTER 1990
MID-SOUTH WOODS SITE
Page 2 of 2
MW-10
MW-12
MW-14
MW-15
MW-16
MW-17
MW-18
MW-20
IWB-170
Benzo(a)anthracene (ppb)
4Q89
<10
<10
<10
<10
<10
<10
<10
<10
<100
1Q90
<10
<10
<10
<10
<10
<10
<10
<100
<10
2Q90
<10
<10
<10
<10
<10
<10
<10
<10
<100
3Q90
<10
<10
<10
<10
<10
<10
<10
<10
<100
Benzo(b & k)fluoranthene (ppb)
4Q89
<20
<20
<20
<20
<20
<20
<20
<20
<200
1Q90
<20
<20
<20
<20
<20
<20
<20
<200
<20
2Q90
<10
<10
<10
<10
<10
<10
<10
<10
<100
3Q90
<10
<10
<10
<10
<10
<10
<10
<10
<100
Benzo(a)pyrene (ppb)
4Q89
<10
<10
<10
<10
<10
<10
<10
<10
<100
1Q90
<10
<10
<10
<10
<10
<10
<10
<100
<10
2Q90
<10
<10
<10
<10
-------
S
^~-
Table 5
MID-SOUTH WOOD RECOVERY SYSTEM: CONTAMINANT CONCENTRATIONS IN RECOVERY WELLS
FOURTH QUARTER 1989 TO THIRD QUARTER 1990
Page 1 of 2
RW-1
RW-2
RW-3
RW-4
RW-5
RW-6
RW-7
RW-8
RW-9
RW-10
RW-11
RW-12
RW-13
RW-14
RW-15
PCP(ppb)
4Q89
NS
17
NS
<1
160
26
27
2,500
NS
280
NS
<1
38
<1
15,000
1Q90
820
6.7
700
1.8
380
NS
280
1,700
1,500
120
370
4
200
1300
65,000
2Q90
900
2
280
1.7
360
2.1*
88
2,100
1,500
350
39
39
190
16
5,800
3090
1300
2.1
NS
NS
NS
NS
2.5
10,000
NS
5.7
66
NS
NS.
NS
3,700
Arsenic (ppb)
4Q89
NS
3.7
NS
<2
<2
6.6
16
11
NS
30
NS
<2
<2
<2
410
1090
17
3.6
<2
<2
<2
NS
6.2
5.3
<2
4.2
<2
3.8
6.5
2.9
16,000
2Q90
32
5.2
5.8
<2
2.7
3.5
50
8
4.6
2.6
<2
2.7
6.8
6
3
3Q90
36
6.5
NS
NS
NS
NS
31
94
4.6
16
<2
NS
NS
NS •
2,200
Chromium (ppb)
4Q89
NS
<50
NS
<50
<50
<50
<50
<50
NS
<50
NS
<50
<50
<50
840
1Q90
<50
<50
<50
<50
<50
NS
<50
<50
NS
<50
<50
<50
<50
<50
25,000
2090
<50
<50
<50
<50
<50
<50
<50
<50
<50
<50
<50
<50
<50
<50
620
3O90
<50
<50
NS
NS
NS
NS
<50
<50
<50
<50
<50
<50
NS
NS
200
i
-------
IO
O
Table 5
MID-SOUTH WOOD RECOVERY SYSTEM: CONTAMINANT CONCENTRATIONS IN RECOVERY WELLS
FOURTH QUARTER 1989 TO THIRD QUARTER 1990
Page 2 of 2
RW-1
RW-2
RW-3
RW-4
RW-5
RW-6
RW-7
RW-8
RW-9
RW-10
RW-11
RW-12
RW-13
RW-14
RW-15
Benzo(a)anthr»cene (ppb)
4Q89
NS
<10
NS
<10
<10
<10
<10
<10
NS
<10
NS
<10
-------
Mid-South Wood Products
quarter of 1990. The contamination in IWB-170 is
especially significant because it demonstrates that
contamination exists at depths of at least 172 feet
in the northwest corner of the old pond. The
extent of deep contamination is not known.
Additional study of the deep contamination was
considered too costly considering the complexity
of the site geology. The high variability and high
concentrations relative to the aqueous solubility of
PCP in Wells MW-20 and IWB-170 suggest that
the ground-water contamination in these wells may
be the result of dense, nonaqueous phase
liquidcontamination, especially considering the
depth of 1WB-170.
PCP and arsenic contamination was detected also
in the recovery wells shown in Table 5.
Consistently high concentrations of PCP and
arsenic were detected in RW-1, RW-8, and RW-
15, which pump from French drain systems in the
old plant and old pond areas. The liquids
collected in these drain systems include ground
water contaminated with dissolved constituents and
possibly some carrier oil contaminated with PCP.
The arsenic and chromium contamination in RW-
15-16,000 ppb and 25,000 ppb, respectively, in
the first quarter of 1990-was probably the result
of the CCA plant northeast of the French drain
pumped by RW-15. Chromium concentrations in
all recovery wells except RW-15 were below
detection limits during each of the four sampling
periods. PAHs were below detection in all
recovery wells.
The standards at which soil removal action would
be required for both arsenic and chromium are
based on background soil. Although chromium
and arsenic occur naturally in some soils in
concentrations as high as 5,000 ppb and 3,000
ppb, respectively, they were not found at this site
in background water samples. However, because
these metals are treated and discharged, they are
subject to compliance with NPDES daily
maximum discharge standards. The discharge
water standards are 50 ppb for both metals.
Arsenic and chromium concentrations comply with
this effluent standard even before treatment at all
monitoring and recovery well locations, with the
exception of RW-15, which is located in the
vicinity of the CCA treatment plant.
One of the factors that probably caused the
decrease in contaminant concentrations in ground
water from 1985 to the fourth quarter of 1989 was
the operation of the interim three-well recovery
system from early 1985 to mid-1989. Natural
attenuation and downward and lateral migration of
the contaminant are other factors. The operation
of the full-scale 15-well recovery system starting
in mid-1989 also probably contributed to the
reductions observed by the fourth quarter of 1989.
It is difficult to assess the lateral extent of the
improvement in ground-water quality. Because of
the complex fracture system and the potentially
limited interconnection between fractures, it is
possible that the improvements in water quality are
not laterally extensive and that substantial pockets
of contamination remain. Also, because the
French drains were excavated to relatively shallow
depths, the remediation system addresses only
shallow ground-water contamination and the
removal of LNAPLs. The system does not address
contamination by the dense, nonaqueous phase
liquids that are believed to exist at the site.
SUMMARY OF REMEDIATION
The Mid-South Wood site has been contaminated
by spills of wood treatment chemicals and by
disposal of these materials in open ponds.
Contamination occurred both onsite and offsite in
soils, surface water, and ground water.
Contaminants of concern for ground water are
PCP, a suite of creosote compounds (PAHs),
arsenic, and chromium. None of these is known
to be native at detectable levels in ground water.
The primary sources of PCP and creosote
contamination were the old plant and the old pond.
The main source of metals contamination was the
CCA treatment facility.
Remedial action was initiated to address both the
soil and ground-water contamination at the site.
Action included consolidating and capping
contaminated soils in the landfarms and
implementing a French drain and drilled well
recovery system for contaminated ground water.
An interim system of three French drains with
recovery Wells (RW-1, RW-2, and RW-3) began
operating in early 1985. The current system of 8
French drains and 15 recovery wells began
operating in the summer of 1989.
Monitoring- and recovery-well data from the first
four quarters of operation in 1989 and 1990, when
compared to data from 1984 and 1985, provided
the basis for the evaluation of the system.
Drawing definitive conclusions from the limited
310
-------
Mid-South Wood Products
data would be premature. In general, however, the
data show that concentrations were significantly
lower in 1989 and 1990 than in 1984 and 1985.
The PAH compounds that were analyzed-
chrysene, benzo(a)anthracene, benzo (b+k)
fluoranthene, and behzo(a)pyrene—were not found
in 1989 and 1§90 in concentrations that exceed
health-based standards in any of the wells
sampled. Arsenic and chromium were also near or
below detection limits in all wells, with the
exception of recovery Well RW-15, in 1989 and
1990. The arsenic and chromium in RW-15 are
believed to be the result of contamination
originating from the CCA treatment plant.
Significant concentrations of PCP were found in
two monitoring wells (MW-20 and IWB-170) and
in several recovery wells in 1989 and 1990. The
PCP found in MW-20 and in the recovery wells is
probably due to the dissolution of PCP from
sources in the waste ponds and landfarrns, and the
interception of light free-phase carrier oils
containing PCP. LNAPL contamination by oils
has been observed within the French drain
recovery system (U.S. EPA, 1991b). The presence
of high concentrations of PCP in IWB-170 at a
depth of 172 feet is a strong indication of dense
free-phase (DNAPL) contamination. Evidence of
free-phase contamination was observed directly in
fractures in core samples taken from the deepest
intervals of IWB-170 (U.S. EPA, 1991b). The
limits of the depth of contamination in other areas
was reported to be 60 feet (B&F Engineering,
1991b); however, no other wells were deeper than
59 feet as of the end of 1989 (B&F Engineering,
1989). Because of the high cost of investigating
deep DNAPL contamination in fractured rock, and
the fact that the deep aquifer was not used as a
water supply, additional investigations were not
considered cost-effective.
The general reduction in contaminant
concentrations observed in ground water from
1985 to 1990 can be attributed in part to the
ground-water recovery system. The operation of
the 3-well extraction system from early 1985 to
mid-1989 and of the 15-welI system from mid-
1989 to the fourth quarter of 1989 probably
decreased concentrations to some degree; however,
it is also possible that the contaminants were
attenuated naturally from 1985 to 1989 or migrated
laterally or downward because of ground-water
gradients or contaminant density. Because of the
complex fracture system and the possibility that
the fractures intercepted by the recovery system
may not be connected to other highly contaminated
fractures nearby, it is difficult to draw conclusions
about overall ground-water cleanup at the site.
The fracture system is highly heterogeneous; as a
result, adjacent sampling points may contain
significantly different concentrations of
contaminants. This heterogeneity in contaminant
distribution is compounded by the presence of
LNAPL and DNAPL contamination.
The data shown in Tables 4 and 5 suggest that
there is little evidence of residual creosote
contamination at the site. However, the lack of
detectable concentrations of creosote in the form
of three PAHs in 1989 and 1990 may be a result
of the placement of the recovery and monitoring
system at shallow depths. The aqueous solubility
of PAHs is also generally below the detection
limits shown in these tables, which means that it
would be possible to have nearby DNAPL pools
without exceeding the detection limits. Creosote
has a tendency to exist as a DNAPL because of its
density of approximately 1.05 g/cm3 and its
viscosity, which is 50 to 70 times that of water.
The absence of creosote contamination in recent
ground-water samples despite the use of creosote
as a wood treatment liquid from approximately
1955 to 1977 may be due to the downward
migration of most of the creosote contamination
below the monitoring and recovery system.
Therefore, it is possible that DNAPL creosote
contamination exists at depth and is undetected by
the existing system. The evidence for the
existence of PCP, a treatment compound used
from 1967 to 1977, in DNAPL at depths of at
least 172 feet is strong because of the high
concentrations of dissolved PCP found (14% of
aqueous solubility). DNAPL observed in fractures
down to 172 feet may consist of both PCP and
creosote; however, only PCP was detected in the
deep ground-water samples.
Pathways for potential migration of dissolved
constituents are primarily to the west from the old
plant and small pond areas, although some
contamination may migrate east from the old plant.
Some of the contaminants that originated in the
source areas appear to be migrating directly to
Moon Spring along the fault zone. These
contaminants are at relatively shallow depths due
to vertical upward gradients in the fault zone.
Contamination is also suspected at the railroad
tracks to the south. Downward migration by
311
-------
Mid-South Wood Products
DNAPLs is another potential contaminant
migration pathway.
SUMMARY OF NAPL-RELATED
ISSUES
The presence of LNAPL contamination by carrier
oils at the Mid-South Wood site has been observed
directly. LNAPL and shallow, dissolved
contamination have been the focus of site
investigations and remediation to date. However,
it is also known that some onsite DNAPL
contamination exists, particularly along the fault
line. Although preliminary analytical results from
ground-water sampling revealed that levels of
onsite contaminants, including PCP and PAHs,
were generally reduced, these concentrations
cannot be interpreted to preclude the possibility
that DNAPLs eventually will be detected in
ground-water samples from'the current monitoring
network. The presence of several PAHs and PCP
at concentrations greater than their aqueous
solubility in 1984 and 1985 suggests that DNAPLs
were present at that tune. DNAPLs were observed
to depths of 172 ft during deep drilling.
Free oil containing creosote compounds and/or
PCP, was disposed of onsite in the old plant and
old pond areas over a period of more than two
decades. Some free phase creosote was also
disposed of during this period. Creosote and PCP
have chemical properties that tend to favor their
accumulation and migration as DNAPLs. For
example, PCP and the PAH compounds have
densities greater than that of water, which favors
their downward migration in the saturated zone.
The density of PCP is 2.0 g/cm3, and the density
of most of the PAH compounds is approximately
1.2 g/cm3. Free phase compounds with these
densities can migrate downward readily, regardless
of hydraulic gradients.
The high viscosity of creosote inhibits its recovery,
particularly in gravity flow systems such as French
drains. Creosote's high viscosity greatly decreases
its mobility in response to hydraulic gradients and
may account for the failure to detect PAHs in
1989 and 1990 (see Tables 3 and 4). The
principal migration direction of creosote is
expected to be downward through the complex
fracture network rather than lateral in response to
hydraulic gradients.
DNAPL migration is affected by the geologic
structure of the site. The fault zpne at Mid-South
Wood is characterized by highly fractured rocks
that may provide an effective pathway for
downward DNAPL migration. At the time of the
remedial investigation, there was evidence of
migration into the underlying shale and residual
contamination in the fracture zone. Even if
capping the contaminated soils inhibited additional
migration of contaminants' dissolved in ground
water, DNAPL contaminants may continue to
migrate downward into the fractured rock. Site
investigations also revealed that, due to the
fractured bedrock in the remedial areas, not all
contamination can be collected by the ground-
water recovery and treatment system (U-S. EPA,
1986b). Obtaining comprehensive data about
DNAPL migration in fractured-rock systems,
however, is technologically complex, and in this
case was considered economically prohibitive.
312
-------
BIBLIOGRAPHY/REFERENCES
B&F Engineering, Inc. September 8, 1986.
Proposed Remedial Action Plan, Mid-South Wood
Products Superfund Site, Mena, Arkansas.
B&F Engineering, Inc. May 15, 1987. Free Oils
Investigation, Mid-South Wood Products, Mena,
Arkansas.
B&F Engineering, Inc. September 26, 1989.
Monitoring Well Sampling and Analysis Plan,
Mid-South Superfund Site, Mena, Arkansas.
B&F Engineering, Inc. February 1990a. Fourth
Quarter 1989 Ground Water Monitoring Report,
Mid-South Superfund Site.
B&F Engineering, Inc. May 3, 1990b. First
Quarter 1990 Ground Water Monitoring Report,
Mid-South Superfund Site.
B&F Engineering, Inc. May 1990c. Operation
and Maintenance Manual, Superfund Remediation,
Mid-South Wood Products Site, Mena, Arkansas.
B&F Engineering, Inc. May 31, 1990d. Second
Quarter 1990 Ground Water Monitoring Report,
Mid-South Superfund Site.
B&F Engineering^ Inc. November 29, 1990e.
Third Quarter 1990 Ground Water Monitoring
Report, Mid-South Superfund Site.
B&F Engineering, Inc. March 21, 1991(a).
Personal Communication with William Fletcher,
President.
B&F Engineering, Inc. June 4, 1991(b). Letter
from Bill Fletcher to Jennifer Sutler of EPA
Headquarters.
U.S. Environmental Protection Agency (U.S.
EPA). December 1982. Aquatic Fate Process
Data for Organic Priority Pollutants, EPA-440/4-
81-014.
U.S. EPA, Region VI. October 24, 1984.
Remedial Investigation Report, Mid-South Wood
Products, Mena, Arkansas, Volume I.
U.S. EPA, Region VI. March 13, 1986a.
Supplemental Remedial Investigation, CCA Plant,
Mid-South Wood Products Site, Mena, Arkansas.
Mid-South Wood Products
U.S. EPA, Region VI. April 1986b. Feasibility
Study, Mid-South Wood Products Site, Mena,
Arkansas.
U.S. EPA, Region VI. November 14, 1986c.
Record of Decision, Mid-South Wood Products
Site, Mena, Arkansas.
U.S. EPA, February 20, 1991a. Personal
cqmmunication with Cathy D. Gilmore, Remedial
Project Manager, Environmental Protection
Agency, Region VI.
U.S. EPA, Region VI. April 16, 199 Ib. Personal
communication with Lou Barinka.
313
-------
CASE STUDY 21
Occidental Chemical
Lathrop, California
Abstract
The soils and ground water underlying the Occidental Chemical site have been
contaminated with pesticides as a result of past handling and disposal practices. The
primary contaminant of concern at the site is dibromochloropropane (DBCP), because of its
high mobility and known sterilizing effect on humans. The extraction system, which
consists of six extraction wells, began operation in 1982. The system appears to capture
most of the existing contaminant plume. Concentrations of pesticides have decreased
substantially since extraction began. The installation of two additional extraction wells,
EW-6 and EW-7, is planned for 1991.
Background Data
Date of Problem Identification
Extraction Started
Types of Contaminants
Primary Aquifer Materials
Maximum Number of Extraction Wells
Maximum Total Extraction Rate
Estimated Plume Area
Estimated Plume Thickness
Maximum Reported Concentrations
1977
June 1982
Pesticides
Interbedded alluvial sand,
silt, and clay
6
600 gpm
770 acres
190 feet
Dibromochloro-propane:
4,200 ppb
314
ISLClt
-------
CASE STUDY
OCCIDENTAL CHEMICAL SITE
BACKGROUND OF THE PROBLEM
The Occidental Chemical site is located in
Lathrop, California, approximately 60 miles east of
Oakland, in California's Central Valley (see Figure
1). A pesticide and fertilizer plant was operated at
the site by Occidental Chemical from 1953 to
1983. Past handling and disposal practices at the
site have resulted in contamination of the soil and
ground water underlying the area. The site is on
the southern limit of the town of Lathrop in an
area of light commercial and industrial activity.
The primary contaminants "of concern at the site
are dibromochloro-propane (DBCP) and ethylene
dibromide (EDB), both of which are fumigant
pesticides. Site remediation is administered by the
State of California and the U.S. EPA (EPA)
National Enforcement Investigation Center.
Because the initial site investigation began before
the Superfund legislation was passed in 1980, the
remedial action is driven by a 1981 consent decree
rather than by Superfund.
SITE HISTORY
The Occidental Chemical plant began operating in
1953 and began producing pesticides as early as
1957. A contamination problem was first
discovered in 1977 when it was found that a
substantial percentage of the plant workers were
sterile-possibly as a result of exposure to DBCP.
Concern over possible ground-water contamination
led to a cease and desist order by the California
Central Valley Regional Water Quality Control
Board on April 27, 1979, which required the
contamination to be characterized (COM, 1983).
In mid-1979, the EPA conducted an extensive
environmental audit of post-disposal practices. In
December 1979, the U.S. and the State of
California filed suit against Occidental (U.S. EPA,
January 199 la).
In response to the legal actions taken in 1979, a
large-scale investigation of the contamination of
soils and ground water at and near the site was
conducted in 1980. This investigation included the
installation and sampling of 43 onsite and offsite
monitoring wells, the sampling of 31 nearby wa-
ter-supply wells, extensive soil sampling, and the
excavation of several trenches in the western third
of the site to identify buried wastes. Monitoring
wells at locations PW-1 through PW-14 shown in
Figure 2 were installed during 1980.
These initial samples revealed low concentrations
of DBCP in several offsite watersupply wells, and
extensive onsite contamination of ground water
and soils. A total of 21 pesticides were detected in
the 43 onsite monitoring wells. The excavation
work in the western storage area intercepted four
major disposal trenches and a number of smaller
disposal pits. Many of the disposal pits and
trenches were found to contain bottles and other
product containers, some of which were filled with
liquid pesticides. Some wastes in these disposal
areas were below the water table (Canonic
Environmental, 1981). A report summarizing the
results of this Phase I investigation was submitted
by Occidental Chemical in December 1980
(Canonic Environmental, 1980).
On February 6, 1981, a consent decree was signed
which established the framework for future site
investigations and remediation. The plan called
for excavation and ' offsite disposal of source
material from the disposal pits and contaminated
soils from several areas of the site. The offsite
disposal of the wastes from the pits was completed
in 1981. Some source areas on site were capped
instead of being removed. Additional monitoring
wells and a ground-water extraction, treatment, and
reinjection system were also installed. The
remediation system, consisting of five extraction
wells, two injection wells, and a carbon adsorption
treatment system, began operating on June 22,
1982.
