United States       Office of Emergency and   Publication 9355.4-05A
           Environmental Protection   Remedial Response     PB92-963347
           Agency          Washington, DC 20460   February 1992

           Superfund
&EPA     Evaluation of Ground-Water
           Extraction Remedies:
           Phase II

           Volume 2
           Case Studies and Updates

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Evaluation of Ground-Water Extraction Remedies: Phase II
Volume 2 - Case Studies and Updates

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                             Publication 9355.4-05A
                                  February 1992
EVALUATION OF GROUND-WATER
EXTRACTION REMEDIES: PHASE II
              Volume 2
            Case Studies
   Office of Emergency and Remedial Response
     U. S. Environmental Protection Agency
            Washington, D.C.

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                              CONTENTS




                                                                  Page




 Introduction	v






 Site Name



 Amphenol Corporation	1



 Black & Decker	11



 Des Moines TCE  	23



 Du Font-Mobile	34



 Emerson Electric	44



 Fairchild Semiconductor  	45



 General Mills  	70



 GenRad Corporation	91



 Harris Corporation	105



 IBM-Dayton  	117



 IBM-San Jose	134



 Nichols Engineering  	171



 Olin Corporation	194



 Ponders Corner  	207



 Savannah River Site  	218



Site A	-236



 Utah Power & Light	245



Verona Well Field	257
                                   in

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                            CONTENTS
                            (Continued)

Site Name                                                      Page
Ville Mercier .	285

Mid-South Wood Products	286

Occidential Chemical	314

Sylvester/Gilson Road	341

Tyson's Dump  	374

Western Processing	414
                                 IV

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                           INTRODUCTION TO  VOLUME  2
This volume was prepared as part of the second
phase of a study to  evaluate the effectiveness of
the ground-water extraction systems being used to
remediate ground-water contamination  at hazard-
ous waste sites.

Volume 2 includes updates  of 17 of the 19 case
studies originally written in  the first phase of the
evaluation   and   published   by   the   U.S.
Environmental Protection Agency in  1989 (U.S.
EPA, 1989). For  two of the sites in the original
study, Case  Study 5 and Case Study 19, no new
information  was available, so no  update has  been
written. Also included in this volume are five new
case studies for sites not addressed in the original
evaluation.  Volume 1 is a  companion document
summarizing the information on the 24 sites in
both phases  of the study and presenting general
conclusions.

The 17  case-study   updates  presented  in   this
volume are intended  to be true updates rather than
replacements of the original  case studies.  Enough
information  is given  in the updates to  make them
stand-alone  documents, but  much of the detailed
background  information presented in the original
case studies  has not been repeated.  For fullest
understanding of the sites, both the original  and
the update should be read.

The case studies and updates are thought to repre-
sent  site  conditions   and   remedial   activities
accurately,  on  the  basis  of the site  documents
acquired in this project. The documents generally
included site investigation and remedial design re-
ports and periodic  (usually  quarterly  or annual)
monitoring reports for  the operating ground-water
remediation  systems.  The  site  documents were
generally furnished by regulatory agency personnel
associated  with  the  sites   or   by  the  parties
responsible   for   remediation.     In   addition,
comments on drafts of each of the case studies and
updates were solicited from  individuals known to
be familiar with the sites. Many helpful comments
were received and were incorporated in the stud-
ies. Still, there is no  way to ensure that significant
facts have not been overlooked.

The case  studies and updates  are  meant to be
informative  rather  than definitive.  They should
not be  considered authoritative source documents
within  the framework  of enforcement  actions or
site negotiations. Under no circumstances are they
to  be  interpreted   as  official  statements  of
regulatory findings for the sites concerned.

Various interpretations  and conclusions about site
characteristics and remedial progress are presented
in the case studies  and  updates.  Many  of the
interpretations are taken directly from  the site data
and monitoring  reports.  In such cases, the source
documents containing the interpretation are usually
referenced.  Conclusions  drawn by the authors of
the case studies generally are presented in the last
two sections of each study, which are summaries
of the remediation as a whole and of issues related
to  nonaqueous-   phase   liquid  contaminants
(NAPLs).  Particularly in the "Summary of NAPL-
Related Issues," the authors felt  free to present
tentative interpretations  that  are  more  or less
speculative.

               REFERENCE

U.  S. Environmental  Protection Agency  (U.S.
EPA).  October 1989.   Evaluation  of Ground-
water  Extraction Retnedies:  Volume  2.  Case
Studies 1-19. EPA 9355.4-03.
                                                                   203

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                                                  UPDATE OF CASE STUDY 1

                                                       Amphenol Corporation
                                                            Sidney, New York
Abstract

Monitoring  data collected  since 1988 show that  the extraction system has continued to
induce a zone of capture that encompasses the areas of known volatile organic compound
(VOC)  contamination.  Concentrations of VOCs  have decreased in  some shallow wells
indicating the ground-water quality in the shallow  aquifer continues to improve as a result
of remediation.  However, VOC concentrations have  stabilized at higher levels in some
deeper 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
1983
January 1987
Tetrachloroethylene
Trichloroethylene
Chloroform
Fluvial and glacial silt, sand, and gravel
2
260 gpm
9 acres
100 feet
Total VOCs 329 ppb

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                               CASE STUDY UPDATE
                           AMPHENOL CORPORATION

                          BACKGROUND OF THE PROBLEM
            INTRODUCTION

This  report discusses  events and  progress in
remediation at the Amphenol site from early 1989
through June 1990. It is an update of the original
case study, which  was based on data  collected
through the end of 1988 (U.S. EPA, 1989, Case
Study 1).

The Amphenol  site is  a manufacturing facility
located in the village of Sidney,  New York (see
Figure 1).  Electroplating wastewater impounded
in two waste treatment lagoons has contaminated
soil and  ground  water  at the site with volatile
organic compounds (VOCs).  This contamination
is a potential threat to the water  supply wells of
the village of Sidney.  The site is  administered by
the New York State Department of Environmental
Conservation.

The problem was  first discovered in 1983  when
monitoring required by the EPA under the RCRA
showed that soils  and  ground water beneath the
treatment lagoons  were contaminated by VOCs.
The waste lagoons were taken out of operation in
1985. The ground-water extraction system began
operation in January 1987 and has been operated
almost continuously since startup.

The area is underlain by 100 to 200 feet of fluvial
and  glaciofluvial  deposits of  unconsolidated silt,
sand, and gravel.   Within  these  unconsolidated
sediments are  two transmissive zones referred to
as   the  shallow   and  deep  aquifer  zones,
respectively.  The unconsolidated deposits are
underlain by flat-lying shale bedrock.

The direction of ground-water flow is variable. It
is influenced by  the  water level  in the nearby
Susquehanna River, the surface topography, and
ground-water  pumping  from both  the  Sidney
production wells and the extraction system.   The
most common flow pattern, which occurs when the
river stage is high, is for ground water to flow to
the southeast and southwest away from the  river.
When this occurs, ground water in  the area of the
two  lagoons diverges  and  flows  to  both the
southwest  and  southeast.   When  ground-water
levels are high relative to the river stage, ground
water flows to the northwest.

The   primary  contaminants   of  concern  are
trichloroethylene   (TCE),   chloroform,  tetra-
chloroethylene, and other  VOCs.  The area of
greatest contamination is immediately southwest of
the two lagoons in the shallow aquifer zone.  The
shallow plume is divided  into  two  lobes,  one
extending west from  the lagoons parallel  to the
river and the other extending to the southeast.  The
deep plume is southeast of the lagoons and appears
to turn to the east at its southern limit in response
to ground-water pumping  by  the  water supply
wells of the village of Sidney.

           UPDATE ON SITE
          CHARACTERISTICS

There have been no important changes in the site
administration,  or in the  understanding of the
hydrogeologic setting or waste characteristics since
the time of the original case study.

             REMEDIATION

       Design and Operational
       Features of  Remediation
                 System

The objectives of remediation are to reduce total
VOC concentrations   to less  than  5 ppb in the
subsurface and to prevent  contaminated ground
water from reaching the  Sidney  water supply
wells.  The remediation  system,  as shown in
Figure 2, consists of two extraction wells—RW-1,
which  is  screened  from   100 to  120 feet  and
designed to remediate the deep aquifer zone, and
RW-2, which is  25  feet deep and designed to
remediate the shallow zone.  Both wells are close
to the lagoons.   Wells RW-1  and  RW-2 are
typically  pumped  at  approximately  140 and
60 gpm, respectively.

The extraction system  has not been modified since
the end of 1988.  However,  a second production
well for the village of Sidney, one located farther

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                                                                Amphenol Corporation
                        i Former
                  Waste Lagoons
                                                     1000   2000    3000    4000   5000
SQUKW: USGS.1082. SidmyQtud«ngiB,7J
Minute Topographic Swmt
1000     0     2000

     scale in fast
Figur* 1
SITE LOCATION MAP
AMPHENOL SITE

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                                                                                                 nol Ftocomy Wrt
                                                                                           PfttMiMtorMnl (Of«p.
                                                                                          PtnafMtwrNMffDtfpMid
                                              Sidney Sewag*
                                              Treatment Ptant
Source ERM. 1990s


No
-------
                                                                    Amphenol Corporation
 northeast of the lagoons than Well No. 1, was put
 into operation on November 30, 1989.  Although
 Well  No. 1  is   operational  and  is  pumped
 intermittently  for  maintenance purposes,  Sidney
 has generally used only Well No. 2 for its water
 supply since November 1989 (Woodyshek, 1991).
 Since  1989,  Well  No. 2  has   been operated
 intermittently  at  800 gpm,  whereas  prior  to
 November   1989,   Well  No. 1   was  operated
 continuously at 400 gpm. The change in pumping
 has caused a slight increase in the zone of capture
 of the water supply wells and a slight decrease in
 the zone of capture of the recovery wells.