Other remedial activities or administrative actions
since the startup of the remediation system
include: (1) the sale of the Occidental property to
the J. R. Simplot Company in January 1983, (with
responsibility for remediation retained by
Occidental), (2) the demolition of the DBCP plant
and excavation of soils in its vicinity in late 1983,
(3) the addition of six monitoring wells in 1986,
(4) the discovery, assessment, and excavation of
an area of high pesticide contamination in soils
315
I ADI Well
-------
Occidental Chemical
o
1
S
f
o
o
o
a
316
-------
Occidental Chemical
Louis* Aw.
»-it
UbbT
Own*
I Fart
IW-41
f«-t*
Western Storage Area
PV-S4
a PW - Moniumng We!t«
S EW-fxtraetlon Weils
• IW . Infection Wells
Notes: Only monitoring wells a! locations PW-1 to
PW-14 were installed by the end of 1980. Extraction
and tnjecton wetls began operating in June 1982.
Railroad Siding
Excavat-on
Plaat Bauodmrr
Souic*: Weston. Inc., 1990
SOU (f«t)
Flgura2
WELL LOCATION MAP, 1989
OC5CID»ITAL CHEMICAL SITE
317
PC?
-------
Occidental Chemical
underlying a railroad siding in the southeast part of
the site from 19SS through 1988 (Weston, 1987a,
1988b, 1989a), and (5) the addition of .monitoring
Well PW-22-71 to the extraction system in
December 1989. Other routine maintenance work
on the injection and extraction wells was
performed in 1989 and 1990, The installation of
two additional extraction wells, EW-6 and EW-7,
is planned in 1991 (U.S. EPA, May 14,1991).
GEOLOGY
The Occidental Chemical site is located in the
center of the Central Valley, approximately half
way between the Sierra Nevada mountains on the
east and the Coast Range mountains on the west
The western boundary of the site is approximately
two miles east of the San Joaquln River,
The site is underlain by several hundred feet of
unconsolidated alluvial and marine sediments of
Tertiary and Quaternary age. These sediments
consist of interbedded sands, clays, and silts, with
occasional gravels. Individual strata vary in
thickness from 1 to 100 feet and are commonly
discontinuous. Figure 3 is an east-west cross
section across the Central Valley along a transect
approximately 2 miles south of the site. This
figure shows the complex stratigraphy of discon-
tinuous and intergraded beds that characterizes the
geology of the region.
Geologic logs recorded during drilling at the site
show that its stratigraphy consists of interbedded
and discontinuous beds of sand and clay similar to
the stratigraphy shown in Figure 3. Two
important differences are: (1) that sand and gravel
beds appear to constitute approximately 40 percent
of the sediment thickness of the upper aquifer on
site, and (2) the Corcoran clay member is
continuous across the site (Canonic Environmental,
1980). The thickness of the Corcoran clay is
approximately 50 feet. A cross section of the
stratigraphy along the western boundary of the
plant, from PW-7 to PW-12, is shown in Figure 4.
HYDROGEOLOGY
The sediments underlying the Occidental Chemical
site can be divided into three distinct
hydrogeologie units-~a . 250-foot-thick upper
aquifer, the 50-foot-thick Corcoran clay confining
unit, and a 200-foot-thick lower aquifer. The
upper aquifer is an important regional water-supply
aquifer. It is generally unconflned
with the exception of a few areas that are confined
by overlying impermeable sediments. The lower
aquifer is confined and contains brackish ground
water with high chloride concentrations. As
shown in Figure 4, these zones can only be loosely
correlated across the site.
The upper aquifer is divided into three partially
coupled permeable zones. These three zones
consist of a shallow zone from 31 to 83 feet, an
intermediate zone From 84 to 150 feet, and a deep
zone from 151 to 218 feet. These three zones can
only be loosely correlated across the site, as shown
in Figure 4. The top of the Corcoran clay is
approximately 250 feet below land surface but is
deeper in some areas. There is a downward
gradient of approximately 1 foot per 50 vertical
feet within the upper aquifer (Canonie
Environmental, 1980).
Ground water has been used extensively for
irrigation over a period of several decades in the
region surrounding the site. The site is at the edge
of a broad cone of depression centered around the
city of Stockton eight miles north of the plant.
Water levels on site depend on a complex pattern
of agricultural and industrial pumping in the
vicinity of the site; however, the direction of
horizontal ground-water flow is generally to the
west or northwest towards the San Joaquin River.
During periods of high pumping, ground water
flows to the north in the northern third of the site.
The response to pumping is greatest to the deep
zone of the upper aquifer. Horizontal gradients
are generally 1/1000 to 5/1000 ft/ft at the site.
A 25-hour aquifer test of a production well
screened from 210 to 270 feet in the deep zone of
the upper aquifer was performed in August 1980.
The results of this test showed that the regional
aquifer has a transmissivity of 21,000 gallons per
day per foot, a hydraulic conductivity of 2 x 10"2
cm/sec, and a storage coefficient of 7 x 10"5, The
low storage coefficient demonstrates that the deep
zone of the upper aquifer is confined in the
vicinity of this production well. The 1980 aquifer
test also showed that the vertical hydraulic
conductivity of the clay aquitard overlying the
production zone is estimated to be 1 x 10
cm/sec. A second aquifer test was performed at
the site in November, 1985 (Weston, 1986);
however, the results of this test were not available.
318
-------
LEQEND
400 —
300 —
200 -
100 —
S»aL«vtl —
-100 —
FemMtan Contact
WM«rW*H
•200.
-300 —
-400
•500-
Source: Canonfe EnvtroraiMntal, 1980
F1{}UT«3
EAST-WEST CROSS SECTION
THROUGH THE CENTRAL VALLEY
TWO MILES SOUTH OF THE SITE
OCCIDENTAL CHEMICAL SITE
o
8
I
i
o
y.
s
-------
Occidental Chemical
SOUTH WB»T
PW-7 PW-S
1 1
P
8
8
Norm.-
1_OGWJOTW M
NOT TO 1" "
PW-8
I
NOJCTMEA5T
PW-10 PW-12
WVLU
ZONK.
flft-IO« TMOC)
Source: Canonto Erwirenmentai, 1980
noun 4
SITE GEOLOGICAL CROSS SECTION
ALONG WESTERN PLANT BOUNDARY
OCCIDENTAL CHEMICAL SITE
320
-------
Occidental Chemical
WASTE CHARACTERISTICS AND
POTENTIAL SOURCES
The ground water underlying the Occidental
Chemical site has been heavily contaminated with
a number of pesticides as a result of past disposal
practices. During initial sampling of 43
monitoring wells in 1980, 21 different pesticides
were detected. Table 1 lists these 21 pesticides.
The pesticides dibromochloropropane (DBCP) and
ethylene dibromide (EDB) are the primary contam-
inants of concern. Only DBCP was found in a
majority of the monitoring wells. -Both
compounds are nematocidal fumigant pesticides.
The isomers of the pesticide BHC, including
lindane, were also common.
DBCP is a highly toxic pesticide that is known to
have a sterilizing effect upon exposure. DBCP is
highly mobile and has a high solubility in water
(1,230,000 ppb). Because of its high toxicity and
its high mobility and persistence in soil and
ground water, the EPA phased out the use of
DBCP from 1077 to 1979. The current Proposed
Maximum Contaminant Level (PMCL) for DBCP
is 0.2 ppb. EDB is also highly soluble (4,310,000
ppb) and mobile in water (U.S. EPA, 1987). It is
known to be a potent carcinogen in rats. The
current proposed MCL for EDB is 0.05 ppb. The
use of EDB was banned by the EPA in 1983.
The environmental audit of the Occidental
Chemical plant conducted in the late 1970's
showed that past liquid and solid waste disposal
led to the contamination of soil and ground water
at the site. Until at least 1970, waste pesticide
solids and concentrated liquids were disposed of
onsite in shallow trenches in the western storage
area shown in Figure 1. A number of these
trenches were excavated in 1980 and found to
contain bottles and other containers of pesticides.
Liquid wastes were also disposed of in unlined
ditches and ponds in permeable soils until at least
1976. Several separate source areas have been
capped, or excavated and removed, since remedial
activities began in 1980.
DBCP was found at a maximum concentration of
1,200 ppb in one 200-foot-deep well during early
sampling. It was also detected at a concentration
of 4 ppb in a private well 0.5 miles north of the
Occidental Chemical plant (U.S. EPA, 1985).
Contamination by DBCP was distributed widely
throughout the site in 1980, but was generally
highest at PW-6 near the western storage area.
EDB contamination was also widespread in the
western third of the site and in adjacent offsite
areas in 1980. Remediation efforts have focussed
on DBCP because it is the most mobile of the
contaminants of concern.
Figures 5, 6, and 7 show the distribution of DBCP
in the shallow, intermediate, and deep zones,
respectively, in October 1982, shortly after
remediation began. These figures show that
DBCP contamination is greatest along the western
boundary of the plant and offsite to the west.
Contamination extended slightly farther to the west
in the intermediate and deep zones than in the
shallow zone in October 1982.
REMEDIATION
Selection and Design
of the Remedy
The stated objectives of the remediation system at
the Occidental Chemical site are to contain the
contaminant plume in the upper aquifer by ground-
water extraction, and to treat the extracted ground
water to an effluent DBCP concentration of 1 ppb,
or less, before injecting it into the lower aquifer
(Weston, 1990). Aquifer restoration is also an
objective of remediation, as stated in the consent
decree, according to the EPA, NEIC (1991c).
Steps taken to improve ground-water cleanup have
included redistribution of pumping to high
concentration areas, conversion of PW-22 to an
extraction well, and an increase in treatment
system capacity (EPA, NEIC, 1991a.)
The remediation system consists of six extraction
wells and two injection wells. The two injection
wells are used to inject the treated effluent water
into the brackish aquifer that underlies the
Corcoran clay at a depth of 300 to 500 feet. A
system of 69 monitoring wells is used to monitor
the progress of remediation and to check on the
integrity of the clay layer separating the two
aquifers. Sixty-five of these wells are installed in
the upper aquifer, primarily in groups of three
wells, each of which is installed in one of the
three zones of the upper aquifer. Eight of the 69
wells are used to monitor the hydraulic separation
between the upper and lower aquifers.
321
-------
Occidental Chemical
Table 1
PESTICIDES DETECTED IN INITIAL 1980 MONITORING WELL SAMPLING
OCCIDENTAL CHEMICAL SITE
(Total Number of Wells = 42)
Chemical
DBCP
Lindane
a-BHC
A-BHC
EDB
2,4-D
Disyston
Delnav
Dimethoate
Dieldrin
Sevin
2,4,5-T
Thiodan I
HCB
p,p'-DDT
Toxaphene
Chlordanc
DDE
Ethyl Parathion
DEF
Methyl
Parathion
Number of
Wells Where
Detected
33
21
19
13
11
8
6
5
4
3
3
3
2
2
1
1
1
1
1
1
1
Detection
Limit
(PPb)
0.1
0.05
0.05
0.05
1.0
2.0
1.0
1.0
1.0
0.05
30
0.5
0.05
0.05
. 0.05
5
0.5
0.05
1.0
1.0
1.0
Range
(ppb)
0.13-1240
0.06-14,85'
0.08-9.15
0.09-5.6
1.0-49.4
1.8-4
2.0-6.2
1.8-25.2
1.8-15.2
0.05^0.3
30-80
1.0-1.4
-
-
-
-
-
-
-
-
-
Median
(PPb)
168
2.3
1.7
2.65
7.4
3
3.2
6.5
11.2
0.05
70
1.4
0.05
0.05
0.90
8.2
0.53
0.59
3.3
1.7
2.5
MCL/
PMCL
-/0.2
4/0.2
-
-
-/0.05
100/70
-
-
-
-
-
10/50
-
-
-
5/5
-a
-
-
-
-
Source: Canonic Environmental, 1980
MCL= Maximum Contaminant Level, Safe Drinking Water Act (SDWA)
PMCL= Proposed Maximum Contaminant Level
"-" = No standard or standard not known
322
-------
Occidental Chemical
PW. Monitoring W«lls
EW. Extraction WMls
IW - Infection W«lls
SCALE
0 1,375
1,375-
DISTRIBUTION OF DBCP (potl) IN THE SHALLOW ZONE,
3143 FOOT LEVEL-OCTOBER 1882
OCCIDENTAL CHEMICAL SITE
323
-------
Occidental Chemical
» *
WM1 NDPW-13
ND /
ND
PW-20
Q.2 MUM
OeeMmtaf Cfwmictf Co.
Plant Boundary
PW-Monitoring WWIs
EW • Extraction Walls
IW * Injection Wtlis
Souiea: Wtrton, Inc., 19B4
SCALE
0 1475
Figures
DISTRIBUTION OF DBCP (ppb)
IN THE INTERMEDIATE ZONE,
KM50 FOOTHVEi-OCTOBiR 1982
OOJIDENTOL CHEMICW. SITE
324
/ao
-------
Occidental Chemical
2y / / / «**-•
/•/If "w-'z^-
////yaio^
SS.n '////.51-rj
1. *•" b^ / f/J^?/'
~" -b^3 yi/.V iW
PW - Monttorlng Walls
EW-Injection Walla
DISTRIBUTION OF DBCP
-------
Figure 2 shows the remediation system as it has
existed since 1989. The five main extraction wells
arc designated EW-1 through EW-5. EW-1 and
EW-2 are north of the plant, EW-3 is north of the
western storage area, and EW-4 and EW-5 are
offsite to the west of the plant. The placement
and pumping rates of the five extraction wells
were chosen using computer modeling completed
in 1981. The system is designed to intercept the
prevailing offsite ground-water flow to the north
and west. These five extraction wells began
pumping at approximately 500 gpm on June 22,
' 1982, Their combined pumping rate in January
1991, was 600 gpm "(U.S. EPA, 19"9"la). '
Monitoring Well PW-22-71 (PW-22, shallow zone)
was converted to an extraction well in December
1989, and is pumped intermittently at an average
rate of approximately 0,56 gpm. The pumping
history and screened interval of the five main
extraction wells is shown in Table 2. EW-1 is
screened over part of both the intermediate and the
deep zone, EW-2 is screened over the deep zone
only, and EW-3, EW-4, and EW-5 are screened
over all three zones. The pumping program was
changed from a seasonal to year-round in October
1985, to enhance hydraulic control in the western
part of the site. The addition of two more
extraction wells, EW-6 near PW-10 and EW-7
near EW-5, has been proposed to increase the rate
of contaminant recovery, but these wells had not
been installed as of May 1991. Installation is
planned by the end of 1991.
The extracted ground water is treated by carbon
adsorption before being injected into the brackish
lower aquifer that underlies the Corcoran clay.
The carbon adsorption system is fairly effective in
removing most of the contaminant pesticides;
however, the solvent sulfolane, which was used in
a past manufacturing process, is not removed.
Sulfolane is found throughout the site; however, it
is of less concern than DBCP because it is
believed to have a low toxicity. (U.S. EPA,
199 Ib).
The monitoring well system is sampled three times
a year-in February, June, and October. Wells
from the Lathrop water district are sampled six
times a year. The analytical parameters used in
the ground-water sampling program are shown in
Table 3. The ground-water samples are analyzed
for inorganics, pesticides, herbicides, BHC
isomers, sulfolane, and radiologic parameters.
Occidental Chemical
EVALUATION OF PERFORMANCE
The extraction system at the Occidental Chemical
site has generally been effective in controlling the
contaminant plume in all three zones since the
system began operating in June 1982. The general
pattern of ground-water flow in the area of the
plant has varied since startup because of periodic
changes in nearby water-supply pumping and in
the distribution of natural and artificial recharge.
Despite seasonal variations in pumping, the
piezometric surface in all three zones has been
drawn down by the extraction wells to create a
northeast-southwest trending trough that transects
the northern third of the plant area. Ground water
north of the plant generally flows southeast toward
the trough and then turns to flow southwest in the
area underlying the northern third of the site.
Ground water in the southern two-thirds of the site
generally flows northwest toward the trough and
then turns to flow southwest in the area west of
the plant bopndary,
Figures 8, 9, and 10 are contour plots of the water
levels in the shallow, intemediate, and deep zones
of the upper aquifer, respectively, during June
1989, October 1989, and February 1990. These
figures illustrate the trough in die piezometric
surface at each depth along an axis connecting
extraction Wells EW-1 and EW-2 north of the
plant, EW-3 in the center of the site, and EW-4
west of the plant during 1989 and 1990.
Contaminated ground water flowing inward
towards the trough of depression in the area east
of EW-4 appears to be captured by the extraction
network. Contaminated ground water in the area
west of EW-4 does not appear to be captured by
the existing extraction system.
Hydraulic control was not achieved in the deep
zone underlying the area northwest of the site in
June 1989. This lack of control was reported to
be the result of high-volume pumping north of the
site during the summer. Some intermittent periods
of ineffective hydraulic control in the south and
southwest from 1983 through 1987 were also
reported (Western, 1984, 1985a, 1986, 1987,
1988a). Hydraulic control was achieved in these
areas in 1988 and 1989 as a result of
improvements in the extraction system in 1987 and
1988 (Western, 1989b, 1990). In general, the
extraction system has created a trough of
depression that appears to have captured the bulk
326
-------
Occidental Chemical
Table 2
EXTRACTION WELL DATA
Well
EW-1
EW-2
EW-3
EW-4
EW-5
Depth
(ft)
220
220
210
200
170
Screen
Interval
135 to 210
150 to 210
60 to 94
134 to 200
70 to 120
170 to 190
70 to 160
Pumping Rate
Prior to
10/85
(gpm)
150 summer
100 winter
150 summer
100 winter
200 summer
150 winter
0 summer
75 winter
0 summer
75 winter
Pumping Rate
After 10/85
(gpm)
100
100
150
75
75
Pumping
Rate
After 10/88
(gpm)
100
100
180
50
75
Source: Weston, 1990
of the contaminant plume since startup in 1982,
despite anomalous periods of ineffective control in
some areas. Some contaminated ground water in
areas west of EW-4 may have flowed beyond the
limits of the capture zone since 1982.
The size and concentration of the pesticide plume
has decreased substantially since the extraction
system began operation in June 1982. Figure 11
shows concentration isopleths and trend surface
contour plots of the DBCP distribution in the
shallow, intermediate, and deep zones in February
1990. Trend surface analysis is a statistical
averaging technique that shows overall trends in
the concentration data, while reducing the
weighting of anomalously high values. Reference
to the corresponding contour plot of the
concentration of DBCP in the shallow zone in
October 1982 (Figure 5) shows that DBCP
concentrations have been reduced to less than 1/10
of their earlier levels in the shallow zone over
most of the site. For example, the concentration
of DBCP in the shallow zone decreased from 355
ppb to 12 ppb in PW-10, and from 487 ppb to 1.2
ppb in PW-8 from October 1982 to February 1990.
The concentration of DBCP in the shallow well at
PW-22 was higher in February 1990 (290 ppb)
than in October 1982 (180 ppb); however, the
decrease in DBCP concentrations observed in
nearby wells suggests that the high concentration
in PW-22 may be quite localized. The
concentration of DBCP in the shallow well at
PW-22 was 10.1 ppb in June 1989 suggesting that
the concentration in this well may also be quite
variable.
A comparison of October 1982 concentrations
shown in Figures 6 and 7 to February 1990
concentrations shown in Figure 11 demonstrates
that the concentration of DBCP has also decreased
substantially in the intermediate and deep zones of
the upper aquifer. Intermediate zone
concentrations decreased from 135 to 2 ppb in
PW-8, from 224 to 15 ppb in PW-7, from 203 to
0.1 ppb in PW-10, and from 210 to 0.5 ppb in
PW-12. Similar reductions were observed in the
deep zone. However, the concentrations varied
substantially between sampling events in some
cases.
Figure 12 is a three-dimensional plot of the trend
surface of DBCP concentrations in the three zones
from October 1982 to February 1990. This figure
clearly shows that the concentration of DBCP has
decreased substantially since 1982. Note that the
vertical scale used for the February 1990 data is
twice that used in the other two plots, so
reductions are even greater than they appear.
327
-------
Table 3
SAMPLING AND ANALYTICAL SCHEDULE, PERMANENT MONITORING (PW),
AND LATHROP DISTRICT WELLS
PERMANENT MONITORING WELL OPERATIONS
Sampling
Frequency: 3 times yearly - Feb., June, and Oct.
Location: All PW wells
Analysis Required
Parameter
DBCP/EDB
Sulfolane
Inorganics1
Nitrate
BHC Isomers6
Radiological5
Uranium only
Frequency
All sampling periods
All sampling periods
All sampling periods
October only
October only
Every other October*
Every other October*
*Odd number years
LATHROP WATER DISTRICT WELL OPERATIONS
Sampling
Frequency: 6 times yearly - Feb., April, June, Aug., Oct., and Dec.
Location: All operating wells
Analysis Required
Parameter
DBCP/EDB
Sulfolane
Inorganics1
Nitrate
Uranium only
Organochlorine2
Organophosphorous3
BHC Isomers6
Herbicides4
Radiological5
Frequency
All sampling periods
All sampling periods
All sampling periods
October only
All sampling periods *
October only
October only
October only
October only
October only
LEGEND:
1. Inorganics
pH, Conductivity, SO4, Cl
2. Organochloride Scan
Aldrin DDT
Chlordane Dieldrin
ODD Heptachlor
DDE Toxaphene
3. Organophosphorous Scan
DEF Ethyl Parathion
Delnav Methyl Parathion
Dimethoate Disyston
4.
Herbicides
2,4-D
2,4,5-T
5. Radiological
Gross Alpha
Radium 226
Total Uranium
Gross Beta
6. BHC Isomers
A-BHC D-BHC
B-BHC G-BHC
Source: Weston, 1990
328
-------
jam IM»
OCTOMM1M*
Sourc«:W»s)on. Inc. 1990
(Poor Quality Original)
Figure 8
CONTOUR PLOTS OF WATER LiVEL ELEVATIONS
IN THE SHALLOW ZONE, 1969 AND 1990
OCCIDENTAL CHEMICAL SITE
Q.
-------
OCTOMM 1»M
Sourc*: W«ston, Inc., 1990
C«MTOUI1 PLOTS OF WATER LEVEL ELEVATIONS
m m£ WTERMEDIATE ZONE| Ii8a M01890
OCCIDENTAL CHEMICAL SITE
o
O
*
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-------
OJ
UJ
O
OCTOKN 1*m
FCWtMNY 1MO
Source: Wwton, Inc.. 1990
RgurelO
(Poor Qualttv Ortaliw!) CONTOUR PLOTS OF WATER LEVEL ELEVATIONS
(roorwu»nyung,n»u WTHEDEEpZONEf1if8 AND 1990
CJCCJDENTM. CHEMICAL SITE
a
ex
0)
i
O
o
s
-------
SHALLOW ZONE
DBCP Trend Surface
DBCP Concentration Isoptettw
WTER*ECMATE ZONE
DBCP Trend Surf«»
DBCP Concentration Isopteths
DEEP ZONE
Trend Surface
mm «i..fcrr ->U^ / #
*" ?^f,-~*
DBCP Concentration Isoptelhs
Sourc*: Wwton, Inc., 1990
-4
Figure 11
TREND SURFACE MID CONCENTRATION ISOPLETTHS
(Poor QualHv Orkjlnal) OF DBCP CONCENTRATIONS IN THE SHALLOW,
INTERMEDIATE, AND DEEP ZONES FEBRUARY, 1990 (ppb)
OCCIDENTAL CHEMICAL SITE
o
o
o
a
o
i
O
I
-------
UJ
UJ
o
-c
•HALLOW ZOMt
OCTOBER till
FEIHUAftV 1»iS
ftMUAMV 1MO
Sourc*: Weston, Inc., 1990
Figure 12
w««r n,,,utv Orialnah TREND SURFACE OF DBCP CONCENTnATIONS IN THE
{Poor Quality ongin*i) ^..UTFR OP TUP SITP nrrnnpn ioa-> TO PPRRHARV 1
CENTER OF THE SITE, OCTOBER 1982 TO FEBRUARY 1990
OCCIDENTAL CHEMICAL SITE
o
o
o
a
Q
O
»
8
-------
Occidental Chemical
These plots also suggest that the DBCP plume has
not migrated substantially since 1982, despite the
fact that DBCP is known to be highly mobile in
ground water.
Figures 13, 14, and 15 show the trend in DBCP
concentrations from October 1982 to February
1990 in monitoring Wells PW-6-197, PW-8-150,
and PW-22-71, respectively. Well PW-6-197 is
the deep zone monitoring well at PW-6, located
along the western boundary of the plant. Figure
13 shows, a steep initial drop in DBCP
concentrations followed by a steady decrease
through the end of 1986. Concentrations in PW-6-
197 appear to have stabilized at approximately 10-
15 ppb since the end of 1986. This pattern of
steep initial decreases followed by more gradual
reductions was observed in many of the
monitoring wells. The concentrations of DBCP in
several cells decreased to below detection limits by
the end of 1986.
Other wells have shown a more gradual decrease
and greater variability in DBCP concentrations
since 1982 than PW-6-197. An example of this
trend is the data from PW-8-150 shown in Figure
14. PW-8-150 is the intermediate zone monitoring
well at PW-8, located on the northwest corner of
the former Western Storage area. The DBCP
concentration in PW-8-150 decreased from
approximately 150 ppb in early 1983 to
approximately 30 ppb at the end of 1989. The
reason for the sharp increases and decreases seen
in the concentration trend is not known. However,
the increases and decreases appear to be seasonal.
Overall, the plots display general decreasing
groundwater contamination levels.
The concentration trend in PW-22-71 has been
extremely variable since late 1982, as shown in
Figure 15. PW-22-71 is the high-concentration
monitoring well that was converted to use as an
intermittent extraction well in December 1989.
The reason for the high variability and long term
stability in DBCP concentrations is not clear,
however, the proximity of this well to the Western
Storage area suggests that the stability and
variability may be the result of a residual source
of DBCP in the soil.
Figure 16 is a time series plot of the monthly
average concentration of DBCP in the influent to
the treatment system from mid-1982 to early 1990.
This plot shows that the composite concentration
of DBCP in ground water extracted by the remedi-
ation system has decreased substantially over the
7-1/2 years of system operation—from approxi-
mately 4000 ppb in October 1982 to approximately
20 in mid-1989. The influent concentration
appears to have stabilized since mid-1989.
Site operations have calculated that the rate of
decrease hi DBCP contamination is slowing
(Weston, Inc., 1990). The recendy expanded
extraction system is intended to accelerate the rate
at which contaminants are removed from the
ground water. It is uncertain if the additional
extraction wells will affect DBCP concentrations.
SUMMARY OF REMEDIATION
The soils and ground water underlying the
Occidental Chemical site have been contaminated
with a variety of pesticides as a result of past
disposal practices. The most critical of these
pesticides is DBCP because of its high mobility
and known sterilizing effect on humans. AM three
zones of the 250-foot-thick upper aquifer have
been contaminated with pesticides. Ground-water
contamination is greatest in the shallow zone
along, and to the west of, the western boundary of
the plant; however, low-level contamination has
also been detected offsite to the north.
Contamination in the intermediate and deep zones
of the upper aquifer extends farther offsite to the
west than in the shallow zone. Several source
removal actions have occurred since cleanup began
in 1981.
The site is being remediated using a system of five
extraction wells located north and west of the
plant, and along its western boundary and one
intermittent extraction well in a high concentration
area in the western part of the plant. The
extraction system, which pumps from all of the
three upper aquifer zones, began operating at
approximately 500 gpm on June 22, 1982, and has
operated continuously since then. The extracted
ground water is treated and reinjected into the
brackish lower aquifer that underlies the Corcoran
clay confining unit at a depth of 300 to 500 feet.
The extraction system has created a drawdown
trough that trends northeast-southwest along the
northern boundary of the plant. This trough
controls offsite ground-water flow to the north and
west and appears to capture most or all of the
existing contaminant plume, despite occasional
periods of ineffective control caused by high-
volume water-supply pumping in the area.
334
-------
u>
-c
A
a
a.
8
o
T—i—i—i—i—r
10/82 6/83 2/84 10/34 6/85 2/86 10/86 6/87
2/83 10/83 6/84 2/85 10/85 6/86 2/87
2/88 10/88 6/89 2/90
10/87 6/88 2/89 10/89
Sourer W«s»oo, Inc., 1990
Hgura 13
CONCENTRATION OF DBCP IN PW-fr-197,
OCTOBER 1982 TO FEBRUARY 1990
OCCIDENTAL CHEMICAL SITE
O
o
o
£
o
i
o
9
3
s
-------
a
•S
I
I
o
,—i—,
10/82 6/83 2/84 10/34 6/85 2/86 10/8S 6/87 2/88 IO/8B 6/89 2/90
2/85 10/83 6/84 2/85 10/8S 6/86 2/87 10/87 6/88 2/89 10/89
Sourc*: Wrton. Inc., 1990
O
o
2.
a
-------
50
o.
o.
o
1
*<
§
3
i1" • »—i—r—i—i—i—i—i—i—i—i—r
10/82 6/83 2/84 10/34 6/85 2/86 10/8i 6/87 2/88 10/88 6/8§ 2/90
2/83 10/83 6/84 2/85 10/85 6/86 2/87 10/87 6/88 2/89 10/89
Sampling Periods
Source W«ston. Ina, 1990
Figure 15
CONCENTRATION OF DBCP IN PW-22-71
OCTOBER 1982 TO FEBRUARY 1990
OCCIDENTAL CHEMICAL SITE
a
a
o
i
O
i
I
-------
CO
«JU
tun
Source: Wwton, Inc.. 1990
Figure 16
MONTHLY AVERAGE CONCENTRATION OF DBCP (ppb)
IN THE TREATMENT PLANT INFLUENT,
1982 TO MARCH 1990
OCCIDENTAL CHEMICAL SITE
§
O
f
i
O
s
-------
The concentrations of pesticides have decreased
substantially in all three zones of the upper aquifer
since extraction began in 1982. ^Contaminant
concentrations irt the upper aquifer are commonly
less than 10 percent of their original levels,
although high concentrations persist at the shallow
well at PW-22, Significant reductions in nearby
wells suggest that this area of high onsite
contamination is not laterally extensive. DBCP
concentrations -are still up to three orders of
magnitude higher than the drinking water standard
of 0.2 ppb DBCP in some areas. The
concentration of DBCP in the influent to the
treatment system has decreased to less than 1
percent of its original concentration in the 7 1/2
years of operation.
SUMMARY OF NAPL-RELATED
ISSUES
Occidental Chemical
9. Some of these changes were order of
magnitude increases and decreases in concentra-
tions. This variability was recognized early in the
site monitoring program and was part of the
justification for using trend surface analysis to
smooth the data and make interpretation easier.
The reason for the variability is not known. It is
possible that the variability could be an indication
of NAPL contamination, particularly at PW-22
where concentrations have historically been the
highest observed at the site. A more complete
analysis of the historical data would be necessary
to add strength to this hypothesis.
Contamination by non-aqueous phase liquids
(NAPLs) is not suspected at the Occidental
Chemical site. Some signs of contamination by
NAPLs would include: (1) contaminant
concentrations greater than 1 to 10 percent of
aqueous solubility, (2) persistence of the
contamination despite efficient extraction,
(3) significant increases in contaminant
concentrations following periods without pumping,
(4) the existence of cross-gradient or upgradient
contamination caused by slopes in the surface of
impermeable layers, (5) high variability in
contaminant concentrations, and (6) direct
observation of NAPLs. None of these
characteristics are present at the Occidental
Chemical site.
Indications of possible NAPL contamination can
be attributed to other factors. The stable trend, for
example, in the influent concentration of DBCP
since mid-1989, could be due to operational
factors. Moreover, even if the existence of buried
containers of pure product in the trenches can be
taken as an indication that a NAPL source was
released near the water table surface, this does not
necessarily suggest that these contaminants
remained in NAPL form after migrating some
distance from their source.
Considerable variability in pesticide concentrations
was observed between sampling events at a few
individual locations in the monitoring network,
notably in the shallow well at PW-22. Other
examples of variable concentrations, especially
along the western border of the site, can be seen in
the 1989/1990 data presented in Figures 7, 8, and
339
-------
BIBLIOGRAPHY/REFERENCES
Camp, Dresser & McKee (COM). May 3, 1983.
1982 Annual Report, Occidental Chemical
Company, Lathrop, California, Section IV:
Recalibration of the Ground-water Flow Model in
the Vicinity of the Occidental Chemical Facility,
Lathrop, California,
Canonic Environmental Services Corp. December
1980. Groundwater and Soil Analysis Program
Near Lathrop, California, Phase I Study.
Canonic Environmental Services Corp. July 1981.
Soil Mitigation Measures, Western Storage Area,
Occidental Chemical Company, Lathrop,
California, Final Report.
Luhdorff and Scalmanini Consulting Engineers.
April 1983. 2982 Annual Report, Occidental
Chemical Company, Lathrop, California, Sections
I, II, and III.
U.S. EPA, NEIC. June 1991c. Comments by
Tom Dahi on the draft case study of the
Occidental Chemical site.
U.S. Environmental Protection Agency (U.S.
EPA), Tom DahL November 1985. Occidental
Chemical Company at Lathrop, California, A
Groundwater/Soil Contamination Problem and a
Solution, paper presented at the First International
TNO Conference on Contaminated Soil, Utrecht,
the Netherlands.
U.S. EPA, Office of Drinking Water. March 31,
1987. Health Advisories for 16 Pesticides,
PB 87-200176.
U.S. EPA, Tom Dahl. 199la. Occidental
Chemical Company at Lathrop, California, A
Groundwater/Soil Contamination Problem and a
Long-term Solution. Paper presented at the
Institute Per L'Ambiente conference on The
Reclamation of Contaminated Soils, Milan, Italy.
U.S. EPA, National Enforcement Investigation
Center (NEIC). May 14, 199 Ib. Personal
communication with Tom Dahl, Consent Decree
Coordinator for the Occidental Chemical-Lathrop
site.
Weston, Inc. 1984. Occidental Chemical
Corporation, 1983 Annual Report, Groundwater
Remedial Program, Lathrop, California.
Occidental Chemical
Weston, Inc. 1985a. Occidental Chemical
Corporation, 1984 Annual Report, Groundwater
Remedial Program, Lathrop, California.
Weston, Inc. 1985b. Trend Surface Analysis of
DBCP Concentrations in Groundwater at the
Facility in Lathrop, California.
Weston, Inc. 1986. Occidental Chemical
Corporation, 1985 Annual Report, Groundwater
Remedial Program, Lathrop, California.
Weston, Inc. 1987a. Occidental Chemical
Corporation, 1986 Annual Report, Groundwater
Remedial Program, Lathrop, California.
Weston, Inc. August 21,1987b. Site Investigation
Report, J. R. Simplot Company Facility, Lathrop,
California.
Weston, Inc. 1988a. Occidental Chemical
Corporation, 1987 Annual Report, Groundwater
Remedial Program, Lathrop, California.
Weston, Inc. June 2, 1988b, Proposed Remedial
Excavation Plan, J, R. Simplot Company Facility,
Lathrop, California.
Weston, Inc. January 9, 1989a. Remedial
Excavation Project Report, J. R. Simplot Company
Facility, Lathrop, California.
Weston, Inc. 1989b. Occidental Chemical
Corporation, 1988 Annual Report, Groundwater
Remedial Program, Lathrop, California.
Weston, Inc. 1990. Occidental Chemical
Corporation, 1989 Annual Report, Groundwater
Remedial Program, Lathrop, California.
340
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CASE STUDY 22
Syivester/Gilson Road
Nashua, New Hampshire
Abstract
Ground water at this 20-acre site is contaminated primarily with volatile organic compounds
in a fractured bedrock aquifer and in the unconsolidated overburden. The site has been
capped and enclosed within a slurry wall. Ground water within the slurry wall is extracted,
treated, and reinjected. A portion of the treated water is injected outside the slurry wall to
maintain inward gradients. Concentrations of the more soluble compounds have decreased
substantially over the nine years of remediation. However, toluene concentrations have not
been reduced, leading to the suspicion that toluene may be present in nonaqueous phase.
Background Data
Date of Problem Identification
Extraction Started
Types of Contaminants
Primary Aquifer Materials
Maximum Number of Extraction Wells
Maximum Total Extraction Rate
Estimated Plume Area
Estimated Plume Thickness
Maximum Reported Concentrations
1970
December 1981
Arsenic, metals, semivolatile and volatile
organic compounds
Glacial sand, gravel, and till over fractured
schist
8
300 gpm
16 acres
110 feet
Tetrahydrofuran (THF): 1,000,000 ppb
Methylene Chloride: 122,500 ppb
Methyl Ethyl Ketone: 80,000 ppb
Toluene: 140,000 ppb
Chloroform: 81,000 ppb
341
I3BS
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CASE STUDY
SYLVESTER/GILSON ROAD SITE
BACKGROUND OF THE PROBLEM
This case study summarizes the remediation of
ground-water contamination at the Sylvester/Gilson
Road site, located in the City of Nashua, New
Hampshire. A location map is presented in
Figure 1 and a site plan is presented in Figure 2.
SITE HISTORY
Approximately six acres of the site was used as a
sand borrow pit for an undetermined number of
years. The operator of the facility began using the
pit for waste disposal in the late 1960s. Wastes in
the pit include household refuse, demolition
material, chemical sludges and hazardous liquid
chemicals. The refuse and demolition material
were usually buried and the sludges and liquids
were either mixed with trash or allowed to
percolate into the ground adjacent to the old sand
pit. Drums containing hazardous liquids were
buried or placed on the ground surface.
Dumping at the site was discovered by the State of
New Hampshire in late 1970 and a court
injunction was issued in 1976 ordering the removal
of all materials from the site. The operator did not
comply with the injunction and illegal dumping of
hazardous wastes continued. In 1978, state
officials observed drums stored at the site. A
court order was issued in October 1979 prohibiting
all further disposal of hazardous wastes at the site.
Documents show that over 800,000 gallons of
hazardous wastes were disposed at the site during
ten months of 1979. In June 1980 1,314 drums
containing primarily toluene, xylene, and benzene
were removed from the site.
The initial site investigation, begun in April 1980,
revealed high concentrations of heavy metals and
volatile and semivolatile organics in ground water.
The contaminant plume moved from the site
northward toward Lyle Reed Brook (Figure 2).
Volatile hazardous compounds that reached the
creek were volatilized into the atmosphere
resulting in ambient air concentrations above
acceptable public health limits. The initial
investigation indicated that if the plume migration
was not mitigated, water quality criteria for
arsenic, methylene chloride, chloroform, 1,1-
dichloroethane (1,1-DCA), trichloroethylene
(TOE), and benzene could potentially be exceeded
in the Lyle Reed Brook and the Nashua River.
In December 1981, the EPA initiated emergency
containment action at the site and a ground-water
recirculation system was installed. The purpose of
this system was only to control the offsite
migration of contamination; no ground-water
treatment was included at that time. Four
extraction wells were installed to remove
contaminated ground water from an area
downgradient of the disposal area and discharge it
to recharge trenches upgradient of the disposal
area (Figure 2).
A remediation feasibility study was completed in
May 1982, and a record of decision (ROD) was
issued by the EPA in 1982. The ROD called for a
slurry wall to be installed around the 19.2-acre site
and a synthetic cap to be placed over the area.
This containment 'system was installed by
December 1982. Pilot plant studies for treatment
of extracted ground water were conducted in early
1983. A supplemental ROD concerning ground-
water extraction and treatment was issued in
September 1983. The 'existing ground-water
pumping/recharge system began operation in
September 1984 with no treatment. The ground-
water treatment plant for removal of metals and
volatile organic compounds (VOCs) began
operation in April 1986.
GEOLOGY
The site is underlain by fractured bedrock mantled
with 20 to 100 feet of unconsolidated sediments.
These sediments consist of a thin low-permeability
glacial till covered by a high-permeability sand
and gravel outwash deposit (Figure 3). The glacial
till ranges in thickness from 0 to over 20 feet and
appears to be absent in the vicinity of Wells LIM-
40, M-21, FIM-5, and GZ-5 (Figure 2).
342
-------
SyIvester/Gilson Road
0 1000 2000
SatoinFMt
Sourc»: USGS, P«pp«mll Qusdnngto. 1979
Figui»1
STTE LOCATION MAP
NASHUA, NEW HAMPSHIRE
343
-------
Sylvester/Gilson Road
t
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pi
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ills Hi
344
-------
Sylvester/Gilson Road
The bedrock unit reportedly consists of a biotite
schist of the Merrimack Group and igneous rocks.
It is differentially weathered and fractured and is
characterized by northeast and north-trending
ridges and valleys. As Figure 3 shows, the top of
the bedrock surface is irregular, with variation in
relief of more than 70 feet. Unconsolidated
deposits are in the valleys in the bedrock surface
and are thickest where bedrock elevations are the
lowest (Figures 3 and 4).
HYDROGEOLOGY
The site is located within the Lyle Reed Brook
watershed. Lyle Reed Brook flows from the east
to within 50 to 1,000 feet of the site around the
southern, western, and northwestern boundaries,
eventually discharging into the Nashua River.
Two major aquifer systems within this watershed
underlie the site. One is the sand and gravel
stratified drift aquifer, and the other is the
fractured bedrock aquifer. A discontinuous silt,
sand, and gravel till layer of varying thickness and
permeability separates the two aquifers. In
general, the till has a lower hydraulic conductivity
than the overlying stratified drift and, in some
places, may act as a confining layer. Where the
till is absent, the stratified drift and fractured
bedrock aquifers are in direct hydrogeologic
communication.