  EVALUATION OF PERFORMANCE

 The two extraction wells appear  to continue to
 capture   the  contaminant  plume  and  prevent
 contamination  from  reaching  the  water  supply
 wells,  despite   the  addition  of  Well  No. 2.
 Contaminant  concentrations in wells 7-D and
 12-D, the deep wells that are closest to the water
 supply wells, were found to be below detection
 limits when these  wells were sampled in March
 1990.  Since sampling began  in the mid-1980s,
 water supply well No. 1 has consistently contained
 1 to 3 ppb of TCE and other volatiles and has not
 shown any  decrease in concentrations in response
 to remediation. Contaminant concentrations have
 been consistently  below detection  limits  in Well
 No. 2.  Despite the persistence of contamination in
 Well No. 1, ground-water contour data suggest that
 the  remedial   objective   of  preventing   the
 contaminant plume  from migrating to the  water
 supply wells has been met since the end of 1988.

 Figures 3, 4, and 5 are time series  graphs of total
 VOC concentrations in  wells 1-S,  17-S, and 1-D,
 respectively. Wells 1-S and 1-D are paired wells
 located  immediately  south  of the  west lagoon,
 while well 17-S is located immediately west of the
 west lagoon. All three wells have been  among the
 most contaminated wells at the site historically.
 Figures 3  and 4,   both  show  that total  VOC
 concentrations   have   continued   to   decrease
 gradually since the end of 1988,  indicating that
 ground-water quality in the shallow aquifer zone
 continues to improve as a result of remediation.

Figure 5  shows that total VOC concentrations  in
deep well 1-D were stable from late 1988 through
mid-1990.    These  results  suggest  that  the
remediation system has not significantly improved
 the water quality in the part of the deep aquifer
 zone adjacent to the deep extraction well since the
 end of 1988.

 Table 1  shows  a  comparison  of  total  VOC
 concentrations in 8 monitoring wells from 1986
 through June  1990.   The concentration of total
 VOCs  has  decreased substantially  in  all  the
 contaminated shallow wells listed in Table 1 since
 1986.   However,  the  concentrations have been
 essentially stable in deep well 18-D  since 1986.
 The overall decrease in VOC concentrations at the
 site are likely to be a result of remedial activities,
 including the drainage  of the wastewater lagoons
 in mid-1985, the removal of contaminated soils in
 late 1986, and the startup of the extraction system
 in January, 1987.

    SUMMARY OF REMEDIATION

 The monitoring  data collected since  1988 show
 that the extraction system has continued  to induce
 a zone of capture  that encompasses the  areas of
 known contamination by VOCs and protects water
 supply wells,  despite  changes  in  water supply
 pumping.  Continued gradual improvement in the
 water quality of the shallow  aquifer zone is also
 evident. Monitoring data show that concentrations
 have stabilized in some deep wells, indicating that
 the extraction  system may not  be improving
 ground-water quality in the deep aquifer zone in
 some areas.

   SUMMARY OF NAPL-RELATED
                  ISSUES

 The presence  of contaminants  in  the  form  of
 nonaqueous phase liquids (NAPLs) has  not been
 suggested in any of the information reviewed for
 the Amphenol  site.    Although  the  chlorinated
 organic solvents that are the primary contaminants
 of concern have the potential  to remain in  the
 aquifer as a dense nonaqueous phase, the historical
 means  of  contaminant deposition,  the  source
removal actions at the site,  and  the  observed
 distribution of ground-water contamination suggest
 that NAPLs, if present at all, probably  do not exist
 in large quantities.

The VOCs  from  the Amphenol  plant  were
 apparently conveyed to the storage lagoons as a
constituent of the plant's process waste water.  It
 is not known to what extent the VOCs were

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-4
Tabtel
COMPARISON OF TOTAL VOC CONCENTRATIONS



1-S
1-D
3-S
5-S
15-S
17-S
18-S
18-D
1*8* THROUGH JUNE 19*
.MM
M**mmm
91
60
5
ND
8
105
*
4
MBteHi
179
154
172
ND
100
161
•«
17
M*«
119
102
72
ND
50
132
77
9
It87
W*mm
47
53
*
ND
2
50
11
<1
M«ta=,
61
74
*
ND
22
155
20
16
MM*
54
64
1
ND
12
95
15
8
1988
Mb—
38
20
ND
ND
ND
36
ND
6
MotMB
50
47
1
ND
1
64
16
12
Mm
45
29
<1
ND
<1
49
8
9
1989
m.^.,.
23
27
ND
ND
ND
15
10
8
ItafaM*
39
32
ND
ND
1
38
11
13
MtWB
29
30
ND
ND
<1
26
11
10
19W
MttM
22
24
ND
ND
ND
24
9
12
«1»M
17
25
ND
ND
1
17
NS
7
Altered after ERM, 1990s
Notes:
ND =5 none detected
NS = not sampled
* = only one analysis available
(D

O

O
o

•5
o

S

o

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300
100
    1983
                                                                                             1991
                                                                                                           •o
                                                                                                            (D
 O
 O
n
                                                         Figure 3
                                                         HISTORY OF TOTAL VOC CONCENTRATION IN MONITORING
                                                         WELL 1-S, SHALLOW AQUIFER ZONE
                                                         AMPHENOL SITE

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oo
                    400
                    300  -
                    200
                    100  -
                                                            1
                         1984
1985
1986
1987
1988
1989
                                                                                                       1990
1991
                                                                             Figure 4
                                                                             HISTORY OF TOTAL VOC CONCENTRATION IN MONITORING
                                                                             WELL 17-S, SHALLOW AQUIFER ZONE
                                                                             AMPHENOL SITE
                                                                                                                                  13
                                                                                                                                  3"
                                                                                                                                  0)
Q
o
-<
T3
O
S
•**•
o

-------
SO
                        200
                        100 —
                  o

                  §
                                                    •§
                                                    Q
                                                    c
                            1964
  I


1985
1988
1989
  I


1990
1991
                                                                                                                                              T3
2.

o
                                                                                                                                              •
                                                                                                                                              o

                                                                                                                                              I
                                                                                                                                              o

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 dissolved in this waste.  The lagoons were lined
 with asphalt, which later became coated with metal
 hydroxide  sludge due  to precipitation  from the
 metal plating waste. When the lagoons were taken
 out of service, it was found that the asphalt in the
 southern portion of the eastern lagoon had partially
 deteriorated.  This could be the result of contact
 with chlorinated solvents, but  there is  no direct
 evidence of this.

 An  extensive  program  of soil  sampling  was
 conducted  in the upper 5 to 6 feet of  the  soils
 beneath  the lagoon.   In most areas  the VOC
 concentrations in the soils were less than 25 ppm.
 However,  in the southern portion  of   the  east
 lagoon, where  the asphalt  lining  was damaged,
 field screening  with a flame ionization  detector
 showed  VOC   concentrations  of  more  than
 1,000 ppm in three locations. When samples taken
 from   these hot  spots  were  analyzed  in  the
 laboratory,  the highest VOC reading was  32 ppm.
 If the  soils  were  contaminated  with   NAPLs,
 concentrations   on  the  order   of  hundreds or
 thousands of ppm  would be expected.   Because
 soil concentrations at these levels were detected by
 field  screening in  only 3 samples  out  of  the
 approximately   200 samples  taken,  it   can  be
 concluded that NAPL contamination, if present, is
 not extensive. The levels of VOC contamination
 detected in ground water have been generally less
 than 300 ppb in the upper aquifer zone and less
 than 160 ppb in the lower zone.  These levels are
 below  the aqueous solubility of the major organic
 constituents present by  a factor of 1,000  or more
 and would not normally raise  suspicion of the
 presence of NAPLs.

       UPDATE BIBLIOGRAPHY/
             REFERENCES

 Environmental   Resources  Management   (ERM).
 February 20, 1990a. 1989 Annual Summary of the
 RCRA Ground-Water Monitoring. Letter to Henry
 Mitchell of Amphenol Corp.

 ERM.  February 20, 1990b.   Letter to Henry
Mitchell    of   Amphenol   Corp.,   discussing
monitoring  in the fourth quarter of 1989.

ERM. June 12,  1990c. Letter to Henry Mitchell of
Amphenol Corp., discussing monitoring in the first
quarter of 1990.
                Amphenol Corporation

ERM.  September  20,  1990d.   Letter  to  Henry
Mitchell   of   Amphenol  Corp.,   discussing
monitoring in the second quarter of 1990.

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.

Woodyshek,  John.   January 3, 1991.  Personal
communication with  John  Woodyshek, Village of
Sidney engineer.
                                                  10

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                                                   UPDATE OF CASE STUDY 2

                                                             Black and Decker
                                                          Brockport, New York
Abstract

The extraction system, which pumps from an enhanced fracture zone, has continued to meet
the objective of plume containment since the end of 1988.  Some contaminated ground
water from formerly downgradient areas also  continues to be captured.  Concentrations in
areas downgradient of and lateral to the fracture zone have generally decreased since 1988.
Trends are stable  or decreasing in upgradient areas.  Concentrations of 5 percent of the
aqueous solubility  of TCE persist in the most contaminated well in the bedrock.
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
May 1988
Trichloroethylene
1,1,1 -Trichloroethane
1 ,2-Dichloroethylene
Vinyl Chloride
Glacial till over fractured sandstone
1
10 - 15 gpm
11 acres
40 feet
Trichloroethylene 86,000 ppb
                                       11

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                                CASE STUDY UPDATE
                                   BLACK & DECKER

                           BACKGROUND OF THE PROBLEM
             INTRODUCTION

 This  report discusses  events and progress at the
 Black & Decker site from the start of remediation
 in 1988 through early  1991. It is an update of the
 original  case  study,  which  was  based  on
 concentration data through November 1988 (U.S.
 EPA, 1989, Case Study 2).

 The Black & Decker site is  a,former appliance
 manufacturing plant in Brockport, New York (see
 Figure 1). The ground water over much of the site
 has   been   contaminated   by  volatile  organic
 compounds (VOCs) originating from metal-plating
 wastewater, sludge, and other sources. The site is
 under  the  jurisdiction of the U.S.  EPA under
 RCRA and of the New York State Department of
 Environmental Conservation (NYSDEC).

 The problem was discovered in 1985 when^ground
 water  in the  area  around  the  plant's waste
 management facility was sampled and found to be
 contaminated with VOCs. Operation of the waste
 management facility was terminated  in 1986 and
 1987.    A  pre-fracturing  pumping  test  was
 conducted in March 1987, using a single extraction
 well,  which proved to be  ineffective, because it
 failed to  capture ground water from a broad  area
 of the fractured bedrock aquifer.  In May 1987, an
 artificial  fracture  zone designed to  enhance the
 effectiveness of  the  remediation  system  was
 created using explosives. The  present remediation
 system,  which  consists  of one extraction  well
 centered  within the artificial  fracture zone,  was
 operated intermittently from  May to October 1988
 and virtually continuously from  October  1988 to
 early 1991.

 There are three geologic units that  underlie the
 Black & Decker site near the surface. The first is
 a 5- to 20-foot-thick  deposit of unconsolidated
 glacial till that thickens  to the  north across the
site.  This till is underlain by a 50-foot-thick  unit
of fractured sandstone,  known  as  the  Medina
sandstone.  Underlying the  Medina sandstone is
the Queenston shale, which is several hundred feet
thick at the Black & Decker site. There  are  two
 aquifers at the site-the overburden aquifer within
 the unconsolidated  till and the bedrock aquifer
 within the fractured sandstone.  Both aquifers are
 contaminated with VOCs.  The horizontal direction
 of ground water flow within both aquifers is to the
 north-northwest.     The  vertical  gradient  was
 downward across most of the site in 1990.

 The contaminants of concern are trichloroethylene
 (TCE),  1,2-dichloroethylene  (1,2-DCE),  1,1,1-
 trichloroethane (TCA), and vinyl chloride.  Most
 of the contaminant mass is within the upper half of
 the fractured bedrock aquifer.  The contamination
 appears to have originated from the  wastewater
 lagoons and the sludge-drying  pits of the waste
 management area on the  southeast border of the
 site.  Some leakage from pipes may  also have
 occurred.

            UPDATE ON SITE
           CHARACTERISTICS

 The  information   on   the   history,   geology,
 hydrogeology,    waste   characteristics,   and
 administration of the site  reported in the original
 case study is still current.  Additional information
 on  site geology  has  been  made  available  by
 NYSDEC.  It has been reported that the bedding
planes in the Medina sandstone dip 1 to 3 degrees
 to the  south, away  from  the artificially induced
fracture zone.   Complete  information on  site
characteristics can be found in the original case
study.

             REMEDIATION

The extraction system  consists  of one  extraction
well that pumps ground water  from a 300-foot-
long artificial fracture zone  created to enhance
flow within the fractured bedrock and increase the
efficiency  of remediation.  The fracture zone  is
several feet  wide  and  extends  approximately 25
feet into  the fractured sandstone bedrock.   The
extracted  water is  treated with an air stripper and
then discharged to the Barge Canal that borders
                                              12

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                                                                           Black & Decker
                       **/'    'A    V/K ^
                         V".   '       ,M   ,   •  /
                                                      1.'	j.	_^ ••	gfc'g v +ff •»  • ••••   •   ; i L>-•'^••^

                                                       **"*  'a~ ^gtfyBOTgi^ *E? V^J'T-""' "•'
                                                      ••—i—•—s    IM •.••jjj'si* ifSfj^k--*t-»  -j<.«"
                                               New York State
                                                 Barge Canal
                                                        ^r-^-^-Ti
Source: USGS. 1978. Brackpqrt Qu«rtngl», 7.5
Minuta Topographic Series.-
   1000   2000
        ••

Scale in Fwt
                                               13
(Poor Quality Original)

                   Figure 1
                   SITE LOCATION MAP
                   BUCK4DECKEPS.*t
                   BROCKPORT. NEW

-------
                                                                                Black & Decker
 the site on the north.  The objective of remediation
 is  not to clean up both aquifers  to health-based
 levels as erroneously stated in the original  case
 study. As stated by the site operators, the primary
 objectives of the ground-water extraction system
 are (1)  to  prevent  the  plume  of VOCs  from
 migrating  further, and (2) to capture VOCs that
 have migrated  downgradient  of  the  artificially
 induced   fracture  zone.      (General  Electric
 Company, 1991).  The  monitoring well system
 consists   of  several wells   installed  in   the
 overburden aquifer and a  series of individual or
 clustered wells  installed in the bedrock aquifer.
 The monitoring system is sampled quarterly.

 No substantial changes have been  made in  the
 infrastructure of the  remediation  or monitoring
 systems  since the end of  1988.   The extraction
 system  was  operated nearly  continuously  from
 1989 through early 1991.  The average pumping
 rate during  periods  of  operation  in  1990  was
 approximately 12.4 gpm (Dunn Geosciences Corp.,
 1991). The system was shut down from February
 27  to March 24, 1989, from December 15, 1989 to
 January 31, 1990, and from December 30, 1990 to
 January 10, 1991-in each case  due to mechanical
 or maintenance problems.

 The extraction system has  continued to capture
 contaminated  ground  water  from  both  the
 overburden and bedrock aquifers within the plant
 boundaries since  the end of 1988.   The extent of
 the capture zone  within the overburden aquifer is
 difficult to assess, however, because of the limited
 number of wells installed in the overburden aquifer
 in  the  vicinity  of  the  fracture  zone.    The
 potentiometric surface within the shallow bedrock
 aquifer in August  1990 is shown in Figure 2.
 Figure 2 shows  that the  capture zone within the
 shallow bedrock aquifer extended laterally to the
 east of the fracture zone approximately 200 feet in
 late 1990. Because of insufficient water-level data
 on the northeast boundary of the site, it is difficult
 to determine whether the ground water reported to
 flow northeast from the waste management area is
 being captured by the  current extraction system.

In general, the extraction  system  appears  to be
effective   in  preventing   the   continued  offsite
migration of contamination.   The  capture zone
created by the extraction system is most extensive
in the intermediate and  deep  wells within  the
bedrock aquifer.  This indicates  that bedrock
 fractures are interconnected at the deepest intervals
 of the monitoring network and  suggests that  the
 capture zone extends vertically below the deepest
 wells of the monitoring system.

 The  operation  of the extraction  system  since
 October  1988  has  resulted  in a  decrease in
 contamination   in  monitoring  wells   located
 downgradient of and lateral to the  fracture  zone.
 Figures 3  and  4 are  time-series  plots  of  the
 concentration  of TCE in overburden wells GFJB-
 18S and GEB-23S, respectively, from early 1987
 to late  1990.  These two  wells  were designed to
 monitor ground water quality in the overburden
 aquifer  along  the   centerline   of  the  plume
 upgradient of the fracture zone. The concentration
 of TCE in well  GEB-18S, the most contaminated
 overburden well,  has generally decreased  since
 1987~from 38,000 ppb in January 1987 to 4,300
 ppb in November  1990.   The reason for  the
 midyear peaks observed in 1988, 1989, and 1990
 is unknown.  The bedrock well, GEB-18B, that is
 paired with GEB-18S  is one of the  few  wells in
 which the ^ncentration of TCE has not decreased
 substantially.  Since 1987 TCE  concentrations in
 GEB-18B  have decreased from 20,000  ppb in
 January 1987  to 12,000 ppb in  November 1990,
 with fluctuations ranging  between  8,600  ppb to
 35,000 ppb.

 Figure 4 shows  that the concentration of TCE in
 GEB-23S  fluctuated between  0  and 7 ppb  from
 late 1987 to late 1990 but peaked to 25 ppb in  the
 fourth  quarter of  1988.    The  reason  for  the
 concentration  peak in late  1988 is not known.
 Most of the contamination at this location is in  the
 bedrock, as shown by concentrations in GEB-23B
 (see Figure 5).

 Figure 5 shows  the  time-series trend  of  TCE
 concentration in bedrock well GEB-23B since  the
 beginning of 1987.  TCE concentrations increased
 from 62,000 in mid-1987  to 86,000  ppb in  mid-
 1988, followed by a  decrease through early 1989.
 The concentrations appear to have stabilized after
 early 1989.