Ground water in the stratified drift occurs under
water table conditions, while ground water within
the fractured bedrock probably occurs under
semiconfined conditions (Weston, 1989). Aquifer
tests in the stratified drift yielded a range of
hydraulic conductivity between 20 and 200 ft/day
and a range of transmissivities between 700 and
6,600 ft2/day (Weston, 1989). Transmissivity for
the fractured bedrock is reported as 6,500 ft /day
(Weston, 1989). However, Weston (1989) reports
that pumping rates in the bedrock wells range from
2 to 100 gpm. This suggests that there is a
significant range of hydraulic conductivity in the
bedrock (see Table I).
On the basis of this data, Weston (1982)
concluded that the overburden and bedrock
aquifers are hydrogeologically similar and respond
in a similar manner to regional hydraulic
influences. As a result, Weston (1982) expected
that without active gradient control there would be
considerable underflow from the slurry wall
containment area.
Ground-water elevations measured hi the stratified
drift in January 1982,1 month after the start-up of
the ground-water recirculation system, ranged from
167 to 174 feet above MSL and showed ground
water flowing across the site in a northwesterly
direction toward Lyle Brook (Figure 5). Weston
(1982) calculated ground-water flow velocities to
be 0.8 to 1.6 feet/day and reported that Goldberg,
Zoino, and Associates estimated the hydraulic
gradient to be 0.003 to 0.004 feet/foot The water
level contours shown in Figure 5 show no obvious
hydraulic effect produced by die interim
recirculation system that began operating in
December 1981.
WASTE CHARACTERISTICS AND
POTENTIAL SOURCES
Ground water is contaminated with numerous
organic compounds and selenium. The maximum
ground-water concentrations of these compounds
in 1981 and the cleanup goals are presented in
Table 2. Note that only validated date are
presented here. Some samples that were not
validated showed higher concentrations than the
maximum values listed. The cleanup goals, known
as alternate concentration levels (ACLs), were
based on extensive research and are levels deemed
necessary to adequately protect human health and
the environment (U.S. EPA, 1990).
Table 2 shows that there has been a significant
decrease in the concentrations of contaminants on
this site. However, two contaminants (toluene and
1,1 dichlorethane) show significant increases in
concentration in some samples.
Figure 6 presents a contour map of total VOC
concentration for December 1980. The high-
concentration area of the plume extended in an
eEiptical shape from the area of historical liquid
waste disposal near the current location of trench 3
to monitoring point FIM-41. Tetranydrofuran
(THF) was found in concentrations exceeding
1,000,000 ppb. Toluene, melhylene chloride, and
methyl isobutyl ketone occurred at concentrations
one to two orders of magnitude lower. In the
vertical column, the contaminants were distributed
relatively uniformly in the overburden with slight
decreases in concentration with greater depth.
VOC concentrations were elevated in bedrock near
monitoring point M-l, suggesting hydraulic
connection between the overburden and the
bedrock.
345
!3C(p
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Sylvester/Gllson Road
Table 1
ESTIMATES OF AQUIFER CHARACTERISTICS
SYLVESTER/GILSON ROAD SITE
Parameter/Flow Zone
Hydraulic Conductivity
(ft/day)
Overburden/Stratified
Drift
Transmissivity (ft2/day)
Overburden/Stratified
Drift
Bedrock
Saturated -Thickness (ft)
Overburden/Stratified
Drift
Horizontal Hydraulic
Gradient (ft)
Overburden/Stratified
Drift
Bedrock
Porosity (%)
Overburden/Stratified
Drift
Effective Porosity/Specific
Yield (%)
Overburden/Stratified
Drift
Vertical Hydraulic
Conductivity (ft/day)
Till Layer
Regional Groundwater
Recharge (in/yr)
Basinwide
Estimates
30-100
2,000-
8,000
10-80
0.006
30-32
14-32
—
24
Site-
Specific
Measure
ments
20-200
700-6,600
6,500
30-90
—
—
—
5
—
Earlier
Modeling
Studies
'50
3,500
6,500
50
0.004
0.004
—
25
5
42
Current
Modeling
Studies
30
2,500
1,190
30-80
0.004-0.006
0.004-0.006
—
25
5
18
Source: Weston, 1989
346
I3D7
-------
Sylvester/GHson Road
Table 2
GROUNDWATER QUALITY IN 1981 AND 1988
SYLVESTER/GILSON ROAD SITE
ACL Compounds
Vinyl Chloride
Benzene
Chloroform
1,1,2 Trichloroethane
Tetrachloroethene
Trichloroethylene
Methyl Ethyl Ketone
Chlorobenzene
Methylene Chloride
Toluene
1,1 Dichloroethane
Trans-1,2 Dichloroethylene
1,1,1 Trichloroethane
Methyl Methacrylate
Selenium
Phenoli
Concentration
in Gronndwater
(1981)
950
3400
81000
17
570
15000
80000
1100
122500
29000
15
18000
2000
3500
NA
NA
Alternate
Concentration
Level
(ACL)
95
340
1505
1.7
57
1500
8000
110
12250
2900
IS
1800
200
350
2.6
400
Concentration
In Gronndwater
(1988)
300
1100
5
5U
10
3
7400 J
800
39
31000
2200
9200
38
ND
5U
2274
Number of
Samples That
Exceeded
ACLs
1
2
0
0
0
0
0
7
0
3
18
1
0
ND
0
3
Number of
Samples
65
65
65
65
65
65
65
65
65
65
65
65
65
0
10
25
Source: Weston, 1989
Note: All concentrations in ppb.
ND denotes No Data.
NA denotes Not Available.
Sampling points with multiple occurrences include FIM 29-2 and FIM 44-3.
No data is available for Methyl metacrylate.
Only validated data are presented.
J= estimated value
U » below quantification limit
347
-------
Sylvester/GHson Road
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348
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Sylvester/GIIson Road
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7
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Sylvester/Gilson Road
REMEDIATION
Selection and Design of the
Remedy
As a result of the initial ROD, a synthetic cap and
containment wall were constructed to minimize
infiltration and limit contaminant migration. The
containment wall, shown in Figure 7, corresponds
approximately to the location of the perimeter
fence shown in the other site maps. It was
constructed of bentonite slurry with a design
hydraulic conductivity of 10"7 cm/sec. The slurry
wall is approximately 4 feet wide, 4,000 feet in
perimeter length, and as deep as 100 feet in some
locations (Weston, 1989). Approximately 20 acres
are enclosed by the wall and covered by the cap.
The existing remedial system also includes eight
ground-water extraction wells (A through H) and
seven recharge trenches (l through 7). The
purpose of the system is to isolate contaminated
ground water, recover and treat ground water in
the isolated system, and induce uniform flushing
of the isolated upper saturated zone. Ground
water is extracted, treated, then recharged through
trenches. The maximum pumping rate for each of
the eight wells is 40 to SO gallons per minute
(gpm) (Weston, 1989). The ground-water
treatment system design flow rate is 300 gpm
(U.S. EPA, 1990).
The extraction well and recharge trench locations
are shown in Figure 2. Three of the trenches (1,
2, 3) are located at the upgradient end of the site,
three trenches (4, 5, 6) are located in the middle of
the site, and one trench (7) is located just outside
the containment wall on the northeast side of the
site. Recharge to trench 7 is intended to maintain
greater pumping rates than recharge rates in the
containment area to induce inward rather than
outward flow through the fractured bedrock under
the slurry wall.
Table 3 lists the 1988 average extraction rates for
wells and the average recharge rates for the
trenches. The average total extraction rate was
260 gpm. Approximately 50 gpm of the treated
ground water is recharged to trench 7, exterior to
the wall. The majority of the treated ground
water, averaging 105 gpm, is recharged to
trench 4. The recharge rates to trenches 1, 2, and
3 are variable. Recharge to trenches 5 and 6 has
been minimal. The preferential recharge to trench
4 results in mounding of the ground-water surface
in the area of trench 4 (see Figure 8).
The ground-water treatment system includes
chemical precipitation for removal of inorganic
constituents, high temperature air stripping for
volatile organics removal, and extended aeration
activated sludge treatment for the portion of the
waste stream that is to be discharged offsite (in
trench 7). Sludge produced by the treatment plant
is deposited in the disposal areas shown near the
center of the site on the site maps. These disposal
areas are constructed above the cap that covers the
site inside the slurry wall and are provided with a
leachate collection system. The treatment system
began operating in 1986. Prior to that time, the
ground-water extraction system was operated
solely to recirculate ground water within the
confines of the slurry wall, and there was no
offsite discharge.
EVALUATION OF PERFORMANCE
Hydraulic Control
A ground-water elevation contour map for the
stratified drift aquifer in July 1988 is presented in
Figure 8. This map shows that water elevations
across the site were slightly higher in 1988 than in
1982 (Figure 5), and the major ground-water flow
at the site continued to be to the northwest and
west. Mounding is evident around trenches 2 and
4; however, cones of depression are not apparent
around the extraction wells. In addition, the
gradient across the slurry wall was not consistently
inward (Figure 8). These observations suggest that
pumping rates are insufficient to effectively control
ground-water flow, especially at the northwest and
southwest ends of the site.
There have been some problems with clogging of
the recharge trenches, which may have limited the
rates of ground-water recirculation. Before 1986,
recharge of untreated water to the onsite trenches
led to fouling by iron precipitation. Now that
metals are removed at the treatment plant before
the ground water is recharged, iron precipitation is
no longer a problem. However, the fouled
trenches still need to be rehabilitated. Biological
encrustation has been a problem in the offsite re-
charge trench, but periodic treatment with
hydrogen peroxide seems to be effective in
keeping this trench in operation.
352
I1B 5 W11
-------
Sylvester/GHson Road
Source: Western, 1989
Rgui»7
(Poor Quality Original) SLURRY WALL
* SYLVESTSW3JISON ROAD SITE
353
-------
Sylvester/Gilson Road
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354
-------
Sylvester/Gilson Road
Table 3
1988 EXTRACTION AND RECHARGE RATES
SYLVESTER/GILSON ROAD SITE
Wells (A-H)
and Trenches (1-7)
A
B
C
D
E
F
G
H
1
2
3
- 4
5
6
7
Extraction/Recharge (gpm)
Plant Records
30-38
0-38
0
38 - 47
38-50
0-45
0-45
35-50
5-20
5-35
5-65
5-80+
0-15
0-10
50
Estimated Average
33
30
0
42
45
25
40
45
10
35
60
105
0
0
50
Sourcfe: Weston, 1989
355
-------
Sylvester/Gilson Road
A new operating mode was proposed in 1989 to
increase ground-water capture. Pumping and
recharge rates would be preferentially redistributed
toward areas of high residual contamination
without significantly reducing the overall capture
zone. The proposed new extraction and recharge
rates are shown in Table 4. The intent is to
increase pumping in areas of high contamination
(wells A, H, G, and F), increase recharge in areas
of high contamination (trenches 2 and 3), and
decrease recharge to trench 4. The rates were
selected on the basis of contaminant concentrations
and the capabilities of individual wells and
trenches (Weston, 1989). The new total extraction
rate is 300 gpm.
Six new extraction wells in areas of greatest
residual contamination were planned for
installation in the fall of 1990 (U.S. EPA, 1990).
Additional flow modeling was conducted to
optimize the locations and pumping rates of the
wells. Rebuilding recharge trenches to maintain
design recharge rates was planned for the summer
of 1990.
Multilevel monitoring points show downward
ground-water gradients across much of the site,
indicating that the contaminant plume may be
escaping downward from the stratified drift into
the fractured bedrock zone in areas were the till is
absent. In view of this, consideration is being
given to increasing the recharge rate to trench 7 to
100 gpm (U.S. EPA, February 13, 1991).
Reductions in Mass and
Concentration of
Contaminants
Treatment Plant Influent Data. Figure 9
presents plots of VOC concentrations in treatment
plant influent for selected compounds (toluene,
THF, chloroform, chlorobenzene) over time. The
plots show decreasing concentrations for THF,
methyl etJbyl ketone (MEK), and chloroform with
stable toluene concentrations. Toluene concentra-
tions remained relatively constant although high
removal efficiencies were observed in the
treatment plant (Weston, 1989).
Ground-water Quality Data. Data collected in
May 1988 showed decreases in pollutant
concentrations since treatment plant startup in
1986 ranging from 58 to 100 percent for all ACL
compounds except toluene and 1,1-dichloroethane
(1,1-DCA). The maximum concentration of ACL
compounds detected in 1988 are given in Table 2.
For eight of the 16 ACL compounds, all of the
samples collected had concentrations less than the
ACLs. Ground-water quality data were collected
after May 1988, but according to Region 1 EPA
staff, the data are not available at this time as a
result of pending litigation.
Because there are many contaminants in the
ground water, three indicator compounds were
selected to monitor water quality conditions:
toluene, THF, and 1,1-DCA. Toluene and THF
have historically been dominant contaminants.
Toluene and THF are both less dense than water
and 1,1-DCA is more dense than water.
Contour maps of total VOC concentrations at
various depths across the site in May 1988 is
shown in Figures 10A through IOC. Cross-
sections of total VOC concentrations are shown in
Figure 11. VOC concentrations exceeding 10,000
ppb occur along the west side in the shallow
overburden and in the bedrock. VOC
concentrations greater than 100,000 ppb are found
at the southern end of the site in the overburden
aquifer.
A comparison of total VOC concentrations in 1988
with those of 1980 (Figure 6) shows an order of
magnitude reduction. It is also evident that the
plume has been split by recharge trenches 4 and 5
in the middle of. the site. The bedrock
concentrations are higher under trenches 4 and 5
than around extraction wells C, D, and E. The
opposite trend is observed in the overburden.
Contour maps of toluene concentrations at various
depths in May 1988 are presented in Figures 12A
through 12C. Cross-sections of toluene
concentrations are shown in Figure 13. Toluene
concentrations in the overburden range from over
100,000 ppb at the southeastern end of the site to
10 ppb at the northwestern end. Toluene con-
centrations in the bedrock exceed 1,000 ppb along
the southeastern end and west side of the site.
The sustained elevated toluene concentrations in
both treatment plant influent and ground-water
monitoring wells may indicate the presence of
toluene floating on the ground water and/or at
residual saturation in the vadose zone as a
nonaqueous phase liquid (NAPL). Other VOCs
may be in solution with the nonaqueous phase
356
13C5
-------
Sylvester/Gllson Road
Table 4
PROPOSED NEW EXTRACTION AND RECHARGE RATES
SYLVESTER/GILSON ROAD SITE
Well/Trench
A
B
C
/
D
E
F
G
H
1
2
3
4
5
6
7
Extraction/Recharge (gpm)
40
• 40
47
0
23
50
50
50
60
75
75
55.
10
10
50
Source: Weston, 1989
357
-------
Ul
oo
o
CONCENTRATION (ppb)
10
Aug 86 Nov 86 Feb 87 May 87 Aug 87 Oct 87 Feb 88 May 88 Aug
DATE
*- TOLUENE
THF
MEK -*-
SITE NASHUA, NH
DATA FROM MSE, EdJ, S STATE LAB
Source: Weston, 1989
SELECTED VOCt W TREATMENT
PLANT INFLUENT
SYLVESTERA3ILSON ROAD SITE
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toluene. Additional investigations, such as sol! gas
studies, borings and sampling, and excavation
beneath the cap, are underway to locate and
develop a remedial action for the source of
nonaqueous toluene. The investigation and design
of a toluene recovery system is scheduled to be
completed in April 1991. Free product recovery
measures will involve depressing the water table in
the source area and skimming the toluene (U.S.
EPA, February 13, 1991).
Contour maps of THF concentrations and 1,1-DCA
concentrations in May 1988 are presented in
Figures 14A, 14B, ISA, and 15B. Cross-sections
of THF concentrations are presented in Figure 16.
Areas with high THF concentrations do not
correspond to areas with high VOC concentrations
in 1988 as they did in 1980. THF is no longer the
dominant plume contaminant. Areas of high 1,1-
DCA concentration appear to correspond with
areas of high toluene concentrations. Both 1,1-
DCA and toluene have relatively low water
solubility.
THF, a relatively mobile and low-toxicity
compound, has moved into the northwestern end
of the site, where its is not within the capture zone
of the existing extraction wells. Toluene and some
other persistent VOCs have moved into lower flow
zones at the base of the overburden and in upper
bedrock, where they are less likely to be captured
by relatively shallow recovery wells operating at
the site. This may be a result of preferential
recharge to trench 4, which is causing mounding
of hydraulic heads, and may be setting up deeper
circulation flow paths that radiate outward below
the intakes of the extraction wells (Weston, 1989).
Overall contaminant concentrations were an order
of magnitude lower in August 1987 than
December 1980. During this period the plume
migrated downgradient. In May 1988, the bedrock
zone remained contaminated across the site and
offsite to the northwest, west, and southwest.
Offsite contamination is probably a result of
downward circulation and advection of
contaminants induced by the pumping/recharge
operation (Weston, 1989). Natural underflow
through the upper fractured bedrock flow zone
may have also contributed to offsite migration of
contaminants (Weston, 1989).
Sylvester/Gilson Road
SUMMARY OF REMEDIATION
The remediation of the Sylvester/Gilson Road site
is summarized as follows:
• There are two. aquifer zones beneath the
facility that are contaminated primarily
with volatile organics. Contamination in
both zones has extended offsite to the
downgradient Lyle Reed Brook.
» A bentonite slurry wall was installed
around the perimeter of the site and a
synthetic cap was placed over the entire
site.
• A ground-water extraction/recharge
system was installed including eight
extraction wells inside the slurry wall and
seven recharge trenches. The system
began operating in 1984. A 300 gpm
treatment plant began operating in 1986.
Siege then, ground water has been
extracted, treated, and then recharged
through trenches located both inside and
outside the slurry .wall.
• From May 1986 to May 1988, 40 to 100
percent reduction in concentration was
observed for all ACL compounds except
1,1-DCA and toluene. 1,1-DCA
concentrations exceeded the ACL in 18 of
65 samples collected in 1988. No
decrease was observed in toluene
concentrations suggesting that there may
be a nonaqueous source of toluene at the
southeastern (upgradient) portion of the
site. Additional site investigations are
planned to locate the toluene source.
« Water level monitoring does not show
that inward gradients are being
maintained across the slurry wall.
Contaminants appear to be escaping from
the site by flowing under the wall in the
bedrock aquifer. Also, some
redistribution of contamination has
occurred in areas that are not effectively
captured by the extraction wells.
Contaminant levels exceeding ACLs were
observed in these areas. Six additional
extraction wells were planned to more
effectively control plume migration.
367
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Sylvester/Gilson Road
SUMMARY OF NAPL-RELATED
ISSUES
Nonaqueous toluene is thought to be floating on
the water table at the southern end of the site near
monitoring well M-19. This is suspected because
toluene concentrations in the ground water in this
area have remained high in spite of more than
seven years of ground-water recirculation and two
years of treatment. The toluene concentration
measured in ground water sampled from well
M-19 in May 1988 was 140,000 ppb. This is
approximately 26 percent of the aqueous solubility
of toluene (534,800 ppb). Such a high
concentration, relative to solubility, is in itself a
very strong indication that the compound is present
as a NAPL. Furthermore, as shown in Figure 9,
the toluene concentration in the treatment plant
influent was remarkably stable throughout the
available two years of record. In spite of these
strong indications of NAPL presence, free-phase
toluene has not been observed in any of the
monitoring wells (U.S. EPA, 1991).
Another contaminant of importance at the site is
1,1-DCA. The maximum concentration measured
in May 1988 was 2,900 ppb in well FIM-29. This
is less than 1 percent of the solubility of this
compound. However, the maximum
concentrations have not been decreasing over the
period of record. Also, as shown in Figure ISA,
the areal distribution of 1,1-DCA is similar to that
of toluene. This leads to the supposition that
nonaqueous 1,1-DCA, and potentially several other
compounds, may be dissolved in the floating
NAPL layer.
Tetrahydrofuran, the contaminant with the highest
initial ground-water concentrations is nuscible in
water. It is, therefore, unlikely to be present as a
NAPL. The relatively rapid reduction in THF
concentrations and the marked change in the shape
of the THF plume between 1981 and 1988 can be
contrasted to the toluene plume's stability and
resistance to remediation efforts. Unless
specialized techniques are used to remediate the
assumed floating NAPL layer, it is unlikely that
the ground-water extraction and recirculation
system will be very effective in cleaning up the
site.
A program is presently under way at the site to
investigate the NAPL problem and design a
recovery system for it. However, because of the
sensitivity of ongoing negotiations, no detailed
information has been made available on these
efforts.
BIBLIOGRAPHY/REFERENCES
Roy F. Western, Inc. (Weston). January 1982.
Final Report, Sylvester Hazardous Waste Dump
Site Containment and Cleanup Assessment.
Roy F. Weston, Inc. (Weston). February 1989.
Remedial Program Evaluation Gilson Road Site,
Nashua, New Hampshire.
U.S. Environmental Protection Agency (U.S.
EPA). July 1982. Superfund Record of Decision,
Remedial Alternative Selection, Sylvester Site,
Nashua, New Hampshire.