The  concentration of TCE in  well GEB-30BI,
 located north of the fracture zone, from early  1987
 through late  1989 is shown in Figure 6.   This
 figure   shows   an  abrupt  decrease  in   TCE
concentration from 280 ppb in October 1987 to 59
                                                 14

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    (Poor Quality Original)
Figure 2

POTENTIOMETRIC SURFACE IN THE SHALLOW

BEDROCK AQUIFER, AUGUST 21,1991

BLACK & DECKER SITE
CO
£f
O
*•

*

O
(B
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44)000
30000   ~
20000  -
10000  -
       196?
1988
  I
1969
YEAR
1990
1991
                                                                                   Figure 3
                                                                                   CONCENTRATION OF TCE IN
                                                                                   MONITORING WELL GEB-18S
                                                                                   BLACK & DECKER SITE
CD
i"
o
                                                                                  O
                                                                                  O
                                                                                  o

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1987
                      1988
                                                                   1990
1991
                                            YEAR
                                                                              Figure 4

                                                                              CONCENTRATION OF TCE IN

                                                                              MONITORING WELL GEB-23S

                                                                              BLACK & DECKER SITE
CO

0)
O
pr

fi»

a

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DC
                   90000
                          1987
1991
                                                                                                    Figures

                                                                                                    CONCENTRATION OF TCE IN

                                                                                                    MONITORING WELL GE&-23B

                                                                                                    BLACK (DECKER SITE
OJ

0
O
                 O
                 (D
                 O

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1967
                       1988
                                                                    1990
1991
                                             YEAR
                                                                             Figure 6
                                                                             CONCENTRATION OF TCE IN
                                                                             MONITORING WELL GEB-30BJ
                                                                             BUCK t DECKER SITE
                                                                                                           09
                                                                                                           tt
                                                                                                           O
               I

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                                                                              Black & Decker
 ppb in December 1987, followed by a  gradual
 decrease in TCE concentration to  less than 1 ppb
 in November 1990. The concentration of TCE in
 GEB-30BI in October  1986  was 39 ppb.   The
 reason for the high TCE concentrations in 1987 is
 not  known.  The substantial  reduction  of TCE
 concentrations in GEB-30 BI  is evidence  that the
 extraction system has drawn  back ground water
 from the formerly  downgradient  area  near this
 well. The water levels shown in Figure 2 support
 this  conclusion.

 Figure 7 shows the concentration  of TCE in the
 recovery well RW-1A from October  1987  through
 the end of 1989.   These data  show  a substantial
 decrease in  the   concentration  of TCE  from
 October  1987 through November  1988, followed
 by  a  period  of stable or  slightly decreasing
 concentration through November 1989.

 The  concentration of VOCs in the ground-water
 monitoring  system  in general has decreased since
 ground-water extraction  began in  October 1988.
 An increase in the concentration of VOCs  in mid-
 1987,  at the time  of  artificial fracturing,  was
 observed in several  wells  downgradient  of and
 lateral to the fracture zone.

    SUMMARY OF REMEDIATION

 In the  initial case study, it  was reported that the
 remediation system captured contaminated ground
 water effectively through the end of 1988.  Recent
 data  demonstrate that the remediation system has
 continued to capture the ground water from most
 or all  contaminated areas and,  therefore,  has
 continued to achieve its  stated objective of plume
 containment. Concentration  data collected through
 1990 show that the concentration of VOCs has
 decreased or remained stable since 1987  in  most
 of the wells in the monitoring system, indicating
 that  the  remediation  system   is  also  removing
 contaminants from  the ground water.  However,
 for   site  operators  to  terminate  ground-water
 extraction,  they  must  be  in  compliance  with
 health-based standards as listed in the  original case
 study and in the post-closure  permit for  the site
 (NYSDEC,  1991b).  Concentrations of VOCs that
are   considerably  greater  than  these   target
concentrations  persist over much of the  site,
particularly  along the centerline of the plume and
in the bedrock.
    SUMMARY OF NAPL-RELATED
                  ISSUES

 It is not known whether a  residual source of
 ground water contamination in the form of a dense
 nonaqueous phase liquid (DNAPL)  is present at
 the  Black  &  Decker  site.    Persistent  high
 concentrations of contaminants despite  efficient
 extraction are one indication of DNAPLs.   Data
 collected through  the end of 1990 generally show
 a  significant decrease  in VOC  concentrations.
 Although several  wells show  a stable or slightly
 declining trend in concentrations during 1989 and
 1990, this type of asymptotic decline is typical of
 the  concentration history  of  many  non-DNAPL
 sites where ground-water extraction has been in
 progress  for several  years.   The  concentration
 trends to date at the Black & Decker site are not
 strongly  indicative of  DNAPL  contamination.
 However, the concentration of TCE in GEB-23B
 in excess of 85,000 ppb in 1988  (approximately
 8.5 percent of  aqueous solubility) suggests  that
 DNAPLS may be present in some areas of the site.
An increase in the concentration of contaminants
following  periods without  ground-water pumping
is another characteristic of sites contaminated with
NAPLs.  Increases in the concentrations of select
contaminants were observed in wells GEB-29BD,
GEB-30BD, GEB-32BS, and 32BD from February
to May 1989.  These increases may be related to
the shutdown of  the remediation  system from
February 27  to   March 27,    1989;   however,
additional concentration data following subsequent
shutdowns are needed to verify this relationship.

The presence of the artificial fracture zone may be
a problem if DNAPLs are present at the site. The
fact that the hydraulic capture is extensive  in the
bedrock, even  at  the  deepest  intervals of  the
monitoring network,  suggests  that the zone  of
good  interconnection between fractures  extends
below  the deeper wells in the sandstone bedrock.
DNAPLs of VOCs are generally 30 to 80 percent
more dense than water.  As a result, they have a
strong  tendency to sink in  the subsurface and are
able to flow downward against hydraulic gradients.
The creation of an artificial  fracture zone may
favor downward migration of DNAPLs, if present,
below the vertical extent of ground-water capture,
and thus establish a deep residual of contamination
that  cannot be  remediated   using  the  present
extraction  system.  This is primarily  true in  the
case of any DNAPLs that may be near the
                                               20
                     SffH   1*0(077

-------
                      Black & Decker
                                   z
                                   Ul
                                   a >•
21

-------
                                                                           Black & Decker
 artificial fractere zone,  where downward  gravity
 flow might be enhanced by the artificial fracturing.
 Because the bedrock dips 1 to 3 degrees to the
 south  away from  the  fracture  zone,  however,
 potential DNAPL sources near the existing plume
 center are expected to  flow  to the south.  The
 fracture density and  structure of the underlying
 Queenston shale has not been reported;  therefore,
 it is difficult to predict the fate of any potential
 DNAPJLs should they migrate below the sandstone,

       UPDATE  BIBLIOGRAPHY/
             REFERENCES

 Dunn Geosciences  Corp,  March 1988.  RCRA
 Annual Ground-Water  Monitoring Report-1987
 Black & Decker (U.S.), Inc.,  Housewares Group
 Brockport, New York.

 Dunn Geosciences  Corp,  March 1989.  RCRA
 Annual Ground-Water  Monitoring Report-1988
 Former Black & Decker Facility Brockport,  New
 York.

 Dunn Geosciences  Corp.  March 1990.  RCRA
 Annual Ground-Water  Monitoring Report—1989
 Former Black & Decker Facility Brockport,  New
 York.

 Dunn Geosciences  Corp.  March 1991.  RCRA
 Annual  Ground-Water  Monitoring Report--1990
 Former Black & Decker Facility Brockport,  New
 York.

 General Electric Company. May 29, 1991. Letter
 from   Michael   lanniello,   Remedial   Project
 Engineer, GE Corporate Environmental Programs.

 New  York State Department  of  Environmental
 Conservation (NYSDEC). May 13, 1991a. Letter
 from Lawrence M. Thomas,  Senior Engineering
 Geologist, Bureau  of Hazardous Waste Facility
Management.

NYSDEC.    June  11,   1991b.     Personal
Communication with Lawrence M. Thomas, Senior
Engineering  Geologist,  Bureau   of  Hazardous
Waste Facility Management.

U.S.  Environmental  Protection  Agency (U.S.
EPA).   October 1989.  Evaluation of Ground-
 Water  Extraction Remedies:    Volume  2.   Case
Studies 1-19, Interim Final  EPA/9355.4-03.
                                             22

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                                                   UPDATE OF CASE STUDY 3
                                                               Des Moines TCE
                                                              Des Moines, Iowa
Abstract

Since startup in December 1987, the extraction system has continued to create a hydraulic
zone of capture in the areas of known ground-water contamination.  Concentrations of
VOCs in ground water have declined as a result of remediation.  However, after initial
sharp decreases in VOC levels at system startup, concentrations appear to have stabilized or
have decreased at a slow rate in most wells and in  the influent to the air stripper.  From
December 1987 through the  end of  1989, the extraction system removed approximately
1,300 gallons of TCE from ground water.
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
1974
December 1987
Trichloroethylene
Trans- 1 ,2-dichloroethylene
Vinyl chloride
Silt, sand, clay, and gravel
7
1,300 gpm
130 acres
50 feet
Trichloroethylene 8,467 ppb
                                       23

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                                CASE STUDY UPDATE
                                    DES  MOINES TCE

                           BACKGROUND OF THE PROBLEM
             INTRODUCTION

 This  report  describes  events and  progress  in
 remediation at the Des Moines TCE site from late
 1988 to early 1990.  It is an update of the original
 case study, which was based on concentration data
 through September 1988  (U.S. EPA,  1989, Case
 Study 3).

 The Des  Moines TCE site  is located in  south
 central Des Moines,  Iowa.  The  site  is near the
 Des Moines Water Works (DMWW), the Raccoon
 River, and a  manufacturing facility belonging  to
 the  DICO Corporation  (see  Figure 1).    The
 primary   contaminants   are   volatile  organic
 compounds (VOCs).  The site is  administered by
 the EPA under the Superfund program.

 The contamination problem was first discovered in
 1974, when contaminants were  detected  in  the
 ground   water  pumped   by   the   DMWW.
 Remediation by ground-water extraction began on
 December 17,  1987,  using a  system of seven
 extraction  wells on the DICO property.

 The alluvial geology  consists of 40 to 60 feet  of
 unconsolidated silt, clay, sand and  gravel overlying
 consolidated shale bedrock. The top 10 feet of the
 alluvial materials consist of silt and clay overbank
 deposits. A sandy aquifer extends from a depth  of
 10 feet to  the top of bedrock.  Water levels in the
 aquifer  range  from  10  to  25 feet  below  land
 surface.  The  predominant  direction  of ground-
 water flow on the DICO property  was  to the west
 prior to operation of  the extraction system.  This
 flow pattern was the  result of long-term pumping
 from the north part of the infiltration gallery oper-
 ated by  the DMWW  (see Figure 1). This part  of
 the gallery was  removed from service in  1984
 because of ground-water contamination.

The  contaminants  of concern at  the site are
 trichloroethylene (TCE), trans-l,2-dichloroethylene
 (Trans-1,2-DCE), and vinyl chloride.   .The main
source of  volatile organics was initially reported
by DICO  to be leaching  from the contaminated
soils west  of the DICO plant.  In  past years, 100
to 200 gallons  of  waste  solvent  sludge  were
applied to these soils for dust control.  However,
the EPA suspects that there are other contaminant
sources and has initiated further investigations to
identify them.

           UPDATE ON SITE
          CHARACTERISTICS

The consultant to DICO has changed names from
AWARE,  Inc., to Eckenfelder, Inc.,  since the
initial case study was written.  The site continues
to be administered by EPA Region VII.

The  original   (Operable   Unit  1)   remedial
investigation indicated that the bedrock surface is
uneven and slopes to the northeast away from the
river at the site (U.S. EPA,  1985).  This bedrock
slope may influence the direction of flow of any
dense nonaqueous phase liquids (DNAPLs) that
may be present.

DNAPLs are suspected because of the reported use
of large quantities of potentially DNAPL-forming
chlorinated solvents  at  the  site.    A  remedial
investigation concentrating on source identification
and control  (Operable  Unit 2)  is  currently in
progress.   Extensive drilling and sampling in the
bedrock  have  been  completed  but  no DNAPLs
have been found in the bedrock as  of June  1991.
Another  remedial  investigation  designed  to
characterize the contamination in the north plume,
thought to be the result  of offsite sources, is also
in progress (Operable Unit 3).   Soil gas studies
have been completed and several new monitoring
wells and soil borings  have been installed and
sampled  as  a part of  the  Operable Unit 3
investigation.

Ongoing investigations seek  to identify all of the
contamination sources of the main DICO  plume
and of (he north plume (Operable Units 2 and 3).
Two large degreasing vats within the main DICO
production building have been identified and are
being  investigated as possible  sources of  VOC
contamination.     Other  potential   sources  of
contamination  on  the DICO property  identified
since the initial case study include:  (1) above-
                                              24

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                                          Des Moines TCE
.^Sl^^^^^iM _ ^%.7^. f
Operable Unit 3
  Study Area

                                         -
                           .v*w JP.  ^-* -:: * *   '• ••• &  •
                           H^C/ifftl>riL^J
                           pi^:-|^4r||4^  J
1-" H: l^r/'/ ..t ?>('* '   ef «4s !r s  Is"!   - "•

DM Moinas Quadrangla, 7.5 Minut* Topographic S»'*»


   /B^^.«. J^^..ltA.. M>.Jt	i	_•%
              .-
         Source: USGS. 1976. DM Moi
                       (Poor Quality Original)
                                        FJgurtl
                                        SITE LOCATION MAP
                                        QES MOINES TCE S>1
                                        DES MOINES.
                  25
                                      sfft

-------
                                                                                    Des Moines TCE
 ground solvent storage tanks southeast of the main
 DICO  building;  (2) an area  near WeU ERW-7
 where used drums  of solvent  were cleaned; and
 (3) an area of construction debris  south of the
 main  building   (Eckenfelder,  1989).     These
 potential sources are shown in Figure 2.

 Some potential sources  of contamination outside
 the DICO property  have also  been identified, the
 most   important   of  which   is   the   VOC
 contamination  that  has  migrated  towards  the
 extraction wells from the campus  of Des Moines
 Tech, north of the DICO property.

 The main source of contamination identified in the
 initial case study-waste sludge containing solvents
 that was applied to road surfaces-does not account
 for the contaminant mass found at the Des Moines
 TCE   site.    Even   at  a  maximum  reported
 concentration  of 3,000,000 ppb  of TCE,  the
 maximum 200 gallons of sludge reported to have
 been  spread onto road surfaces each year would
 have  been equivalent  to 0.6 gallons  of pure TCE
 per year.   Over  the  12-year period from  1966
 through  1978,  during which  the contaminated
 sludge  was  applied,  this   practice  would  have
 accounted for only 7.2 gallons  of TCE,  based on
 available estimates.   By contrast,  750 gallons of
 TCE  were removed  by  the  air stripper from
 December 17,  1987, through  September  1988,
 based  on  mass  balance calculations of the air
 stripper influent and effluent.  Over 1,300 gallons
 of TCE had been removed by  the end of 1989
 (Eckenfelder,  1990).  These results suggest the
 need for more extensive source  identification.

             REMEDIATION

        Design and  Operational
  Features of Remediation  System

The objective of  remediation is to clean up the
ground  water  to  health-based  standards.    The
recovery system in  place as of September 1988
consisted of seven recovery wells, ERW-3 through
ERW-9, oriented  north-south between the DICO
plant and the Raccoon River (see Figure 2).

Several changes were made in the operation of the
extraction system  since late '1988.   Well ERW-9
was removed from service in September 1988 and
was  not operated  in  1989   because  of  iron
encrustation (ERM,  1990).  Well ERW-4  was
taken  out of  service  from late March  to  early
 September 1989,  because of corrosion problems.
 ERW-3 was also  taken out of service for several
 months in 1989 because of corrosion problems.
 Pumping  in  Wells  ERW-5  and  ERW-6 was
 reduced from 225 gpm each to  130 and  160 gpm,
 respectively,  during  a drought in  1989.   The
 overall pumping rate of the extraction system was
 reduced from approximately 1,300 gpm in 1988 to
 approximately 1,000 gpm In 1989.

  EVALUATION OF PERFORMANCE

 The original recovery network Induced a zone of
 ground-water capture that extended horizontally
 beyond the  known limits  of contamination.   A
 decrease in the zone of capture caused by reduced
 pumping in ERW-3, ERW-4, ERW-5, and ERW-6,
 and by the elimination of ERW-9 was observed in
 1989.   Despite  the  reduction   in  pumping,  the
 extraction system has continued to capture ground
 water from all known areas of contamination since
 late 1988.

 The extraction system  has also  continued  to
 remove VOCs from the  ground  water at a
 significant rate. Figure 3 shows  the concentration
 of TCE and Trans-l,2-DCE in the influent to the
 air stripper, from  startup on December 17, 1987,
 through April  1990.   The  concentration of TCE
 was reduced dramatically in the  first 6 months of
 operation.   Since  mid-1988, the concentration of
 TCE has decreased at a much lower rate, from an
 average concentration of approximately 950 ppb in
 mid-1988   to  an   average  concentration   of
 approximately 550 ppb at the end of March 1990.
 Approximately  1,300 gallons   of   TCE  were
 removed by the air stripper from December 1987
 through the end of 1989 (Eckenfelder, 1990). The
 concentration of Trans-1,2-DCE has  been stable at
 approximately 90 ppb since the end of 1988.

 The peak  hi TCE concentrations observed  at  the
 end of March 1989 was reportedly caused by  the
 removal   of  ERW-3 and   ERW-4  from  the
 extraction  system.   Wells ERW-3 and ERW-4  are
 located at  the north end of the  line of extraction
 wells  and extract ground water from  the north
plume, which consists primarily of Trans-1,2-DCE.
 Hence, their primary effect on the concentration of
TCE in the influent  is to dilute the composite
sample  and lower  the  concentration  of  TCE.
However,  no  corresponding  decrease  in  the
influent concentration of TCE  was observed in
September 1989, when ERW-4  was restored to
operation.
                                                  26

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                           Des Moines TCE
                                   !*
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27

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                      3000
                      2000 —
00
                       1000-
                                                    1988
                                                                                     1989
                                                                                                             1990
                                                                          Year
                                                                                              Figure 3
                                                                                              VOC CONCENTRATIONS IN THE INFLUENT
                                                                                              TO THE AIR STRIPPER
                                                                                              DESMCMNESTCESITE
D
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                                                                                    Des Moines TCE
 Updated  time  series   plots  of  contaminant
 concentrations  in  recovery  Well ERW-8  and
 monitoring Wells NW-21 and NW-23  are shown
 in  Figures 4,  5,  and  6,  respectively.     The
 concentration of VOCs in ERW-8 declined rapidly
 from December 1987 through February 1988 and
 then more gradually from February to  September
 1988.  From early 1989 through April 1990, the
 concentrations of  TCE  and Trans- 1,2-DCE in
 ERW-8  were stable  at  approximately 40  and
 30 ppb, respectively.  The concentration of  vinyl
 chloride  in  ERW-8  decreased  to  below  the
 detection limits by mid-1989.

 The concentrations of VOCs in NW-21,  located
 west of the river and east of the north gallery (see
 Figure 2), have been erratic since startup, but have
 decreased gradually from December 1987 through
 April 1990.  These data indicate that ground-water
 quality in this area is  improving  as a result of
 remediation.

 The concentrations of VOCs in NW-23,  located
 southeast  of  the  extraction  wells,  declined
 significantly in the first 6 months of operation, but
 have stabilized since mid-1988;  the concentration
 of Trans-1,2-DCE  in  NW-23, has remained at
 approximately 90 ppb since the beginning of 1989.