U.S. EPA. September 1983. Supplemental
Record of Decision, Groundwater Treatment
Alternative Section, Sylvester Site, Nashua New
Hampshire.
U.S. EPA. July 1990. Explanation of Significant
Differences, Sylvester/Gilson Road Hazardous
Waste Site, Nashua, New Hampshire.
U.S. EPA. Region I. February 13, 1991.
Personal Communication with Chester Janowski.
373
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CASE STUDY 23
Tyson's Dump
King of Prussia, Pennsylvania
Abstract
Disposal of waste liquids into unlined lagoons during the 1960s has led to considerable
contamination of the onsite disposal area and the offsite fractured bedrock. DNAPL
contamination has been observed south of the Schuylkill River and is suspected under parts
of Barbadoes Island. DNAPLs have migrated north along bedding planes in the fractured
rock. Aqueous phase contamination, derived from the DNAPLs, extends to the north side
of the river and has discharged to the river in at least some areas, threatening downstream
users. A seven well interim extraction system, in operation since November 1988, has
generally controlled the central part of the dissolved plume south of the river. Lateral areas
have not been completely captured, but construction of a final system is almost complete.
Background Data
Date of Problem Identification
Extraction Started
Types of Contaminants
Primary Aquifer Materials
Maximum Number of Extraction Wells
Maximum Total Extraction Rate
Estimated Plume Area
Estimated Plume Thickness
Maximum Reported Concentrations
1973
November 1988
VOCs, especially 1 ,2,3-Trichloropropane
(TCP), xylene, toluene, and ethylbenzene
Thin layer of sand and clay over fractured
sandstone and siltstone
7
120 gpm
65 acres
365 feet
1,2,3-Trichloropropane 1,400,000 ppb
374
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CASE STUDY
TYSON'S DUMP SITE
BACKGROUND OF tHE PROBLEM
The Tyson's Dump site is in King of Prussia,
Pennsylvania approximately 15 miles northwest of
central Philadelphia (see Figure 1). The 4-acre
site is located at an abandoned sandstone quarry
that is bordered on the north by a Conrail railroad
shipping yard and the Schuylkill River, on the
south by the high wall of the former quarry and on
the east and west by streams (see Figure 2).
Residential and industrial areas surround the site
on the south and west. Tyson's Dump was
operated as a disposal facility for septic and
chemical wastes from 1960 to 1970. The soil and
ground water underlying the site have been heavily
contaminated with volatile organic compounds
(VOCs) as a result of past dumping into unlined
lagoons. The primary contaminants of concern at
the site are 1,2,3-trichloropropane, xylene, toluene,
and ethylbenzene. Dense non-aqueous phase
liquid (DNAPL) contamination is known to exist
at the site. Tyson's Dump is a Superfund site that
is ranked number 25 on the EPA's National
Priorities List. The remediation of the site is
administered by the EPA and the Pennsylvania
Department of Environmental Resources
(PADER).
SITE HISTORY
Tyson's Dump was operated as a disposal site by
companies owned by Franklin P. Tyson and Fast
Pollution Treatment Inc., between 1960 and 1970.
During this time, various septic and chemical
wastes were brought onsite in tanker trucks and
disposed of in unlined lagoons. As each lagoon
filled up with waste, it was covered, and a new
lagoon was begun. The Ciba-Geigy Corporation,
Smith-Kline Beckman, Wyeth Laboratories, and
the Essex Group all used the dump to dispose of
wastes during this period; all are considered to be
potentially responsible parties (PRPs). In 1969,
General Devices, Inc., acquired the property from
Franklin Tyson.
In 1973, the Pennsylvania Department of
Environmental Resources (PADER) ordered the
site owners to close the Tyson's Dump site. By
this time, most of the 4-acre site contained
lagoons, and contamination was spread throughout
the site as a result of spills and overflows during
operations. The closure order directed that the
lagoons be drained, excavated, backfilled with
clean soil, and revegetated, and the contents of the
lagoons shipped offsite. In response to PADERs
closure order, General Devices, Inc., reportedly
emptied the lagoons of standing water, then
backfilled and vegetated the lagoons (ERM,
1991b).
The investigation of the Tyson's Dump site has
historically concentrated on two separate
administrative components~the "onsite" area, in or
near the area used for disposal, and the "offsite"
area, north of the disposal areas (see Figure 2).
The onsite area was investigated primarily between
January 1983 and August 1985, whereas detailed
investigation of offsite areas began in early 1986
and has continued through 1991.
The investigation of contamination at the Tyson's
Dump site began in January 1983, when the EPA
received a complaint, about conditions at the site
from an anonymous citizen. In response to this
complaint, the EPA and its contractors conducted
an initial survey of the site and sampled soil, air,
and ground water in and near the former disposal
area. This initial field investigation, which was
conducted between January and June 1983,
showed that the onsite soil and ground water were
contaminated with high levels of volatile organic
compounds (VOCs).
Based on early findings during the initial survey in
1983, the EPA determined that immediate action
was required to limit public exposure to
uncontrolled chemical odors and liquid wastes at
the site. In March 1983, the EPA began
addressing the immediate threat posed by onsite
contamination, by instituting several emergency
remedial measures. These included: (1)
construction of a soil. cap over the suspected
lagoon areas and regrading of the site to control
drainage, (2) construction of a leachate collection
system and an air stripper/activated carbon
375
-------
Tyson's Dump
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{Poor Quality OriglnaJ)
Figure 1
SITE LOCATION
TYSON'S DUMP SfTE
KING OF PRUSSIA, PENNSn
376
-------
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It
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Source: ERM. 1987
-— Fence
' Quarry Highwal
^ 1$65 Lagoon Location
Jlf _•; ' 1973 Lagoon Location
il".j Boundaries of Offste Opefabie Units
Figure 2
SITEMAP
TYSON'S DUMP SITE
(A
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-------
Tyson's Dump
leachate treatment system, and (3) construction of
a security fence to limit unauthorized access to the
site. Additional investigation of the extent of
contamination, both on and offsite, was also
specified. The onsite area was defined as the 4-
acre area within and immediately adjacent to the
security fence.
In September 1983, a plan for a full remedial
investigation and feasibility study (RJ/FS) of onsite
contamination was approved. Between December
1983 and March 1984, the EPA and its contractors
conducted an intensive field investigation of the
onsite area. This investigation was primarily
concerned with characterizing surficial and shallow
contamination contained in the unconsolidated
onsite soils. The report on the remedial
investigation of the onsite area was completed in
August 1984. ' ~"
Based on the results of the investigations
conducted in 1983 and 1984, the EPA issued an
Operable Unit record of decision (ROD) in
December 1984, for the onsite area. The ROD
recommended the following actions:
1. Excavation and offsite disposal of
contaminated soils in a RCRA-permitted
landfill.
2. Upgrading the existing air-stripping facility
to treat leachate, shallow ground water, and
surface run-on encountered during
excavation.
3. Excavation and offsite disposal of
contaminated sediments in the gully west of
the treatment plant that receives effluent from
the existing air stripper (see Figure 2).
Between January and August 1985, the EPA began
to implement these remedial measures by installing
soil borings and conducting magnetometer surveys
throughout the site to determine the depth to
bedrock, the extent of waste materials, the volume
of soil to be removed, and the presence or absence
of metallic debris.
In the fall of 1985, Ciba-Geigy agreed to conduct
additional investigations of the offsite area. Five
separate offsite operable units were identified for
study: (1) the deep (bedrock) aquifer, (2) the
hillside area, (3) the railroad area, (4) the
floodplain and wetlands area, and (5) the seep area
(see Figure 2). In March 1986, a work plan was
prepared and in May 1986, an Administrative
Consent Order governing the offsite operable unit
RJ/FS was signed by the EPA and Ciba-Geigy.
In November 1986, Ciba-Geigy began pilot-scale
feasibility tests for using soil vapor extraction
(SVE) to clean up the lagoon area, instead of the
excavation and disposal method specified in the
December 1984 ROD. Tests showed SVE would
be an effective method of reducing VOCs in
contaminated soils. This reorientation of the
onsite cleanup was necessary because SVE had not
been a viable technology at the trine of the original
1984 ROD. Moreover, the findings of the ongoing
offsite RI showed that most of the contamination
had migrated to the bedrock; hence, excavation
and disposal for source control would no longer be
effective. In March 1988, in response to a July
1987 proposal by Ciba-Geigy and the three other
PRPs, the EPA issued a revised ROD, authorizing
the use of soil vapor extraction to remediate the
onsite lagoon soils.
The results of offsite investigations begun early in
1986 were reported in December 1986, in the draft
Offsite RI and Environmental Assessment reports.
These documents covered investigations originally
detailed in the initial March 1986 work plan, and
in a July 1986 addendum. In the draft RI, it was
proposed that remedial measures be selected for
the railroad, seep, hillside, and floodplain/wetlands
operable units, and for the deep aquifer operable
unit in the area south of the river. Additional
study of the deep aquifer north of the south bank
of the river was proposed. These plans were
detailed further in the March 1987 second
addendum to the original March 1986 offsite
RI/FS workplan.
The offsite RI report, which included
investigations north of the river specified in
addendum No. 2, was submitted to the EPA in
July 1987. These investigations showed that: (1)
some of the contamination was present as dense
non-aqueous phase liquids (DNAPLs), (2) the
majority of the aqueous-phase contamination in the
deep bedrock aquifer was a result of DNAPL
dissolution (an estimated 97 percent), and (3) some
of the ground water contaminated with dissolved-
phase was discharging to the Schuylkill River. To
decrease the volume of ground-water discharge to
the Schuylkill River, the PRP's consultant, ERM,
recommended in June 1987 that a ground-water
extraction system be installed. A Partial Consent
Decree was issued on February 19, 1988 requiring
378
IHDb
-------
Tyson's Dump
the PRPs to install and operate a ground-water
extraction system. In 1988, S.S. Papadopulos &
Associates (SSP&A) was retained to design and
install the recommended system along the south
bank of the Schuylkill River.
In August 1988, on behalf of Ciba-Geigy, ERM
submitted a draft offsite operable unit FS to the
EPA proposing the selection of the no-action
alternative for all the offsite operable units except
the deep aquifer operable unit. This selection of
the no-action alternative for four of the five offsite
operable units was authorized by the EPA in a
third ROD in September 1988. This ROD also
specified that a system of extraction wells be
installed along the south bank of the Schuylkill
River, and the ground water be treated using steam
stripping and carbon adsorption.
The interim extraction system, consisting of seven
extraction wells, was brought on line on November
21, 1988. Six of the seven wells began operation
on this date. The soil vapor extraction system in
the onsite lagoon area also began operating in
November 1988 (ERM Enviroclean, 1988).
ERM continued to investigate the extent of
DNAPL and dissolved phase contamination in the
ground water from 1989 through 1991, focusing
primarily on ground water in the deep aquifer
under the Schuylkill River, Barbadoes Island, and
along the north bank of the river, as detailed in
addenda Nos. 3 (June 1989) and 4 (1991) of the
original RI/FS work plan. As part of the
addendum No. 3 investigation, the interim ground-
water recovery system was shut down during part
of February 1990, to evaluate the degree of
hydraulic interconnection between the pumping
wells and monitoring wells installed near the
Schuylkill River. A fourth site ROD (EPA, 1984,
1988a, 1988b, 1990), which required the expansion
of the extraction system south of the river and on
Barbadoes Island, as well as further study of the
hydrogeologic conditions north of the river, was
issued by the EPA on September 28, 1990.
GEOLOGY
The Tyson's Dump is located in an abandoned
sandstone quarry in the Triassic lowlands province
of Pennsylvania. The site is underlain by a
relatively thin veneer of colluvium, fill and
floodplain deposits that overlie the middle and
lower sandstone and siltstone members of the
Stockton Formation. Figure 3 is a north-south
cross section across the site from the Schuylkill
River to the high area south of the site. An east-
west cross section along the river is shown in
Figure 4. These two cross sections show several
monitoring well clusters with open intervals at up
to four levels within the bedrock.
Unconsolidated material on and in the vicinity of
Tyson's Dump consists of undisturbed colluvial
deposits at the base of the quarry high wall, fill
material placed in the former lagoon area during
initial remediation activities, construction debris
and fill material in the seep area, and floodplain
deposits from the base of the bedrock outcrop just
north of the former lagoon area to the south bank
of the Schuylkill River. The onsite colluvium, fill
and the floodplain deposits are not contiguous, as
shown in Figure 3. The depth to bedrock from
south to north across the floodplain varies from 3
to 10 feet at the base of the embankment south of
the railroad tracks to more than 20 feet on the
north side of the tracks (EPA, 1988b).
The floodplain deposits can be divided into three
subunits. The uppermost unit consists of a 1- to
2-foot-thick organic-rich silty clay. This is
underlain by 10 to 15 feet of brownish red sandy
clay with trace gravel and cobbles. This clay unit
is underlain by a basal unit of sand and gravel
with cobbles. The basal unit is 10 feet thick at the
river's edge, but pinches out to the south and is
absent at the railroad tracks.
The bedrock aquifer underlying the site consists of
three units of the Stockton Formation: an upper
red siltstone and fine sandstone unit, a middle
purple arkosic sandstone, and a lower green
arkosic sandstone. These lower two units are
interbedded with occasional thin layers of siltstone.
The red and purple units are more resistant to
chemical weathering than the green unit and tend
to be the ridge-formers in this area.
The Stockton Formation dips to the north-
northwest at approximately 12 degrees regionally.
The data collected during the offsite RI were
found to agree with this regional trend (ERM, May
1990). The area contains several lineaments, and
several east-west high-angle faults were identified
during drilling (ERM, 1990a). High-angle joints
15 to 30 degrees from vertical were observed in
almost all bedrock wells. The predominant
orientation of the in situ joints measured in the
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response to hydraulic loading and barometric
pressure changes suggests that portions of the
bedrock aquifer are confined.
on the island, was found to respond strongly to
changes in barometric pressure. The immediate
Island decreased rather than increased in response
to the recovery test (see Figure 8). Well CW4,
days. Wells south of the river, especially those
close to the pumping wells, generally recovered
quickly, while water levels in wells on Barbadoes
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In February 1990, a recovery test designed to
measure the interconnection of the areas north and
the river, and direct hydraulic connecdon between
the river and the bedrock aquifer. The relative
influence of these two factors varies depending on
location.
almost immediately to changes in river stage. The
influence of the river can be attributed to two
factors: hydraulic loading effects of the water in
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-------
Tyson's Dump
WASTE CHARACTERISTICS AND
POTENTIAL SOURCES
Organic compounds originating from the Tyson's
Dump onsite area have contaminated ground water
underlying the disposal area and as far north as the
north side of the Schuylkill River. These
contaminants are known to be present both as
DNAPLs and as dissolved constituents. Both the
unconsolidated deposits and the fractured bedrock
are contaminated. Dissolved contaminants,
particularly 1,2,3-trichloropropane, were also found
in water samples collected at downstream local
water supply intakes (typically 0.5 to 1.5 ppb) and
in river bottom sediments. Even after treatment,
1,2,3-trichloropropane persisted at the part per
trillion level in finished drinking water. 1,2,3-
trichloropropane was not detected in river samples
collected upstream from the Tyson's Dump site.
The contamination consists of both volatile and
semivolatile organic compounds. The primary
contaminants are the VOCs 1,2,3-trichloropropane,
toluene, ethylbcnzene, and xylenes, but other
volatile and semivolatile organics are also present
(ERM, 1987). The composition of DNAPLs taken
from two intermediate bedrock wells south of the
river is listed in Table 1. Both samples contained
substantial percentages of these four main
contaminants.
DNAPLs were introduced into the ground water
via infiltration through unlined lagoons located at
the Tyson's Dump and are believed to have
migrated downward by gravity flow to the bedrock
surface. At that point, the DNAPLs are believed
to have migrated directly into the bedrock and
possibly flowed along the bedrock surface. Once
in the bedrock, the DNAPLs are likely to have
migrated downward through vertical joints and
along bedding planes, coating the walls of the
bedrock openings and pooling in low areas. A
schematic representation of this flow path is
illustrated in Figure 9. DNAPLs have been
observed in samples of the bedrock ground water
collected from as deep as 135 feet in monitoring
Well 8-1 located adjacent to the south bank of the
Schuylkill River.
The distribution of 1,2,3-trichloropropane (1,2,3-
TCP) in May 1986 in ground water in the
unconsolidated sediments is illustrated in Figure
10. This figure shows that 1,2;3-TCP
concentrations were as high as 690 mg/1 (690,000
ppb) in wells in the east-central part of the onsite
area and as high as 220,000 ppb in the west-
central part of the onsite area in May 1986.
Concentrations were less than 1/1,000 of these
amounts in wells at the east and west ends of the
onsite area. In the two wells in the floodplain
deposits shown in Figure 10, 1,2,3-TCP
concentrations were 730 and 22 ppb, despite the
discharge of ground water from the shallow
bedrock aquifer to the floodplain. More recently,
Terra Vac has completed more than 200 borings in
the onsite area. These data, which were not
available for incorporation into this case study,
provide a clearer understanding of the shape of the
bedrock surface and the distribution of
contamination onsite near the former lagoons
(ERM, 1991b).
The distribution of 1,2,3-TCP in the shallow,
intermediate, and deep bedrock zones in 1986 is
shown in Figures 11, 12, and 13, respectively.
The concentration of both total xylenes and
toluene within these zones was approximately one
order of magnitude less than the concentration of
1,2,3-TCP in 1986 and the overall shape of the
xylene and toluene plumes was similar, hence only
TCP will be shown graphically. Figures 11 to 13
show that the highest concentrations of 1,2,3-TCP
were found in well clusters 3 (810,000 ppb), 6
(1,200,000 ppb), and 11 (980,000 ppb) located
north-northeast of the former eastern lagoons and
in well cluster 10 (400,000 ppb) northwest of the
former western lagoons. Concentrations were
generally highest in the intermediate zone but were
also quite high in the shallow zone, particularly at
11-S (980,000 ppb). Although the investigations
did not extend to the north side of the river in
May 1986, Figures 11 to 13 show that the plume
extended to the river along a broad front. As of
February 1990, ground-water concentrations of
1,2,3-TCP were greatest (1,400,000 ppb) in 31, a
well located south of the Schuylkill River at
intermediate depth (75-99 feet) (ERM, 1990a).
Studies of DNAPL behavior and calculations by
ERM (1987) showed that a very large hydraulic
gradient may be required to move the DNAPL by
ground-water flow because of its density (see
Table 1). This gradient does not exist in the
aquifers underlying this site. Although the
DNAPLs may not respond to the hydraulic
gradients, dissolved contaminants originating from
the DNAPL source are advected with the flow of
ground water. The gradient in the deep aquifer
underlying the floodplain in some areas is upward
toward the river. Therefore, the contamination in
387
-------
Tyson's Dump
Table 1
DNAPL COMPOSITION AND PROPERTIES
1 ,2,3,-Trichloropropane
Xylenes
Ethyl benzene
Toluene
Total
Brookfield Viscosity
Specific Gravity
% by Weight
Well 3-1
23.0
17.0
3.8
4.2
48.0%*
3. cps
1.125gm/cm3
Well 8-1
73.0
5.8
0.9
0.9
80.6%**
7. cps
1 .30 gm/cm3
Source: ERM, 1987
* The balance of the sample composition were compounds eluting later than
xylenes, but not in an elution pattern identifiable as petroleum distillates.
** The balance of sample composition was typical of unidentified petroleum
distillates. Petroleum distillates can be identified as a general class of
compounds because of the characteristic hydrocarbon envelope that is
obtained during gas chromatographic analysis of samples containing these
analytes.
the Schuylkill River is likely the result of baseflow
f with dissolved contaminants discharging to the
river rather than the direct discharge of DNAPLs.
According to ERM, the presence of site-specific
compounds in the river may also be due to runoff
from the drainageways discharging through the
offsite area (ERM, 1987).
ERM (1987) found the solubility of 1,2,3-
trichloropropane to be approximately 1,900,000
ppb; therefore, because the trichloropropane is the
predominant solvent measured in the DNAPL
sample collected at the site, a DNAPL solubility of
1,900,000 ppb was thought to be a reasonable
estimate of the actual solubility of the DNAPL.
Concentrations of dissolved DNAPL greater than
190,000 ppb were interpreted as indicating a
nearby DNAPL source (ERM, 1987). DNAPLs
were found in Wells 2-S, 3-S, 3-1, 5-S, 6-S, 6-1,
and 8-1 in 1986. Efforts to effectively recover
DNAPL were unsuccessful (ERM, 1987).
REMEDIATION
Selection and Design of the
Remedy
Initial remedial efforts conducted by the EPA and
their contractors focused on the onsite
unconsolidated material and consisted of soil
removal and leachate collection and treatment. A
soil vapor extraction system designed to treat the
onsite soil was installed in 1988, and began
operating in November 1988.
The investigations of the offsite area conducted by
ERM showed that the deep bedrock aquifer has
been extensively contaminated with DNAPLs.