    SUMMARY OF REMEDIATION

 The  hydraulic zone  of capture  created  by the
 ground-water extraction  system  has consistently
 included  the  areas  of  known  ground-water
 contamination since the system began pumping in
 December 1987.  Approximately 1,300  gallons of
 TCE were removed by the extraction system  from
 December 1987 through the end of 1989.

 The concentrations of VOCs in ground-water have
 been  reduced  significantly  as  a   result  of
 remediation.    After  initial  sharp  declines,  the
 concentrations of VOCs have continued to  decline
 gradually in  most wells and in the influent to the
 air stripper.  More  complete identification of the
 source and mass inventory of VOC contamination
may help in guiding future remediation  efforts.

   SUMMARY OF NAPL-RELATED
                 ISSUES

The presence of a residual source of ground-water
contamination  in  the  form  of a  DNAPL  is
suspected at  the Des Moines TCE site.  However,
after a preliminary investigation of suspect bedrock
surfaces, the presence of a DNAPL cannot yet be
confirmed.    The  suspicion   persists  primarily
because the quantity of contamination identified in
the  shallow  contaminated soils  seems  to be
insufficient to account for the  scale of the known
ground-water contamination.  By the end of 1989
it was estimated that the quantity of TCE that had
been  removed  by  the extraction  system  was
equivalent to approximately 1,300 gallons of the
pure compound.  The contamination problem was
initially attributed by DICO to a relatively small
amount of waste solvent in sludge used for dust
control  on  the  DICO property.   Current  site
investigations are attempting to identify additional
sources of the ground-water contamination.

The maximum concentration of TCE that has been
detected in ground water at the site was 8,467 ppb.
This  is  less  than 1 percent of the   aqueous
solubility of TCE, and would not in itself be taken
as  an  indication  of the  presence of  DNAPL.
Depth-specific  soil sampling during the remedial
investigation showed  that VOCs were present at
least as deep as the middle of the sand and gravel
aquifer  before  startup  of   the  ground-water
remediation system. Only one sample was taken
from the bottom of the aquifer,  and it did not
show contamination.  However, no contamination
was detected from the shallower  samples taken
from that deep boring either.  More recently, soil
sampling from the  bottom  of the aquifer and the
underlying  bedrock have  failed  to  indicate the
presence of NAPLs.

As  shown in the time-series concentration plots,
the ground-water concentrations have been reduced
substantially since  the beginning  of remediation,
but have  generally stabilized  at  concentrations
above health-based  levels.  This is  consistent with
the presence of a  residual source that  could be
attributed to DNAPLs.   However, it could also be
explained by the gradual release of contaminants
absorbed to soils in the less permeable parts of the
aquifer or the vadose zone.
                                                   29

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  u>
  o
8
                      2000
*d
I
i
5
                      1000 —
                                                      1988
                                                                                         1989
                                                                                                      1990
                                                                         Year
                                                                                               Figure 4
                                                                                               VOC CONCENTRATIONS IN EXTRACTION
                                                                                               WELLERW-8
                                                                                               DES MOINES TCE SITE
                                                                                                                         (A
                                                                                                                         |

                                                                                                                         1
                                                                                                                                      m

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                      Des Moines TCE
                                UJ

                                5
                                uj
                                5
31

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2



§
      120C
      1000
       800 -
600 -
       400 -
       200 -
                                  1988
                                                            1989
1990
                                                   Year
                                                                                                            O
                                                                                                            (0
                                                                                                            (0


                                                                                                            53


                                                                                                            
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                                                                               Des Moines TCE
      UPDATE BIBLIOGRAPHY/
             REFERENCES

Eckenfelder,  Inc. October 1989.  Des Moines
South  Area   Source   Control  Operable   Unit
Sampling and Analysis Plan.

Eckenfelder,  Inc. February 1990.  Performance
Evaluation Report No. 4 (January  1989 through
December 1989)  Groundwater Recovery  and
Treatment System, Des  Moines TCE Site,  Des
Moines, Iowa.

Eckenfelder,  Inc. March 26,  1990.   Progress
Report for February  1990-letter  to Mr. Glenn
Curtis of EPA Region 7.

Eckenfelder,  Inc. March 30,  1990.   Progress
Report for January 1990 letter to Mr. Glenn Curtis
of EPA Region 7.

Eckenfelder, Inc. May  10, 1990.  Progress Report
for March 1990 letter to Mr. Glenn Curtis of EPA
Region 7.

U.S.  Environmental  Protection Agency (U.S.
EPA).   December 17,  1985.   Final Remedial
Investigation  Report, Des Moines TCE Site,  Des
Moines, Iowa.

U.S. EPA.  October 1989. Evaluation of Ground-
water Extraction Remedies:    Volume  2, Case
Studies 1-19.  EPA/9355.4-03.
                                                33
383

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                                                    UPDATE OF CASE STUDY 4

                                                                 Du Font-Mobile
                                                                  Axis, Alabama
Abstract

Ground water in the unconfined sand aquifer is contaminated with volatile organics, base
neutrals, and pesticides from a closed landfill. Since 1985, three extraction wells have
been operating at the site boundary to prevent offsite migration of the contaminant plume.
There have been no significant changes in the system since the original case study.  The
contaminant plume appears to be stable.
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
December 1985
VOCs, Pesticides
Alluvial sand and clay
3
180-gpm
38 acres
30 feet
Total Organic Halides 10,450
Carbon Tetrachloride 5,815
Trichloroethylene 3,940
1,2,4-Trichlorobenzene 6,270
ppb
ppb
ppb
ppb
                                       34

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                                CASE STUDY UPDATE
                               DU FONT-MOBILE SITE

                           BACKGROUND OF THE PROBLEM
             INTRODUCTION

This report discusses progress in the remediation
of  the  Du  Font-Mobile site from  early  1989
through October 1990.  It is an  update of the
original case study  which was based  on data
collected through the end of 1988  (U.S. EPA,
1989, Case Study 4).

The Du Font-Mobile site is an agricultural product
manufacturing facility located in the town of Axis,
Alabama, approximately 25 miles north of Mobile.
Figure 1 shows  the location of the site and the
surrounding properties.  Beginning  in 1969, Shell
Oil Company, then owner of the plant, disposed of
sludges and drums  of liquid wastes  containing
pesticides   and   VOCs  hi  an  onsite   landfill
consisting  of three earthen  pits.  In addition, two
surface impoundments called Six Acre-Foot Pond
and Four  Acre-Foot Pond were used for liquid
wastes generated during insecticide production and
for NPDES surge capacity.

Closure of the  three waste management areas
occurred during  1979 and 1980. The waste drums
and   approximately   4,000   cubic   yards   of
contaminated soils were removed from the landfill
area  and   disposed  of offsite,  followed  by
backfilling  and  regrading.    The  two  surface
impoundments  were  drained,  excavated,  and
regraded.

Ground-water contamination originating from the
former landfill area  was first discovered in 1983
when  sampling was performed by Shell Oil as part
of an  RCRA  facility assessment.   As a  result,  a
ground-water  extraction  and • monitoring  system
was installed  to  prevent further migration of the
contaminants. Additional wells were added to this
system in 1984 and 1985 to improve effectiveness.
Through soil sampling  and  assessment of past
waste-handling  practices, the  two former pond
areas  were judged  not to  pose  a  significant
immediate threat of contamination  to the ground
water.

The site lies  over  three prominent stratigraphic
units.  The shallowest unit consists of 5 to 40 feet
of surficial clay containing discontinuous silt and
sand  lenses covered  with  several feet  of fill
material.   Directly beneath the clay is a layer of
well-graded sand, ranging in thickness from 45 to
70 feet, containing clay lenses but thought to be
hydraulically  continuous.  Finally, immediately
beneath the sand layer lies a second layer of clay,
extending vertically from approximately  90 to 600
feet below the ground surface.

Two aquifers exist beneath the site.  The first is
located in  the sand layer,  with the second located
deep below the site under the lower layer of clay.
Because of the thickness and impermeability of the
lower clay layer, only  the shallow sand  aquifer is
considered   to  be  in   immediate  danger  of
contamination from the site. This shallow aquifer,
referred to  as  the   Alluvium  Aquifer,  has  a
predominantly eastward flow toward the Mobile
River under natural  conditions.   However, long-
term heavy industrial water-supply pumping at the
neighboring  Courtauld's  North America property
has created  a prevailing  northward flow in the
central portion  of the Du  Pont  site,  with the
Mobile River now serving as a source of recharge.

The primary contaminants of concern are VOCs
and  pesticides,  along  with some base-neutrals.
While  the  exact nature and volume  of wastes
disposed  of  onsite   is   unknown, post-closure
ground-water  monitoring  has   detected   the
contaminants listed in Table 1.

           UPDATE ON SITE
          CHARACTERISTICS

Since the  time  of the original case study,  there
have  been   no  important  changes   in   site
administration  or  in  the understanding  of the
hydrogeology, or waste characteristics.  The site
continues  to operate under the  provisions  of a
RCRA permit for operation of a hazardous waste
storage facility that was issued in 1987. For the
past 2 years, the monitoring and extraction wells
have been  sampled on a quarterly basis.
                                              35
                 381

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                                                    Du-Pont-Mobile
  Stautfar Chemical Company
   Courtauld's North America
          Plant Site
E.I. DU PONT DE NEMOURS
     AND COMPANY
       PLANT SITE
                                Scate in Miles
                                                  Figure 1
                                                  SITE LOCATION
                                                  OU PONT-MOBILE Sire
                                                  AXIS, ALABAMA
                       36

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                     Du-Pont-Mobile
Table 1
MAXIMUM CONCENTRATIONS OF CHEMICAL CONSTITUENTS
OBSERVED IN GROUND- WATER MONITORING WELLS
1984 Through 1987
Ground- Water Chemical Constituent
Maximum Con.
(ppb)
Monitoring
Wells
Dates
Volatile Organics
Acroleih
Benzene
Carbon Tetrachloride (CBT)
Chloroform (CRF)
Chlorobenzene
Dibromochloropropane
Dichlorobromomethane
1 , 1 -Dichloroethy lene
Ethylbenzene
Methylene Chloride
Tetrachloroethylene
Toluene
1 ,2-Trans-dichloroethylene
1,1,1 -Trichloroethane
Trichlorethylene (TCE)
1 ,2-Dichloroethane
1 , 1 ,2,2-Tetrachloroethane
1,1-Dichloroethane
144
5
5,815
2,200
42
3.2
260
10
11.2
63
48.8
12.8
42
42
3,940
3.24
73
13.9
DW-2
51
52
24
22
27
27
23,51,52,53
51
27
32
51
24
27
24
E-2
32
23
09/84
07/85
06/87
07/84
12/87
11/84
11/84
03/87
07/85
11/84
11/84
07/85
08/86
11/84
09/84
09/86
06/87
09/86
Base Neutrals
Isophorone
1,2,4-Trichlorobenzene (TCB)
Atrazine
Bladex
Rabon
Pydrin
19
6,270
179
193
2
4.4
32
32
25
25
18, R-l
32
11/84
11/84
06/87
06/86
07/84
12/87
Other Parameters
37
*D7

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                                                                                      Du-Pont-Mobile
Table 1
MAXIMUM CONCENTRATIONS OF CHEMICAL CONSTITUENTS
OBSERVED IN GROUND-WATER MONITORING WELLS
1984 Through 1987
Ground- Water Chemical Constituent
Chlorides
Sulfates
Cyanide
Maximum Con.
(ppb)
108 ppm
325 ppm
0.01
Monitoring
Wells
39
39
39
Dates
08/85
05/86
05/85
              REMEDIATION
  EVALUATION OF PERFORMANCE
         Design and Operation
        Features of Remediation
                  System

The objective of the ground-water remediation at
this site  is  to  prevent  off-site migration  of
contaminated  ground  water.   The  removal  of
contaminants from the  aquifer is considered to be
a  secondary benefit of the remediation  effort.
Since the contaminated soils beneath the former
landfill  continue to be a source of ground-water
contamination, no  projections of time frame for
aquifer restoration have been made.

The remediation  system consists of three operating
ground-water extraction wells located along  the
northern border  of the  site.  Figure 2 shows the
location of all monitoring and extraction wells at
the Du Font-Mobile site.  The first two wells, E-l
and E-2, were initially drilled in late May 1985 to
a depth of 75 feet, near the top of  the shallow
aquifer.  After a failure in the casing of well E-2
in May 1986, well E-3  was installed 25 feet west
of E-2.   Extraction well E-4 was then added  in
December 1986 to increase the effectiveness of the
extraction system.  Currently, wells E-l, E-3, and
E-4 remain in operation, each pumping at rates of
50 to 60 gpm. The extraction system has not been
modified further  since 1986.

The extracted water  is  treated  in  the  plant's
industrial  biotreater  and  then  released  to the
Mobile River as an NPDES-regulated  discharge.
Figures 3 and 4 show the total halogenated organic
compound    (TOX)   concentrations   in    two
monitoring  wells  located near the center of the
plume and in the extraction wells as a function of
time.    The  figures  show   that   the  TOX
concentrations have not decreased steadily over
time. Instead, the TOX concentrations have shown
high variability.  If any  pattern can be discerned
from these records over the past 4 years, it  would
appear  to   be a  slight  trend  of  increasing
concentration.

The observation from Figure  3 that concentrations
in well MW-32 are usually higher than  in MW-24
is consistent with the idea  that  the  landfill is
continuing to release contaminants to the aquifer.
Both wells are located between the landfill and the
line of extraction  wells,  but  MW-32 is closer to
the landfill  and to the probable centerline of the
plume.

Figure 5 shows the measured TOX concentrations
in the monitoring wells MW-50, MW-51, MW-52,
and MW-53, located north of  the line of extraction
wells.   Elevated  concentrations of halogenated
organic substances  were  measured in these  wells,
with the greatest levels found  in MW-51 and MW-
52.   The detection of  organics in these  wells
indicates that contaminants have moved north of
the line of extraction wells at  the site boundary.
However, these contaminants may still be within
the capture zone of the extraction wells.  Because
of the lack of water-level information to the north
of this area,  the extent of the capture zone cannot
be accurately determined.
                                                   38

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                                                                             SITE PLAN SHOWING WASTE MANAGEMENT
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         12000
                1984
1385
    1990
1991
                                                           Year
                                                                                                                            O
Note: The two most recent data points were not validated.
                                                                                               O
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TOTAL ORGANIC HAUOE
CONCEMTBATIONS FOB TWO WELLS   Z
INSIDE THE PLUME                  $
DU PONT - MOBILE SITE                ST

-------
              800
         1
          i
         I
              600 —
400 -I
              200
                  1985
                                                                                           1991
                                                                                                                          o
Note: The two most recent data points were not validated.
                                                                                Hflure4                     ^
                                                                                TOTAL ORGANIC HAUDE       a
                                                                                CONCENTRATIONS FOR FOUR   |
                                                                                EXTRACTION WELLS           g
                                                                                DU PONT - MOBILE SITE          8
                                                                                                                          ffl

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         0
         s
                6000
                5000  -
                4000  -
                3000  —
                2000  —
                1000  —
                                                               MW-50
                                                               MW-51
                                                           •*-—MW-52
                                                               MW-53
                     1965
1986
1967
1968
1989
1990
                                                                                                          1991
Note The two most recent data points were not validated.
                                                                                            a
                                                                                            c
                                                   Figures                        .   .       o
                                                   TOTAL ORGANIC HAUDE CONCENTRATIONS   3
                                                   FOR FOUR MONITORING WELLS UPGRADIENT  •
                                                   FROM EXTRACTION WELLS                  o
                                                   DU PONT - MOBILE SITE                       JT
                                                                                            9

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                                                                                     Du-Pont-Mobile
    SUMMARY OF REMEDIATION

A ground-water extraction  system consisting  of
four wells on the northern boundary of the site has
been in continuous operation since the wells were
installed in  1985 and 1986.  Its  objective is  to
prevent offsite migration of contaminants.  In the
original  case  study,   some  uncertainty  was
expressed concerning the degree of plume capture
achieved by the extraction system.   A  time-
averaged contour plot of the potentiometric surface
under  the influence of the extraction  wells was
presented in  the original  study, which suggested
that the  plume was  being captured.   This plot,
however,  was  based mainly  on water   levels
measured in the upper, and less permeable,  part of
the Alluvium Aquifer.  There was also a general
lack  of  information   on  water  levels  and
contaminant  concentrations  north of  the site
boundary, which would  be helpful in  evaluating
the effectiveness  of the  system.    No  new
potentiometric surface  maps  have  been  made
available since the original case study.

The TOX concentrations in the ground water have
not shown a decline over the 6 years of monitoring
but have instead been highly  variable.   Strong
peaks of halogenated organics continue to occur,
possibly due to slugs of free phase  organics drawn
into  the  extraction  system,  or  to  hydrologic
fluctuations  affecting  leaching of contaminants
from the source area.

   SUMMARY OF NAPL-RELATED
                 ISSUES

Certain  characteristics observed at the Du  Font-
Mobile site suggest that dense non-aqueous phase
liquids (DNAPLs) may be present.  As reflected
by the soil and ground-water sampling and Shell
Company records, the drums buried onsite  Likely
included halogenated organic materials, such  as
trichloroethylene  (TCE),  that  are  potentially
present as DNAPLs.  If stored in their pure phase
and allowed to leak from the drums into the soil,
the DNAPLs could have  penetrated the clay layer
and the shallow  aquifer, where they might be a
persistent  source of  contamination.   Such  a
scenario might explain the high variability in TOX
concentrations in  both the  extraction  wells and
MW-24 and MW-32.
Many DNAPLs have demonstrated  the ability to
quickly  penetrate  the vadose zone  after release,
even in low permeability clays.  Once in the water
table, these liquids  often continue to  migrate
deeper, showing a  tendency to follow gravity more
than the established direction of  ground-water
flow.    As   a  result,  DNAPL   contaminant
concentrations  should typically be higher in the
lower reaches  of the  aquifer.   Ground-water
sampling at the  Du Pont-Mobile  site  has not
determined  the extent of vertical distribution of
contaminants   within   the  plume.     Further
investigation would be  necessary  to determine
whether DNAPLs  are present in the lower reaches
of the aquifer, and if so, whether the extraction
well capture  zone is adequate  to  prevent the
further  migration  of  aqueous   contaminants
originating from a deep DNAPL source.

      UPDATE BIBLIOGRAPHY/
              REFERENCES

E.I. Du Pont de Nemours and Co., Inc. November
1988.    Status  Report  for   RCRA   Facility
Investigation,   Solid  Waste Management Units,
Mobile Chemical Plant.

E.I. Du Pont de Nemours and Co., Inc.   April 16,
1990. Letter report on ground-water  monitoring to
Sue  Robertson of the  Alabama  Department of
Environmental  Management.

E.I.  Du Pont   de  Nemours  and  Co.,  Inc.
January 28, 1991.   Letter report on  ground-water
monitoring  to  Sue  Robertson  of  the  Alabama
Department of  Environmental Management.