Based on the offsite investigation, ERM concluded
that the DNAPLs trapped in the bedrock aquifer
could not be effectively recovered and would
continue to act as a source of dissolved
contaminants in the ground water.
388
-------
Tyson's Dump
LU
Hi
389
-------
OJ
.8
„*•»*«*» «***»
0 ' 100
EXPLANATION
^1 965 L»aoon Location
f 1973 Lagoon Location
Nos.7^Uon*oring W«l ImUJtodh
UnconwftttMDwoMs
xConc«nlratk)n of 1 J J-Tric«oropfopan« In ppm.
Source. ERM, 1987
(Poor Quality Ortalrwn
* '
Figure 10
WSTBIBUHON OF 1 ,2,3,-TRICHLORQPROPANE
IN UliCONSOUDJITED DEPOSITS, MA¥ 1986
TYSON'S DUMP SITE
I
•D
-------
o
Down Dip
Source: ERM, 1967
EXPLANATION
4-8 Wrt Location
ND NoiOfrteclM
— Isoconcentratlon Contour
On SKe Area
Ffgurall «
DISTRIBUTION OF 1,2,3,-TRICHLOROPflOPANE (ppm) ...
IN THE SHALLOW BEDROCK ZONE, 1986 c
TYSONS DUMP SITE 3
•o
-------
o
C-*
o
2-D Wei Location
NO Not Detected
Sourc«: ERM, 1987
(soconcentratton Contour
On-S«eArea
Figure 12 5-
DISTRfBUTH>NOFl^^,-TRfCHLOROPROPANE(ppm) ,-,
IN THE INTERMEDIATE BEDROCK ZONE, 1986 C
TYSCWS DUMP SITE g
"O
-------
o
-C
Source: ERM. 1987
4-O We« Location
NO NotDMKMd
IsoconcwMillion Contour
On Sl« Arta
. _ |
Ftgui*13 . O
DISTRIBUTION OF 1,2^,-TWCWt.OflOPHOPANE (W«nJ §
IN THE DEEP BEDROCK ZONE, 1986 3
TYSON'S DUMP SITE
-------
Tyson's Dump
A number of hydrogeologic tests and a. round of
ground-water sampling were conducted to
determine the hydraulic properties of the bedrock
and the distribution of contamination at various
depths. These data were used to develop a three-
dimensional numerical model of ground-water flow
in the bedrock aquifer along the south bank of the
river (SSP&A, 1988a). A particle tracking model
was also used by SSP&A to simulate contaminant
transport.
As a result of this investigation, two ground-water
recovery systems, one Interim and one final, were
proposed to intercept baseflow to the Schuylkill
River (SSP&A, 1988a). SSP&A designed an
interim system of "seven extraction wells—four 50-
foot wells and three 180-foot wells to be installed
in a line along the Schuylkill River. Modeling
indicated that this system would be capable of
extracting 200 gpra. The interim system was
proposed because it could be brought online
quickly. SSP&A predicted that this system would
be capable of intercepting the most contaminated
ground water in the upper 50 feet of the bedrock
and eliminating most, if not all, of the
contaminated ground-water discharge to the
Schuylkill River, Figure 14 shows the simulated
potentiometric surface and ground-water flowlines
produced by the 7-well interim extraction system,
with a pump rate of 200 gpm. Figures 15 and 16
show the horizontal and vertical zones of capture
of the proposed 7-well interim extraction system.
Six 180-foot-deep test wells, EW-1 through EW-6,
were installed in the bedrock in a line parallel to
and 50 feet from the river bank from November
1987, to March 1988 (SSP&A, 1988a). EW-3,
EW-4, and EW-5 were later completed as recovery
wells as part of the interim extraction system. In
October 1988, recovery Wells EW-10 through
EW-13 were installed (ERM Enviroclean, 1988).
Six of the interim extraction wells, EW-3, EW-4,
EW-5, EW-10, EW-11, and EW-12, began
operating on November 21, 1988. The proposed
depth of installation of the pumps in the first three
wells was 120 to 125 feet, whereas the pumps in
The full-scale ground-water recovery system
proposed by SSP&A consisted of thirteen 180-
foot-deep recovery wells installed in a line along
the Schuylkill River. The projected horizontal
capture zone of the final 13-well system pumped
at 350 gpm is shown in Figure 17. This system
was to be installed after the interim system was in
place. As of June 1991, the final system of
extraction wells had been installed, but the system
had not begun operating, pending EPA
construction of the header system (EPA, 1991b).
EVALUATION OF PERFORMANCE
Hydraulic Control
Figure 18 shows the potentiometric surface
elevations in (be shallow bedrock zone on
September 5, 1990. Extraction Wells EW-3, EW-
4, EW-5, EW-10, and EW-12 were operating on
that date, with a combined pumping rate of
approximately 100 gpm (SSP&A, 1990). This
figure shows that die potentiometric surface around
the operating extraction wells had been lowered to
an elevation of 50 feet or less and that elevations
in non-pumping extraction wells and monitoring
wells had been lowered to less than 60 feet. S.S.
Papadopulos (1990) reports that the average
elevation of the SchuylkiJl River is normally
between 59 and 60 feet MSL. Based on the
potentiometric surface elevations shown on Figure
18, it appears that (he interim ground-water
extraction system is effectively capturing most
ground-water flow along the riverfront between
EW-3 and EW-13. Comparing Figure 5 with 18,
it appears that the capture zone created by the
operating extraction wells may extend laterally as
far as EW-2 on the west and EW-6 on the east.
Flow is also induced from (he Schuylkill River to
the extraction wells when the drawdown is
sufficient, a reversal of natural gradients. The
highest concentrations of 1,2,3-TCP in the shallow
bedrock have historically been observed in
monitoring well clusters 3, 6, and 11. The interim
ground-water extraction system, pumping at a rate
of 100 gpm, appears to be effective at capturing
shallow ground-water flow migrating from the
vicinity of these well clusters.
Another area of high concentration during the RI
was at monitoring well cluster 10 located
considerably west of EW-3. Contaminated ground
water in this area was not expected to be captured
by the interim extraction system but is expected to
be captured by the final system. However, based
the remaining four wells were to be installed at
approximately 65 to 70 feet (SSP&A, 1988b).
The objectives of the ground-water extraction
system are to contain the ground water south of
the river and to stop, or at least limit, the baseflow
of contaminated ground water to the river, on the
potentiometric surface shown in Figure 18, it
appears that the hydraulic gradient between well
cluster 10 and the river may have been reduced, or
394
IHDI
-------
Ui
VO
Ut
-C
o
-C
EXPLANATION
—*—• PatMkt* «I gromtf-watw ttw (pwttelM •fwt«tf •« tap of MM twdrecfc).
— ••—. Cflolour or«M«l p
-------
OJ
N
EXPLANATION
•— Latwal •xiMt of *OM ol capture at lop
of bedrock (48 foot. M3L)
O loc««an of propOMd MW extraction v*N
• TM| <••• convwtad to •xtooeHon «••
Source: SSP&A, 1988a
Figure 15
ZONE OF CAPTURE FOR 7-WELL INITIAL
RECOVERY SYSTEM, 200 GPM
TYSONS DUMP SITE
1
(ft
a
13
-------
-205
400
200 0 200
DISTANCE FROM SOUTH BANK OF fMVf fl (FEET)
400
EXPLANATION
••• 4 PaiMn* of eroontf-wftMr Wow
—00.2- Contour of «qu«l poUnllal, In !•*!
-------
U)
*
oo
N
Scato
Source: SSP&A, 1988a
ZONE CM" CAPTURH FOR 13-WELL
RECOVERY SYSTEM, 350 GPM
P
TJ
-------
ui
8
* • it • r 111 j i
pOTBTOOMenaC SURFACE* THE
MALLOW ttaaocK torn,
(Poor Quality Original)
«<
|
o
-------
Tyson's Dump
at times reversed, depending on the elevation of
the river stage. Although the interim system was
not designed to capture contaminated ground water
in this area, it appears that shallow base flow to
the river from this area has been reduced.
The effect of extraction has been a decrease in the
occurrence of site-specific contaminants in the
river water. Samples of river water at public
water supply intakes downstream have been taken
weekly to monthly since startup. Thirty-seven of
the 40 samples collected at the Pennsylvania
American Water Company's crib intake since the
start of extraction in November 1988, have not
shown detectable levels of 1,2,3-TCP (ERM,
1990a). Of the three remaining samples, only two
were detected above the quantitative detection
limit of 0.5 ppb. By contrast, in the 15 months
before startup, site-related compounds were
detected in 12 out of 37 samples (ERM, 1990a).
These results are shown in Table 2. These data
suggest that the extraction system has reduced the
baseflow of contaminated ground water to the
river.
Concentration Reduction
The distribution of total VOCs (in ppm) in the
shallow, intermediate, and deep zones of the
bedrock aquifer in February 1990, is shown in
Figures 19, 20, and 21. Corresponding total VOC
concentrations in wells north of the river and on
Barbadoes Island in December 1989, are also
shown in brackets, where available. These figures
show that the total VOC plume extends under
Barbadoes Island and the north bank of the river
within the bedrock aquifer. The concentration of
contaminants also clearly increases with depth.
Based on the criterion that concentrations over
190,000 ppb are indicative of a nearby DNAPL
source, it appears that DNAPLs were present as
far as Barbadoes Island within the intermediate
and deep zones of the bedrock aquifer in early
1990.
A comparison to the corresponding December
1989, total VOC concentrations suggests that total
VOC concentrations on Barbadoes Island and
north of the river are increasing over time;
however, ERM (1991) believes that the apparent
increase of VOCs was artificially created by the
introduction of potable water to the borehole
during coring. The drilling fluids were believed to
have temporarily diluted the concentration of
VOCs in the vicinity of the well and this dilution
was reflected in artificially low results from the
first round of samples. Furthermore, ERM (1991)
argues, based on experimental data, that the low
viscosity, high density DNAPL would have
migrated quickly to a meta-s table equilibrium point
and stopped shortly after the lagoons were closed
almost 20 years ago. Therefore, on the basis of
these two rounds, it is not known whether
concentrations were actually increasing; even if
they were, it is unlikely that increases in dissolved
contamination were the result of ongoing DNAPL
movement.
Table 3 shows the concentration of tqtal VOCs
and 1,2,3-trichloropropane in select monitoring
wells since the offsite RI began in 1986. Table 3
includes the cored wells that were installed north
of the south bank of the river starting in 1987. In
general, these data show that concentrations have
decreased at most of the monitoring wells south of
the river. The exceptions to this are some of the
intermediate and deep zone wells, including 31,
4D, 81, 8D, 10XD, and 111. The reasons for these
increased concentrations from September 1986, to
September 1990, are unknown; nor is it clear that
the increase is part of a trend. Some possible
explanations for the differences are: (1) dilution
of the early sample, (2) errors in sampling or
handling, (3) remobilization of DNAPLs during
drilling, (4) the effect of pumping, and (5) the
inherent variability in concentrations in areas near
DNAPL sources.
The concentrations of 1,2,3-TCP in the seven
extraction wells from September 1988, to May
1990, are illustrated in Figure 22. All seven wells
show a significant downward trend following the
startup of the extraction system in November
1988. These data suggest that the concentration of
1,2,3-TCP along the river front is decreasing and
that any potential horizontal baseflow to the river
is less contaminated than before remediation.
However, ERM suggested that this apparent
reduction is caased by dilution of the ground water
with river water drawn in by the extraction system
and reduced time for dissolution of DNAPLs into
ground water during pumping (ERM, 199 Ib). A
sharp increase in the 1,2,3-TCP concentration in
Wells EW-3, EW-11, and EW-12 was observed in
the last quarter of 1989. The reason for the
increase at these three broadly distributed locations
along the river is unknown; however, ERM reports
that increased VOC concentrations have been
400
-------
Tyson's Dump
Table 2
CONCENTRATION OF 1A3-TRICHLOROPROPANE IN THE SCHUYLJOJJL RIVER (ppb)
TYSON'S DUMP SITE
Page 1 of 2
Date
9/2/87
9/10/87
9/16/87
9/23/87
9/30/87
10/07/87
10/14/87
10/21/87
10/28/87
11/11/87
12AJ2/87 •
12/09/87
12/16/87
12/23/87
12/30/87
01/13/88
02/02/88
02/17/88*
03/03/88
03/16/88
03/30/88
04/13/88'
04/27/88*
05/11/88*
05/25/88
06/09/88
06/22/88
07/13/88*
7/27/88*
08/MW88*
Concentration in
River Crib
0.42 B
0.24 B
ND
032 B#
0.25 J#
0.83 B
ND ,
1.1
13
0.88
0.56 B
0.69
1.8
13
NA
NS
1.8
0.87
0.30 B
0.67
0.54 B
1.4
1.2
1.0
032 B
0.64 B
0.44 J
ND
034 B
0.12 J
Date
08/24/88*
09/07/88*
09/21/88*
10/05/88*
10/19/88*
11/02/88*
11/16/88
11/30/88
12/07/88*
12/14/88*
12/20/88*
12/28/88*
01/04/89*
01/11/89*
01/18/89*
01/25/89*
02/01/89*
02/08/89*
02/15/89*
02/22/89*
03/02/89*
03/08/89*
03/15/89*
03/22/89*
03/29/89*
04AM/89*
04/10/89*
04/19/89*
04/26/89*
05/03/89*
Concentration in
River Crib
0.28 B
0.55 B
•0.14 J
ND
ND
ND
ND
0.18 J
ND
ND
ND
ND
ND
ND
ND
ND
0.8 J
ND
ND
ND
ND
0.24 B
ND
ND
ND
ND
ND
ND
ND
ND
401
60177
-------
Tyson's Dump
Table 2
CONCENTRATION OF 1A3-TRICHLOROPROPANE IN THE SCHUYLKEUL RIVER (ppb)
TYSON'S DUMP SITE
Page 2 of 2
Date
05/10/89*
05/24/89*
06/07/89*
06/21/89*
07/05/89*
07/19/89*
08/02/89*
08/16/89*
09/11/89*
09/20/89*
10/04/89*
10/18/89*
11/02/89*
11/15/89*
12/01/89*
Concentration in
River Crib
0.6
0.1 B
ND
0.3 J
ND
ND
ND
ND
ND
ND
ND
ND
ND
ND
ND
Date
01/03/90*
02/07/90*
03/07/90*
05/09/90*
06/06/90*
07/05/90*
08/09/90*
09/05/90*
10/02/90*
11/06/90*
12/04/90*
01/03/91*
02/14/91
03/06/91
Concentration in
River Crib
ND
ND
ND
2.2 B
ND
ND.
ND
ND
ND
ND
0.5
ND
ND
ND
Source: ERM, 1991a
Qualifier Codes:
Analyzed according to modified EPA Method 601 with a quantitation limit of 0.50 ppb.
B - This result is qualitatively invalid since this compound was also detected in a blank at a
similar concentration.
J - This result is a quantitative estimate.
ND - Not detected.
NS - Not sampled.
NA - Not analyzed; all vials were frozen and broken in laboratory refrigerator.
# - Sample vial contained bubbles upon receipt The actual concentration/detection limit may
be slightly higher than reported.
* Analyzed using a DB-624 fused silica megabore capillary column. All other analyses performed
using an SP1000 on Carbopack B packed column.
**Only the River Crib-E will be sampled in the future starting May 25, 1988.
402
-------
T«6fcJ
CONCtNnWTKm Of TOTAL TOC AMB lAJ-TMCHUMtOMtorANE IH
MONITOMNC KfEUJl SINCE IfM H
IffW
TYSON'S DUMP SITE
P*cl*T4
DATE
September IMS
December 1989
FebrMry 1990
September ITO
Tomvoa
TCf
ToulVOO
TVT
TOUI voa
TCT
TOWIVOQ
rcr
Trt.l VOO
TCP
TolrtVOO
TCP
T«ll VOO
TCP
TCP
WELMDNUMMEBS
IS
32,200
3(WW
•
Zl
*^o
&,«»
1,912
i,WO
JS
5O9.200
390,000
31
mjM
810,000
U15,9«
i,«n,ooo
ID
1,619
6?
2M
140
48
Z2320
ZiOOO
41
3,411
3,400
WM
4500
4D
22,r9»
22.000
1IOJ90
110,000
58
285.700
230,000
SI
1,713
I,1W
m
290
so
2a,*»
90
423
NO
Competed (rora ERM, M* 1990, Appendtt 1; KRM, Motfe Wl; F.RM, JVM 18, I9»Ie
Tout VOC cancmmwra luctadc til axBttaeMi aaxft Ihae deieded i» modMeiJ b4»nti
ts
9M,«n
900j06Q
M
l^SMW
1^00,000
1,151200
1,100.000
to
M.466
ss.om
«JI7I
Moe
78
230
230
MO
S30
120
320
2W
_ZLJ
W7
T90
4R3
4M
TO
218
190
47
44
o
en
a
•o
-------
BATE
September 1996
September 1988
.September 1989
December 1989
Fcbrtutry 1990
September 1990
ToulVOCi
TCP
Tout VOC.
TCP
Toll! VOO
TCP
ToUIVOGl
TCP
Tout VOC,
TCP
ToUIVOe*
TCP
TouJ VOC.
TCP
TCP
Tkkkl
CONCENTRATION OF TOTAL VOC AND UVVnUCHLOSOrROPANE IN
MONITORING WELLS S1HCK IMf 81
(«*)
TYSON'S DUMP SITE
WEU. ID NUMBERS
«S
3J«0
ISM
6^36
MOO
IJOO
1300
2300
M
154.500
150,000
661,765
640,000
ID
MOO
7,700
15,082
ISAM
M
ND
ND
M
14
ND
ND
ND
fD
11
ND
n
o •
IBS
WSJ
2,700
6335
SflOO
. 583
tm
920
IK
432^00
400JQOQ
485,259
**>#»
10D
103,720
100,000
21,515
20^)00
I1XD
69^70
69,0»
124/S52
!20J»0
111
1,050.400
990,000
1,060474
1,000.000
760,000
920^00
111
249,780
ZM,000
524,905
490,000
IID
31,150
20,000
7,110
6,700
its
1,462
ND
lfl»
ND
(80
4
2
12D
17
17
13
297
730
14
16,750
1,100
Compiled Irani ERM, M^ 1990, Appends 1; ERM, Mirrt 1991; ERM, Jont 18, 199lc
ToW VOC OMtcemrMiaa mdwfc »11 cawlHocntt acefM time deKcled in «>aciiMd Hub
3
«T
O
'
-------
TiMrl
COMCKMTRATIOK Of TOTAL VOC *W> I JJ-flllClttOHOPllOMWE W
MONITORING WELLS SINCE ItK M
(Pf*)
TYSONS DUMP SITE
DATE
ScptetBoer 1996
AuptU ISS7
Septerotier 14SB
September 1989
December I9R»
Febnui? J9W
September^
ToulVOCt
TCP
T«»l VOC«
TCP
Tolut VOCl
TCP
Tolll VOCl
TCP
Tool VOCl
TCP
Toll! VOC*
TCP
Toui VOC»
TCP
TCP
Ctn^WiRI
CWI-I
2.907
2.900
4.COS
4,600
2MO
2300
6,000
CWI-J
ITS-MI
,
79«
7I»
1.911
1,900
2,123
2,100
IJMS5
1SS
ise
189
ISO
443
430
2.909
CW1-4
17
1C
3
2
33
27
33
C«n4 WtH I
CWH
XO
2
ND
CWI.J
7 '
ND
9
ND
2
ND
CWM
c
ND
8
ND
9
ND
CW1-4
tt-lll
1
ND
3
ND
3
ND
CM^Wriil
CWH
ITt-IM
I
ND
4
ND
CWM
2
ND
2
ND
Compiled from ERM. Mi» 1990. Appendfe 1; md ERM, Much 19)1
Toll! VOC coocetmwtom include »« cixnMueno raceja HICK detected hi awiciMed M»nk»
CW34
11
ND
J9
ND
CWM
ShrfW.
C^4Well4
CW4-I
182J33
IMAM
1^23^20
1.200,000
CW4-I
•T.1M
-------
T«Mt3
CONCENTRATION OF TOTAL VOC AND lAMTMCHLOROMSOPANE IN
MONITORING WELLS SINCE IMC M
TYSONS DUMP SITE
hftJoM
DATE
September 1996
August 1987
Att(tml987
September 1988
September 1989
December 1989
Febrenyl990
September 1999
Toul VOa
TCP
r««i voo
TCP
Taul VOCl
TCP
Touivoa
TCP
TaUlVOa
TCP
ToUIVOO
TCP
CwtdWdl?
CW7-4
37
ND
CW7J
56
ND
CW7-J
36
ND
CW7-1
8
ND
OredWcUl
CW»-4
13
ND
CW*-1
CWt-2
2
ND
CWf-1
' 25
ND
DS-1
3
ND
DB-2
ND
127
120
Compiled ban ERM. Miy 1990. Appetite I; mi ERM. Mircti 1991
Tout VOC canceninlion include ill coral ituetiu acepi tho«e daecled in moctMcd bUiib.
I
(A*
a
-------
Norristown
Flpw.1t
TOTAL VOC* M TME tHALLON
w"
O
T3
-------
i
9
\
CW-S VMLOCMOI
499 ComnMnoM
OlMC Compoundl h n|n
TO>4B
I 1
IMDMKM
-------
Norristo wn
PA
Anriericon
Water Co.
•*«-•!
Norristown
Dom
: EBM 1999»
TOTM. WOCt MTM DCEI> MMWCK
20W|p(»n),FE«m
TV SOWS DUMP SITE
i
«r
o
"O
-------
Tyson's Dump
300000
200000-
100000-
0'
1988
200000
100000-
300000
200000
100000-
1989 1990
YEAR
1988 1989 1990
YEAR
1988 1989 1990
YEAR
1991
1991
1991
EW-3
EW-U
EW-13
EW-5
EW-10
EW-4
EW-12
CONCENTRAnON OF 1&3 -TRICHLOROPROPANE
IN THE SEVEN EXTRACTION WELLS
TYSON'S DUMP SITE
410
-------
Tyson's Dump
observed after even brief shutdown of the
extraction system (ERM, 1991b). The
concentrations of 1,2,3-TCP in the influent to the
ground-water treatment system shown in Figure 23
also shows that the concentration of 1,2,3-TCP
entering the extraction system along the river front
has decreased since slartup,
SUMMARY OF REMEDIATION
The soil and ground water at the Tyson's dump
site have been heavily contaminated with organic
compounds, principally 1,2,3-trichloropropane and
other VOCs, as a result of the disposal of waste
liquids into unlined lagoons in the onsite area in
the 1960s. A substantial fraction of the
contaminants are thought to be present as dense
non-aqueous phase liquids (DNAPLs).
Investigations have further shown that contamina-
tion in the bedrock aquifer extends from the onsite
area to the north side of the Schuylkill River, and
that contaminated ground water discharges to the
river, potentially threatening downstream water
users. DNAPL contamination within the bedrock
aquifer is believed to extend to a depth of at least
135 feet south of the river, and to a depth of at
least 200 feet under Barbadoes Island. These
DNAPLs are believed to have migrated northward .
from the disposal area by gravity flow along
bedding planes in the sandstone bedrock, which
dips north-northwest at approximately 12 degrees.
The direction of horizontal ground-water flow is
radially northward from the disposal area to the
river. Upward vertical gradients in the bedrock
aquifer in the central portion of the site south of
the river, and contamination in the river water
indicate that ground water contaminated with
VOCs discharges to the river from the bedrock
aquifer. DNAPLs are not expected to discharge to
the river because of their depth and density.
However, the DNAPLs in the bedrock are believed
to act as a long-term source of contamination to
the river via the upward flow of dissolved
constituents. The restoration of the aquifer was
deemed to be unattainable in the immediate
vicinity of the DNAPL, because the DNAPL acts
as a continuous source of the solute plume.
In order to limit baseflow of contaminated ground
water to the Schuylkill River from the area south
of the river, a ground-water extraction system was
installed along the south bank of the river. An
interim system of seven extraction wells began
operating in November 1988. A larger system of
13 extraction wells was proposed to supplement
the interim system and increase the zone of
capture of the extraction network. This final
system had been installed, but was not operational
as of June 1991.
The extraction system has been partially successful
In its objectives of containing the plume of
dissolved constituents south of the river and
limiting the baseflow of contaminated ground
water. Limited available data on the hydraulic
response to pumping suggests that part of the
plume has been captured by the system since
startup in November 1988. However, February
1990, data show that the plume is not captured by
the system between EW-11 and EW-5 and east of
EW-5 when extraction Wells EW-10, EW-12, and
EW-13 are not operated. Information on the
capture zone that is produced during periods when
all seven wells are operated was not available for
review. More complete information on pumping
history is needed to judge whether the central part
of the contaminant plume has been captured as
effectively as projected. However, it is known that
a substantial portion of the plume east of EW-3
and west of EW-13 has not been, and was not
expected to be, captured by the interim system.
The system has decreased the frequency with
which site-specific contaminants are detected in
" the river water downstream of the site. Only two
of the 40 samples collected near the intake of a
downstream water supplier have contained 1,2,3-
TCP above detection limits since extraction began,
versus 12 out of 37 samples collected before
startup. Therefore, the system does appear to have
reduced the threat to the health of downstream
water users caused by contamination at the
Tyson's site. The concentration of 1,2,3-TCP in
the extraction wells and in the influent to the
treatment system have decreased substantially
since remediation began. However, ERM believes
that concentrations in the extraction wells and the
influent are only lowered as a result of dilution
effects during .pumping; if the extraction system
were shut off, dissolved-phase VOC concentrations
would be expected to return to historically high
levels as a result of DNAPL dissolution (ERM,
1991b). Future extraction of ground water
underlying Barbadoes Island has been prescribed
by the EPA in a September 1990, ROD. This
extraction is intended to control the dissolved
'plume near the DNAPLs in this area.
411
-------
10
IU
400000
MOOOO J
200000 -
100000 -
1988
I
1989
1990
1991
YEAR
o
Figure 23 3
CONCENTRATION OF 1,2,3-TRICHLOROPHOPANE w"
IN THE INFLUENT TO THE GROUND-WATER
TREATMENT SYSTEM
TYSONS DUMP SITE
•o
Q
-------
Tyson's Dump
SUMMARY OF NAPL-RELATED
ISSUES
Dense non-aqueous phase liquids (DNAPL) have
been found in several bedrock wells south of the
Schuylkill River at the Tyson's Dump site. These
DNAPLs are believed to have migrated downward
from the unlined disposal lagoons into the bedrock
aquifer, where further migration was facilitated by
vertical and horizontal fractures. Northward
migration of DNAPLs towards the river was
favored by prevailing northward hydraulic
gradients, vertical high angle joints, the northward
slope of the bedrock surface, and the 12 degree
north-northwestward regional dip of the bedrock
strata. DNAPLs have been directly observed to a
depth of 135 feet in monitoring Well 8-1 on the
south bank of the river.
ERM has estimated the solubility of the DNAPL
to be approximately 1,900,000 ppb and has
interpreted concentrations over 190,000 ppb to
indicate a nearby DNAPL source. Based on this
criterion, the concentration of 1,220,000 ppb of
total VOCs observed in the deep interval of
monitoring Well CW-4 on Barbadoes Island in
February 1990, suggests that DNAPLs had
migrated to a depth of 200 feet beneath Barbadoes
Island by early 1990. The maximum concentration
north of the river in February 1990, was 6,000
ppb, which suggests that DNAPLs may not have
reached the north side of the river by that time.
BIBLIOGRAPHY/REFERENCES
ERM. July 29, 1987. Tyson's Site, Montgomery
County, Pennsylvania, Off-Site Operable Unit
Remedial Investigation Report, Volume 1.
ERM. May 31, 199s Oa. Draft Tyson's Site Third
Addendum Investigation Report.
ERM. June 1990b.
Feasibility Study.
Off-site Operable Units
ERM. March 6, 1991 a. 1990 Annual Monitoring
Well Report, Tyson's Site.
ERM. June 17, 1991b. Letter from Mr. Joe Ferry
to Steven Brown of CH2M HILL, Re: Review of
Draft Case Study of the Tyson's Site, File: 272-
23-01-01.
ERM. June 18, 1991c. Personal communication
with Mr. Joe Ferry.
ERM. March 29, 1991d. Letter to Mrs. Karline
Tierney of Ciba-Geigy Regarding Monthly
Progress Report for the Remedial Investigation/
Feasibility Study (RI/FS) of the Tyson's Site Off-
Site Operable Units RI/FS, March 1991.
ERM Enviroclean. November 1988. Ciba-Geigy
Corporation, Tyson's Site, Progress Report for
October 1988.
ERM Enviroclean. December 1988. Ciba-Geigy
Corporation, Tyson's Site, Progress Report for
November 1988.
S.S. Papadopulos & Associates, Inc (SSP&A).
August 1988a. Installation and Hydrogeologic
Evaluation of Test Wells and Design of a Ground-
Water Recovery System, Tyson's Site, Montgomery
County, Pennsylvania.
SSP&A. October 21, 1988b.
Ferry of ERM.
Letter to Mr. Joe
SSP&A. October 22, 1990. Letter to Ms. Karline
Tierney of Ciba-Geigy Corporation.
U.S. Environmental Protection Agency (U.S.
EPA). December 1984. Superfund Record of
Decision: Tyson's Dump Site, PA, EPA/ROD/R03-
84/008.
U.S. EPA. March 1988a. Revised Superfund
Record of Decision: Tyson's Dump Sit, PA.
EPA/ROD/R03-88/045.
U.S. EPA. September 1988b. Superfund Record
of Decision: Tyson's Dump Site, PA.
EPA/ROD/R03-88/068.
U.S. EPA. September 1990. Superfund Record of
Decision: Tyson's Dump Site, PA. Operable Unit
3.
U.S. EPA. June 10, 1991a. Personal
communication with Kathy Davies, Regional
Hydrogeologist, Region III.
U.S. EPA. June 24, 1991b. Personal
communication with Kathy Davies, Regional
Hydrogeologist, Region III.
413
-------
CASE STUDY 24
Western Processing
Kent, Washington
Abstract
Western Processing is a former waste recycler and storage facility. The site was closed in
1983. In July 1984, site cleanup began with the removal of waste from the area and the
installation of a slurry wall around the facility. In July 1988, a ground-water extraction and
treatment system began operation. The extraction system consists of 206 well points in the
shallow ground-water zone, each designed to recover 1 gpm. An inward head gradient is
maintained across the slurry wall. Data collected from well points in 1990 indicate
reduction in concentrations for only a few contaminants. Plumes of most metals and
organics remained stable or increased in concentration between 1988 and 1990. However,
the data indicate that metals and organics are being recovered by the well point extraction
system. An LNAPL, consisting of diesel motor oil and solvents, has been observed in two
well points.
Background Data
Date of Problem Identification
Extraction Started
Types of Contaminants
Primary Aquifer Materials
Maximum Number of Extraction Wells
Maximum Total Extraction Rate
Estimated Plume Area
Estimated Plume Thickness
Maximum Reported Concentrations
1983
July 1988
Metals, Organics
Interbedded sand, silt, 'and clay over medium
silty sand
206
220 gpm
14 acres
65 feet
Trans- 1,2-Dichloroethene 390,000
Toluene: 180,000 ppb
Zinc: 510,000 ppb
Nickel: 280,000 ppb
ppb
414
-------
CASE STUDY
WESTERN PROCESSING
BACKGROUND OF THE PROBLEM
This case study summarizes the remediation of
ground-water contamination at the Western
Processing site located at 7215 South 196th Street
in Kent, Washington. Ground water at the site is
contaminated with numerous metals and organics.
A site location map is presented in Figure 1.
SITE HISTORY
From 1952 to 1961 the site was leased to the U.S.
Army for use as an anti-aircraft artillery battery.
In 1961 the site was turned over to the owner
without removal of general support facilities and
sold to Western Processing Company, Inc. From
1961 to early 1983 various chemical reclamation
and industrial waste processing and storage
activities were conducted on 11 of the 13 acres.
The remainder of the site was used for residential
purposes.
The principal wastes received by Western
Processing include: electroplating solutions and
sludges, pesticides and herbicides, spent acid and
caustic solutions, waste oils and solvents, battery
mud, flue dust from secondary smelters, aluminum
slag, and galvanization skimmings.
After the site was closed in early 1983, emergency
removal was conducted by the U.S. EPA.
Hundreds of thousands of gallons of hazardous
chemicals, paint sludges, and wastewater from
ponds and tanks were removed from the site. Th'e
Washington State Department of Ecology installed
stormwater control measures in late 1983.
In July 1984, site cleanup began. This included
removing liquid, solid, and demolition waste from
the site. A slurry wall was installed around a
16.5-acre area to mitigate ground-water migration
and additional stormwater measures were
implemented. In July 1988, a ground-water
extraction and treatment system began operating.
GEOLOGY
Western Processing is located near the north-south
axis of the Duwamish (Kent) Valley, a former
embayment of Puget Sound. The edges of the
valley can be seen at the east and west margins of
Figure 1. The valley has been partly filled with
Recent deposits. The east and west margins of the
Duwamish Valley are defined by a dissected
glacial drift plain with elevations approximately
350 to 600 feet above the valley floor (CH2M
HELL, 1984).
Consolidated rock in the area is exposed only
where there are small outcrops of Tertiary
extrusive and intrusive igneous rocks at the
northern end of the valley. The uplands bordering
the valley are composed of Pleistocene glacial and
interglacial deposits. The valley fill is primarily a
sequence of Recent alluvial and lacustrine
deposits. Recent sediments are typically fine- to
medium-grained sands, silts, peaty silt, and clay.
The total depth of valley fill apparently exceeds
500 feet (CH2M HELL, 1985).
The White River alluvium underlies the Western
Processing site. The alluvium consists of a
complex sequence of discontinuous interbedded
silt, sand, and clay lenses to approximately 40 feet
below the ground surface. A fairly continuous fine
to medium sand with intermittent silty zones exists
below 40 feet. A deep well south of the site
showed that sand and silt extend to a depth of
approximately 150 feet. Beyond this depth, dense
clay and silt were found to extend to at least 365
feet below grade (CH2M HELL, 1985). Figure 2
presents a schematic geologic column showing the
three major hydrogeologic units that underlie the
site.
HYDROGEOLOGY
The Western Processing site is bordered by Mill
Creek on the west. Mill Creek is a tributary of the
Green River, which drains to Puget Sound.
415
-------
Western Processing
Sourc* USGS. Barton and OnMoimt, VMwMngton QmdnngM, 1973
0 1000 2000
Sc«l*inF**t
FJflunH
(Poor Quality Original) SITE LOCATION MAP
WESTERN PROCESSwa SITE
KENT, WA8HINQTON
416
-------
Western Processing
40 Ft
Discontinuous tenses of Silt,
Clay, and Sand.
Kh«1 tolOfUday
150 Ft
Fine-Medium Sand With
Discontinuous Silt Lenses.
Kh.iO to 100 ft/day
Source; CH2M HILL, 1985
Figure 2
SCHEMATIC GEOLOGIC SECTION
WESTERN PROCESSING SITE
417
-------
Western Processing
Ground water in the area occurs primarily in
unconsolidated fluvial, marine, lacustrine, and
glacial deposits. The most productive aquifers are
outwash deposits of the glacial drift that comprise
the uplands. Ground water in the valley floor is
typically very shallow, with an average depth to
water of less than 10 feet. The ground may
become completely saturated in low areas during
wet periods (CH2M HILL, 1984).
Confined ground water occurs frequently in the
area as a result of the complex stratigraphy and
generally fine grained sediments. A flowing
artesian system, meeting part of the City of Kent's
water needs, occurs at depths of less than 300 feet
near the east and west valley margins (CH2M
HILL, 1984).
Ground water in the area is recharged primarily by
precipitation in the uplands bordering the
Duwamish Valley. Ground-water flow is toward
the valley axis and northward toward Puget Sound.
Ground-water losses include discharge to stream
channels and Puget Sound, spring discharges, and,
to a much smaller extent, discharges as a result of
pumping wells and evapotranspiration (CH2M
HILL, 1984).
Deposits underlying Western Processing exhibit
complex small-scale stratigraphy. Sediments are
generally fine-grained sands, silts, and clays. Silty
sands and sandy silts are the most commonly
encountered sediments. Portions of the site have
been filled with a variety of materials. Battery
fragments and black cinders have been reported.
The depth of fill is highly variable across the site
(CH2M HILL, 1984).
Ground water at the site occurs at an average
depth of 6 feet. A ground-water elevation contour
map for the shallow flow zone in August 1984,
before installation of the slurry wall, is shown in
Figure 3. Ground-water movement is affected by
four primary factors: (1) regional ground-water
flow toward the Green River, which has an
upward flow component, (2) ground-water
recharge and mounding onsite, which has a down-
ward flow component, (3) discharge to Mill Creek
and the east drain, and (4) variations in hydraulic
conductivity. Local ground-water flow patterns in
the upper 100 feet are complicated by
discontinuous silt and clay lenses in the upper
40 feet (CH2M HILL, 1984).
Ponded surface water, high precipitation
infiltration, and/or variations in hydraulic
conductivity of the soil caused a ground-water
mound to form near the center of the site in excess
of the mound that would naturally exist between
two discharge areas such as Mill Creek and the
east drain (CH2M HELL, 1985). The horizontal
flow gradient is radial from the center of the site.
Vertical gradients also strongly influence the local
ground-water flow. Figure 4 presents a schematic
cross section that illustrates the vertical gradients.
The downward gradients are strongest in the
middle of the site. Downward ground-water flow
becomes less pronounced near the site boundary;
flow eventually reverses and is upward at the two
drainages. At the north end of the site, horizontal
flow predominates at depths below 70 feet (CH2M
HELL, 1985).
WASTE CHARACTERISTICS AND
POTENTIAL SOURCES
Fifty-seven EPA priority pollutants were identified
in ground-water samples collected hi 1984 from
onsite and offsite wells (CH2M HILL, 1984).
Eighteen priority pollutants, six metals and twelve
organics, were selected as indicator contaminants.
These indicator contaminants are listed in Table 1.
The average concentrations of compounds detected
in ground water in 1984 by area of the site are
given in Table 2. The site areas are shown in
Figure 5.
Figure 6 shows a 1984 map of total indicator
metals concentrations measured in ground water at
various depths. Metals in ground water were most
pronounced hi shallow wells located on the
northern half of the site. Total indicator metals in
these wells often exceeded 100,000 ppb. Ground
water is Shallow wells on the south end of the
site, where metals in soils were highest, contain
considerably lower concentrations of indicator
metals, usually less than 10,000 ppb. Table 3 lists
the maximum concentration detected for each
indicator metal.
Indicator metals exceeded 100,000 ppb in two
onsite intermediate wells in the central and north
central sections of the site. Indicator metals were
above 10,000 ppb in one well on the southern half
of the site. Indicator metals in deep wells were
highest in one onsite location at the northeastern
corner of the site with concentrations slightly
418
-------
Western. Processing
Table 1
SELECTED INDICATOR CONTAMINANTS
WESTERN PROCESSING SITE . '
Organics
Volatile Organics:
1,1,1-Trichloroethane
Trans-l,2-Dichloroethene
Tetrachloroethene
TrjcWoroethene
Toluene
Chloroform
Acid Extractable Compounds:
2,4-DimethyIphenol
Phenol
Base/Neutral Compounds:
Total PAHs*
Total Phthalates
Other Organics:
PCBs
Oxazolidone
Inorganics
Metals:
Cadmium
Chromium
Copper
Nickel
Lead
Zinc
Source: CH2M HILL, 1984
"Total priority pollutant polycyclic aromatic hydrocarbons (PAHs).
419
-------
Western Processing
Table 2
AVERAGE CONTAMINANT CONCENTRATIONS
WESTERN PROCESSING SITE
Page 1 of 3
Area
Contaminant
Average
Groundwater
Concentration
6-15 ft
(PPb)
Average
Groundwater
Concentration
15-30 ft.
(ppb)
I/II Volatiles
Phenol
Methylene chlorine
Trans 1,2-dicWoroethene
Chloroform
Trichloroethene
1,1,1-Trichloroethane
Toluene
Tetrachloroethene
Ethylbenzene
108,583
56,872
20,297
2,378
29,508
21,609
1,633
109
2
1,490
48,971.
154
2,012
7,244
1,014
314
0
0
BN/AE
Naphthalene
Phenanthrene
PCS
Pyrene
Fluoranthene
Benzo(a)anthrancene
Bis(2-ethylhexyl)phthalate
2 -
0
0
0
0
0.3
0
23
0
0
0
0
0
0
Metals
Nickel
Cadmium
Zinc
Chromium
Arsenic
Copper
Lead
15,129
2,391
126,447
5,249
14
1,333
340
14,250
964
117,687
313
12
757
263
420
-------
Western Processing
Table 2
AVERAGE CONTAMINANT CONCENTRATIONS
WESTERN PROCESSING SITE
Page 2 of 3
Area
Contaminant
Average
Groundwater
Concentration
6-15 ft.
(ppb)
Average
Groundwater
Concentration
15-30 ft.
(ppb)
V Volatiles
Phenol
Methylene chlorine
Trans 1,2-dichloroethene
Chloroform
Trichloroethene
1, 1, 1-Trichloroethane
Toluene
Tetrachloroethene
Ethylbenzene
745,954
40,603
147,005
1,213
89,535
3,620
1
183
0
39
122
0
3,787
8,310
0
44
0
0
BN/AE
Naphthalene
Phenanthrene .
PCB
Pyrene
Fluoranthene
Benzo(a)anthrancene
Bis(2-ethylhexyl)phthalate
0.
0
0
0
0
0
0
23
0
0
0
0
0
0
Metals
Nickel
Cadmium
Zinc
Chromium
Arsenic
Copper
Lead
1,327
. 68
18,284
66
5
42
29
461
119
30,876
80
15
24
21
421
-------
Western Processing
Table 2
AVERAGE CONTAMINANT CONCENTRATIONS
WESTERN PROCESSING SITE
Page 3 of 3
Area
Contaminant
Average
Groundwater
Concentration
6-15 ft.
(ppb)
Average
Groundwater
Concentration
15-30 ft
(Ppb)
IX Volatiles
Phenol
Methylene chlorine
Trans 1,2-dichloroethene
Chloroform
TricWoroethene
1,1,1-Trichloroethane
Toluene
Tetrachloroethene
Ethylbenzene
0
20
118
0.3
106
10
0.1
-0
0
0
5
18
0
46
7
0
0
0
BN/AE
Naphthalene
Phenanthrene
PCB
Pyrene-
Fluoranthene
Benzo(a)anthrancene
Bis(2-ethylhexyl)phthalate
0
0
0
0
0
0
0
0
0
0
0
0
0
0
Metals
Nickel
Cadmium
Chromium
Arsenic
Copper
Lead
540
94
*
7
0
3
0
0
0
0
0
0
0
Source: CH2M HILL, 1984
Note: Undetected constituents listed as 0
422
-------
Western Processing
Table 3
MAXIMUM INDICATOR METALS IN SHALLOW GROUND WATER
WESTERN PROCESSING SITE
Compound
Cadmium
Chromium
Copper
Lead
Nickel
Zinc
Depth
(feet)
13
13
10
10
13
10
Concentration
(ppb)
60,000
65,000
13,000
3,300
280,000
510,000
423
IU7
-------
Western Processing
j**
Wtt* u** emtton in FM<
•«»• wmr l**«i Omftw M P*tt
CCoraMM (or Upmrd OrMMnt)
WM* UMl Owntion centaur
tf I I I
*. Ma »» MM mm miiiiii Mr m
«!•«•» •••! »I»IH x Mt ntimtt.
250
500
Source: CH2M HILL, 1985
(Poor Quality Original)
Rgur»3
SHALLOW GROUND-WATEfl ELEVATON
CONTOURS
WESTERN PflOCeSSlNa SITE
424
-------
I/I
EAST
WEST VALLEY HIGHWAY
, GROUND SURFACE
, WATER TABLE
MI(LL WESTERN PROCESSING
CREEK f
(Not to Scale)
CM2MHILL, 1985
i
(0
®
5
8
(A
SCHEMATIC REPf?ESENTATK>N OF LOCAL
GROUND-WATER FLOW SYSTEM
WESTERN PROCESSING SITE
-------
o\
I ~~r~
„ I 3
SLU/t*r WALL
LEGEND
C~U~~\ «»E* OSSI6MTK3N
••««wj
|\C8" j CELL DESIGNATION
ZOO
Source: Canonie Environmental, 1988
Figures
AREA AND CELL DESIGNATION
WESTERN PROCESSING SITE
i
»
*>+
9
3
J2.
5"
(Q
-------
mocmtn rnit
I
I
8
»
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-------
Western Processing
above 1,000 ppb. All other intermediate and deep
wells had concentrations only slightly above
background.
Volatile organic compounds (VOCs) in ground
water were at highest concentrations in shallow
onsite wells in the central and northern half of the
site. Figure 7 presents a 1984 map of total VOC
concentrations at various depths. The highest total
VOC concentrations detected were 1,346,000 ppb
and 660,000 ppb. Total VOCs in intermediate
depth wells are the highest in onsite wells.
Volatile organics were found in several wells in
concentrations much greater than those found
elsewhere. Methylene chloride was highest in
Wells 15 and 9, trichloroethene (TCE) in Wells
15, 21, US, and 17S, 1,1,1-TCA in Wells 15 and
IIS, and trans- 1,2-dichloroethene in Well 21.
These wells were considered potential source areas
from which volatile organics could migrate.
Table 4 lists the concentrations of volatile organics
in wells having more than 100,000 ppb total
volatiles. Concentrations of TCE as high as
20 percent of solubility were observed, which
strongly suggests the presence of a nonaqueous
phase. Trans-l,2-DCE was observed at 390,000
ppb. This is 65 percent of solubility (600,000
ppb), most likely indicating the presence of
nonaqueous product.
Semivolatile organics concentrations exceeding
10,000 ppb were only detected in shallow ground
water. The maximum concentration of total acid-
extractables detected was 5,400,000 ppb in
Well 27. The northern half of the site exhibited
the highest levels of contamination. The most
frequently detected acid extractables were phenol
and 2,4-dimethylphenol. Base/neutral compounds
were detected infrequently. Concentrations of
base/neutrals were considerably lower than other
contaminants with concentrations generally lower
than 20 ppb.
REMEDIATION
Selection and Design of the
Remedy
The objectives of ground-water remediation are to
allow no further contamination of shallow ground
water and reduce ground-water contaminant
concentrations to levels that will protect the
aquatic organisms in Mill Creek. The first phase
of the remediation involved surface cleanup. The
second phase included installation of a
containment wall and a ground-water extraction
system, which was expected to operate for at least
five years.
The containment wall, shown in Figure 8, is
constructed of soil-bentonite slurry with a
hydraulic conductivity of 10"7 cm/sec. The slurry
wall is 3 feet wide and extends 46 feet below
grade (Landau Associates, 1987).
The extraction system, also shown in Figure 8,
includes 206 shallow well points, approximately
30 feet deep. The extraction system includes
onsite, barrier, and trans-l,2-DCE extraction
(referred to as "trans") well systems. The trans
wells are specifically for the mitigation of the
offsite plume of trans-l,2-DCE.
Six well points are located in Area V outside the
slurry wall
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* TtUM MEU. ItSTCH
WELL
Source: Canorte Environmental, 1988
(PoorQu«lttyOriflln»J)
rorr
Figure 8
SITE LAYOUT
WESTERN PBOCESSWa SITE
I
§
o
8
ta
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Western Processing
Table 4
VOLATILE ORGANICS IN WELLS
HAVING MORE THAN 100,000 ppb TOTAL VOLATILES
WESTERN PROCESSING SITE
Page 1 of 2
Well
Number
Depth
(feet)
Compound
Concentration
(ppb)
Onsite Wells
15
TOTAL
21
TOTAL
9
TOTAL
US
TOTAL
14.5
13
13
10,5
Methylene Chloride
1,1, 1-Trichloroethane
Trichloroethene
1,1-Dichloroethane
Chloroform
1,2-Diehloroethane
Toluene
Trans-l,2-Dichloroethene
Trichloroethene
Methylene Chloride
Vinyl Chloride
Methylene Chloride
Trichloroethene
1,1, 1-Trichloroethane
Trans-l,2-Dichloroethene
Toluene
Trichloroethene
1,1,1-TrichIoroethane
Methylene Chloride
Toluene
1, 1-Dichloroethane
720,000
340,000
210,000
33,000
27,000
16,000
5Ma
1,346,005
390,000
170,000
100,000
360
660,360
220,000
17,000
5,500
4,600
2,400
249,500
80,000
73,000
46,000
2,800
2,100
203,900
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Western Processing
Table 4
VOLATILE ORGANICS IN WELLS
HAVING MORE THAN 100,000 ppb TOTAL VOLATILES
WESTERN PROCESSING SITE
Page 2 of 2
Well
Number
11D
TOTAL
17
TOTAL
Depth
(feet)
27.5
13.5
Compound
Methylene Chloride
Trichloroethene
1,1,1-Trichloroethane
Toluene
Trans-l,2-Dichloroethene
Trichloroethene
Methylene Chloride
Toluene
Chloroform
Benzene
1,1, 1-Trichloroethane
Fluorotrichloromethane
Concentration
(ppb)
250,000
14,000
5,200
1,100
780
271,080
42,000
42,000
22,000
12,000
2,200
1,700
920
122,820
Off-Property Wells
27
TOTAL
10
Trichloroethene
1,1,1-Trichloroethane
Methylene Chloride
Chloroform
Toluene
140,000
20,000
16,000
6,700
5M"
182,705
Source: CH2M HILL, 1985
aM indicates compound detected but not quantified.
432
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Western Processing
Table 5
WELL POINT EXTRACTION SYSTEM EXAMPLE PERFORMANCE
NORMAL CELL FLOW DISTRIBUTIONS AT VARIED TOTAL FLOW RATES
(AREA 1)
Cell No.
1
2
3
4
5
6
7
Well
Count
10
18
30
36
30
60
16
Cell Flow Distribution (gpm)
200 gpm
Total
10
18
30
36
30
60
16
150 gpm
Total
7.5
13.5
22.5
27
22.5
45
12
1 00 gpm
Total
5
9
15
18
15
30
8
50 gpm
Total
2.5
4.5
7.5
9
7.5
15
4
Source: Canonie Environmental, 1988
inward gradient and not exceeding the treatment
plant capacity. Precipitation is a factor in
determining extraction and infiltration rates
(Canonie Environmental, 1988).
The infiltration system was not operated during the
first two months of ground-water extraction to
collect data on aquifer drawdown. Once the
infiltration system was started, infiltration was
adjusted to produce at least a one foot drop in the
water table across the slurry wall.
Extracted water is treated in a pretreatment plant,
where metals are precipitated out of solution and
volatile organics are removed by an air stripper.
A portion of the treated water is used in the
infiltration system, and the remainder is discharge
to the Seattle Metropolitan Sewer System.
EVALUATION OF PERFORMANCE
Hydraulic Control
Figure 9 is a ground-water elevation contour map
showing the shallow flow zone in November 1989.
Flow at the southern portion of the site is radially
inward. Row in the northern portion is to the
northwest. An inward ground-water flow gradient
has apparently not been maintained at the northern
end of the site.
Data collected from the piezometer pairs in
November 1990, indicate that inward gradients
exist across the slurry wall ranging from -0.02
feet/foot, at several locations at the northern end of
the site to 17 feet/foot. During November 1990,
the average head difference across the wall at the
18 monitoring points was 4.8 feet (Ecology and
Environment, 1988 through 1990).
Reductions in Mass Concentration
6f Contaminants
Figure 10 presents concentration contour maps for
cadmium in shallow ground water in 1988 and
1990. The 1988 data in Figure 10 were collected
from the extraction well points soon after
installation of the system. The maximum
cadmium contamination occurs in the center of the
site. The maximum cadmium concentration
observed in 1988 was greater than 8,000 ppb. The
maximum cadmium concentration observed in
433
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Western Processing
KEY
Meniortng W«i or PStioimw Locakxi
,4.0 Contour Btvttton* 1-Foot Interval
Sourca: Landau Associates, 1191 a
QROUND-WAT1R ELEVATION CONTOURS
FOR THE SHALLOW ZONE
NOVEMBER 1988
WESTERN PROCESSING SITE
434
-------
1988
Concentrations (ppb)
DRAFT
Source Landau Associates. 1991b
1990
Concentrations (ppb)
I
DRAFT
(Poor Quality Original)
Figure 10
CAOIUM WELLPOINT CONCENTRATION
CONTOUR MAPS FOR 1968 AND 1990
WESTERN PROCESSING SITE
TJ
3
52.
(Q
-------
Western Processing
1990 was about 4,000 ppb, considerably less than
1984 or 1988. The extent of the plume in 1990 is
similar to that in 1988, but the concentration
gradient is much smaller.
Well point concentration contour maps for
chloroform in shallow ground water in 1988 and
1990 are shown in Figure 11. In 1988, the
chloroform plume extended from the central
portion of the site through the southern portion.
Chloroform concentrations greater than 9,000 ppb
were observed in the center of the site. In 1990,
concentrations as high as 10,500 ppb were
observed in the center of the site. The plume in
the center of the site appears to have migrated
south. Concentrations as high as 12,000 ppb were
observed in the southeastern portion of the site in
1990 compared to 6,000 ppb in 1988. Chloroform
has a specific gravity of 1.49, and has a high
aqueous solubility (8,000 mg/1) compared to most
other indicator organics.
Figure 12 shows well point concentration maps for
toluene in 1988 and 1990. In 1988, the toluene
plume extended throughout the central portion of
the site with a maximum concentration of 12,000
ppb. No concentrations in excess of 1,000 ppb
were observed at the northern end of the site as
they had been in 1984. In 1990, considerably
higher concentrations were observed in the central
site with a maximum of 180,000 ppb. Toluene has
a specific gravity of 0.87 and lower aqueous
solubility (515 mg/1) than most indicator organics.
Well-point concentration contour maps for vinyl
chloride in 1988 and 1990 are shown in Figure 13.
In 1988, vinyl chloride contamination was evident
throughout the southern end of the site with a
maximum concentration of 19,000 ppb. Vinyl
chloride contamination is also evident in a smaller
area in the upper central area of the site. The
1990 well point concentration map indicates a
significant reduction in vinyl chloride contami-
nation in both plumes. The maximum 1990
concentration was 3,600 ppb.
Samples of extracted ground water in well point
cell headers have been analyzed for indicator
compounds since the extraction system began
operating. Plots of concentrations versus time are
presented in Figure 14 for total 1,2-DCE,
chloroform, methylene chloride, and TCE. Figure
14 presents data from Cells 5 and 6, which are
two of the most highly contaminated cells. The
plots show highly variable, but declining,
methylene chloride and TCE concentrations from
late 1988 to late 1990. Figure 15 presents well
point cell header concentrations for benzene and
toluene over time in Cells 5 and 6. In Cell 5, a
small declining trend in benzene concentration is
evident; however, no long-term trend is evident in
the toluene plot. In Cell 6, there is a significant
decline in toluene concentrations from October
1988 to July 1989, but no long-term trend is
evident.
The severity of cadmium concentration was
reduced somewhat from 1988 to 1990. Chromium
and nickel also showed reductions in
concentrations during the same period. Metals
with stable or increasing concentrations between
1988 and 1990 included aluminum, iron, lead, and
zinc.
Vinyl chloride contamination was reduced
considerably from 1988 to 1990. Other organics
that exhibited reductions in contamination included
1,1-DCA, 1,1-DCE, methylene chloride, and TCR
Benzene, chloroform, cis- and trans-l,2-DCE,
tetrachloroethane, toluene, 1,1-TCA showed stable
or increasing concentrations from 1988 to 1990.
SUMMARY OF REMEDIATION
The remedial measures implemented at the
Western Processing site are summarized as
follows:
• The three aquifer zones beneath the site
are contaminated with numerous metals
and organics. The shallow aquifer zone
is contaminated most extensively.
• A slurry wall and well point extraction
system were constructed at the site. The
extraction system includes 206 well points
in the shallow ground-water flow zone
each, designed to recover 1 gpm.
Contaminant extraction is enhanced by an
infiltration system which consists of
trenches parallel to the well point headers.
• The extraction and infiltration systems are
controlled to maintain an inward ground-
water flow gradient. Water elevation data
for the shallow ground-water zone in
1989 showed that an inward gradient was
maintained throughout the central and
436
-------
I
1968
Concentrations (ppb)
DRA
Source Landau Associates, 1991b
1990
Concentrations (ppb)
DRAFT
(Poor Quil«y Original)
Flguran
CHLOROFORM WELL POINT
CONCENTRATION CONTOUR MAPS
1988 AND 1990
WESTERN PBOCE3S1NO SITE
i
I
5
3
§
(Q
-------
1990
Concentrations (ppb)
I
•o
5
8
(Q
(Poor Quality Original)
Figure 12
TOLUENE WELL POINT
CONCENTRATION CONTOUR MAPS
1988 AND 1990
WESTERN PROCESSING SITE
00
1988
Concentrations (ppb)
ix>tnu) I andau Associates. 1991 b
-------
•£>•
UJ
*
I
1
1988
Concentrations (ppb)
DRA=T
Souice 1 andau Associates, 1991b
1990
Concentrations (ppb)
DRAFT
{Poor Quality original)
Figure 13
VINYL CHLORIDE WELL POINT
CONCENTRATION CONTOUR MAPS
1988 AND 1990
WESTERN PROCESSING SITE
I
HI
3
o
8
w
w.
(O
-------
Western Processing
Cell 5
Selected Organics
Cell 6
Selected Organics
Source: Landau Associates. 1991b
FlguraU
SEUECrEDORQANICS
CONCBITRAT1ONS
IN GROUND WATER EXTRACTED FROM
CELLS 5 AND 9
WESTERN PROCeSSINW SITE
440
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southern portions of the site, but there
was offsite ground-water migration at the
northern end of the site,
• Data collected from well points in 1990
indicate reduction in concentrations for
only a few contaminants. Plumes of most
metals and organics remained stable or
worsened between 1988 and 1990.
However, the data indicate that metals
and organics are being recovered by the
well point extraction system.
• The lack of significant reduction in levels
of pollution could be a result of additional
contaminants being flushed from the soil
by the infiltration system. The persistent
contamination may also be explained by
the relatively short time the extraction
system has been operating.
SUMMARY OF NAPL-RELATED
ISSUES
Nonaqueous phase liquids (NAPLs) have not yet
been recognized as part of the remediation
problem at the Western Processing Site. In 1988
site operators first observed a floating NAPL
(LNAPL) in two non-adjacent well points (U.S.
EPA, 1991). It is suggested that LNAPLs are
located above the water table and well screens.
Preliminary analysis of the LNAPL revealed that it
consisted of diesel motor oil and solvents (U.S.
EPA, 1991). High ground-water concentration of
several organic compounds relative to their
aqueous solubilities suggests that there may be
other NAPLs at the site.
«
Ground-water concentrations of toluene were not
particularly high when measured during the
remedial investigation in 1984. In 1990, however,
after two years of ground-water remediation,
concentrations as high as 180,000 ppb were
recorded. This is approximately 34 percent of the
aqueous solubility of toluene. High toluene
concentrations were not measured in the early
ground-water samples possibly because the moni-
toring wells were screened below the water table,
which was only a few feet below the ground
surface. When the water table was drawn down
by extraction from the well points, a floating layer
of toluene would be drawn down with it, and
higher concentrations might be measured. The
records of blended toluene concentrations for Cells
5 and 6, shown in Figure 15, show little or no
Western Processing
systematic decline over the two-year period since
the beginning of extraction. This behavior also
tends to suggest that nonaqueous toluene may be
present.
Other organics that are potentially present as
NAPLs are methylene chloride, TCE, 1,1,1-TCA,
and trans-l,2-DCE. Each of these compounds was
detected at ground-water concentrations of more
than 5 percent of solubility. TCE and 1,1,1-TCA
were found at 20 and 36 percent of solubility,
respectively. Trans-l,2-DCE has been detected at
65 percent of solubility. Such high concentrations
can be taken as strong indications that some, or
all, of these compounds may be present as dense
NAPLs (DNAPLs).
If DNAPLs were present in large quantities, the
implications for the success of ground-water
remediation would be serious. Because the
confining slurry wall is not underlain by a
continuous layer of low hydraulic conductivity, the
DNAPLs would not be prevented from sinking
into the finfe to medium sand aquifer at depths of
40 feet and below. However, if the quantities of
DNAPL are relatively small, the interbedding of
silts and clays in the shallow soils would tend to
spread the DNAPLs laterally. Under these
circumstances, a considerable volume of DNAPL
could be present at residual saturation without
penetrating to great depth.
441
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Western Processing
CeilS
Cell 6
- Mar* -M» mm
Source: Landau Associates, 1991b
Flgur* 15
BENZINE AND TOLUENE
CONCENTRATIONS IN GROUND WATER
EXTRACTED FROM CELLS S ANO 6
WESTERN PROCESSING SITE
442
VMl
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Western Processing
BIBLIOGRAPHY/REFERENCES
Canonic Environmental. June 17, 1988. Well
Point Extraction System Operations and
Maintenance Manual (O&M Manual).
CH2M HILL and Ecology and Environment.
December 17, 1984. Remedial Investigation,
Western Processing, Kent, Washington.
CH2M HILL and Ecology and Environment.
March 6, 1985. Feasibility Study for Subsurface
Cleanup, Western Processing, Kent, Washington.
Ecology and Environment. 1988 through 1990.
Operations Data for the Well Point Extraction
System.
Landau Associates, Inc. April 10, 1987.
Supplemental Feasibility Assessment for Flushing
Enhancement Slurry Wall, Western Processing,
Kent, Washington.
Landau Associates, Inc. November 1990.
Quarterly Interpretive Report: First Quarter
1989, Western Processing.
Landau Associates, Inc. February 13, 1991a.
Quarterly Interpretive Report: Fourth Quarter
1989. Western Processing.
Landau Associates, Inc. 199Ib. Draft graphics of
1990 data.
U.S. Environmental Protection Agency (U.S.
EPA). September 1985. Superfund Record of
Decision, Remedial Alternative Selection, Western
Processing Company, Inc., Kent, Washington.
U.S*. EPA. .June 20, 1991. Personal
communication with Mr. Bernard Zavalas,
Environmental Services Division.
443 * U.S. G.P.O.:1992-311-893:60677
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