U.S.  Environmental  Protection  Agency  (U.S.
EPA).   October 1989.   Evaluation of Ground-
Water Extraction  Remedies:   Volume 2,  Case
Studies 1-19. EPA/9.355.4-03.
If DNAPLs were released, the complexity of the
remediation necessary could increase significantly.
                                                  43

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                                                                 CASE STUDY 5

                                                               Emerson Electric
                                                     Altamonte Springs, Florida
Abstract

The site is a former electrical component manufacturing and assembly plant that operated
from January 1979 to the mid-1980s.  From January 1980 to November 1981, wastewater
from metal  filming operations was  discharged to a septic tank and tile  drain on  the
southeast side of the main  plant building.   The discharge  contained chlorinated and
nonchlorinated solvents, xylene, ketones and other contaminants.  From .December 1984 to
June  1987,  a remediation  system consisting  of  five  extraction  wells was operated.
Concentrations of contaminants from composite samples decreased during this period. As a
result, remediation is considered complete and the site has been removed from the State
Action Site list.  Because performance monitoring was limited to composite samples taken
from the extraction wells, it  is difficult  to judge the completeness of aquifer restoration.
Since the original case study was completed, monitoring has been discontinued.  Because no
new  data have been generated, a case study update for the site was not written.  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
1981
December 1984
VOCs
Sand
5
30 gpm
3 acres
50 feet
Methyl Isobutyl Ketone: 90,000 ppb
REFERENCE

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.
                                       44
                                                                     60677

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                                                    UPDATE OF CASE STUDY 6

                                                        Fairchild Semiconductor
                                                            San Jose, California
Abstract

To  date,  the remediation system  appears to be  effective  in  containing ground-water
contamination and has prevented the contamination of public  drinking water supply wells.
Since remediation began in 1982, VOC concentrations in ground water have decreased.  In
many offsite wells, VOC concentrations have  decreased below cleanup levels.  The slurry
wall installed in Aquifers A and B  continues  to prevent offsite migration of contaminants
and resaturation of remediated areas.  In May 1990, pumping of onsite extraction wells
ceased in accordance with the Remedial Actions Plan.  Offsite pumping of ground water has
continued.   Beginning  September  1990, treated ground  water  was  to be reinjected to
resaturate the onsite aquifer contained within the slurry wall.
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
January 1982
1,1,1 -Trichloroethane
1 , 1-Dichloroethylene
Freon
Alluvial sand and gravel with silt
and clay layers
36
9,200 gpm
75 acres
180 feet
1,1,1-Trichloroethane 1,900,000
ppb
                                       45
30$

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                                CASE STUDY UPDATE
           FAIRCHILD SEMICONDUCTOR CORPORATION SITE

                           BACKGROUND OF THE PROBLEM
            INTRODUCTION

The   original  case  study  for   the  Fairchild
Semiconductor Corporation site (U.S. EPA, 1989,
Case Study 6) presented background information
and  data from  ground-water monitoring  and
extraction systems through December 1988.  The
22-acre FairehUd Semiconductor Corporation  site,
located at Bernal Road in the City of  San Jose,
California,  is   presently   owned   by   the
Schlumberger Technology Corporation.  Figure 1
presents  an  overview  of  the   site  location.
FairehUd first discovered chemical residues in the
ground water in November 1981.  Contamination
was  the  result of a  leaking underground waste
solvent storage tank.

The site is included on the California Expenditure
Plan  for the  Hazardous Waste Cleanup  Bond Act
of 1984  and was proposed for inclusion of the
National  Priorities List (NPL) under Superfund.
Cooperative  and enforcement  agreements were
entered into in May, 1985, between the U.S. EPA,
the California  Regional Water Quality Control
Board (RWQCB), and the California Department
of Health Services.  The RWQCB has been acting
as the lead agency overseeing cleanup of the site.

Operation of  a  ground-water extraction  and
treatment system began on January 16, 1982, as
part of interim remedial measure (IRM) activities.
To date,  onsite IRM  activities  have consisted of
underground storage tank removal, excavation of
3,389 cubic yards of soil, ground-water  extraction
and treatment,  conduit sealing, in-situ soil vapor
extraction, and slurry wall containment  Offsite
IRM  activities  have   included   ground-water
extraction,    treatment,  and    monitoring.
Remediation described  in the Remedial Action
Plan  (RAP)  prepared in October  1988, has  also
been implemented.

The Fairchild facility is located in a drainage basin
that  slopes  northward   into   the  nearby  San
Francisco  Bay.  The unit  consists  of a broad
alluvial valley that is  underlain by unconsolidated
clays, silts, sands, and gravel.  Sand and gravel
layers interbedded with silt and silty clay layers
 combine to form four distinct underlying aquifers
 at  the  site.   These aquifers are referred to as
 Aquifers  A,  B, C,  and D.   The  aquifers are
 separated by silt and silty clay  aquitards  which
- range from several feet to 60 feet thick.

 Aquifer A, which consists  of alluvial sands and
 gravel,  is located 10 to 20 feet below the pound
 surface and has a thickness of 15 to 40 feet. It is
 not continuous offsite and is currently dewatered
 onsite  as  a  result  of ground-water extraction
 activities.  The aquifer is hydraulically connected
 with Aquifer B onsite in the vicinity of the former
 underground  waste  solvent storage  tank.   The
 highest solvent concentrations were detected prior
 to  November  1982, within  50 feet of the former
 underground tank in Aquitard A/B.

 Aquifer B consists of dense sands and gravels and
 is  located between  60 and 120 feet below the
 ground surface.  Water level data from April 1982,
 indicate ground water flow  is to  the northwest in
 this  aquifer.     Initially   a confined  aquifer,
 Aquifer B changed from confined to unconfmed as
 a result of ground-water extraction in Aquifers A,
 B,  and  C.

 Aquifer C consists of dense sands and gravels and
 is  located between  150 to 190 feet below the
 ground surface.   The  aquifer  has  remained  a
 confined  system throughout the  duration  of the
 ground-water  extraction activities.   Water-level
 data from April 1982, indicate ground-water flow
 in  this aquifer is to the northwest. The continuous
 40-foot-thick  B/C   aquitard  retards  downward
 migration of contaminants into Aquifer C. Recent
 correspondence  from  Schlumberger  (January,
 1990)  states  that offsite  contamination in the
 aquifer  resulted  from old agricultural   wells
 screened  in  multiple  aquifers  and  not  from
 migration  of  contaminants  vertically  through
 Aquitard B/C.

 Aquifer D, found at depths of 220  to  270 feet
 below  the  ground  surface, is  a  discontinuous
 aquifer.  There is an upward hydraulic gradient
 from Aquifer D to Aquifer C.  No contamination
 has been detected in Aquifer D.
                                              46

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 The primary contaminants found at the site were:
 chlorinated solvents, xylene,  acetone, isopropyl-
 alcohol  (iPA),  and Freon-113.   The highest
 concentrations of contaminants were found onsite
 in Aquifers A and B in the vicinity of the former
 underground waste solvent storage tank.

            UPDATE ON SITE
          CHARACTERISTICS

 The updated case study is based on 1989 and 1990
 data obtained from the California Regional Water
 Quality  Control  Board   (RWQCB).   The  data
 include annual,  quarterly,  and monthly reports
 submitted  to  RWQCB   by  Schlumberger  and
 prepared by Schlumberger's consulting engineers,
 Canonic Environmental.    These reports provide
 information  on  ground-water  extraction  rates,
 hydraulic controls, and contaminant concentrations.

 The hydrogeologic  information provided  in  the
 original case study is still current. No information
 has  become  available  since  1988  that  would
 change the description of basic site hydrogeology.

 Aquifers A, B, and C are monitored on annual,
 quarterly, and bimonthly  schedules to evaluate the
 concentrations" of organic contaminants.  Indicator
 compounds were selected due to their frequency of
 detection, concentrations, and spatial distributions.
 They  include:   1,1,1-trichloroethane (TCA), 1,1-
 dichloroethylene (DCE), tetrachloroethylene (PCE),
 xylenes,  acetone, isopropyl  alcohol  (IPA),  and
 Freon-113.  Since December 1988, TCA and 1,1-
 DCE have been  the most prevalent contaminants
 throughout  Aquifers A   and  B.   The highest
 concentrations  of TCA in Aquifers A and B  in
 1982 were  1,900,000  ppb  and  670,000  ppb,
respectively.

As  noted in the original  case study,  prior  to
November  1982, maximum  concentrations   of
several  indicator  compounds  were  higher than
compound  solubility  levels,  suggesting   that
contaminants  in  the ground  water, and in  the
samples, were present as nonaqueous phase liquids
(NAPLs).
                      Fairchild Semiconductor

              REMEDIATION

 Design and Operational  Features of
        the Remediaton System

 Site remediation goals are based on new  criteria
 that were established by the RWQCB and adopted
 in January,  1989.  These criteria specify  that all
 offsite aquifers must meet Hazard Index criteria of
 less than 0.25. Hazard Index values are based on
 the combination of chemicals present rather than
 on   absolute   benchmark   concentrations   for
 individual chemicals.  The Hazard Index (HI) for
 offsite  ground water  is  calculated  from  the
 following equation:
     Concentration of TCA (ppb) ^ Concentration of 1,1-DCB (ppb)
           200 ppb      *        6 ppb
where 200 ppb and 6 ppb are the onsite cleanup
levels for TCA and 1,1-DCE, respectively.

The criteria also state that onsite wells must meet
the California  Department  of  Health  Services
drinking   water  action   level   or   Maximum
Contaminant  Level  (MCL),  whichever  is more
stringent,  for TCA,  1,1-DCE,  Freon-113,  and
xylenes. The cleanup goal for PCE is 2 ppb based
on  the proposed state MCL.  Cleanup goals for
IPA and acetone are  3,500 ppb  and 2,250 ppb,
respectively, based oh oral reference dose data in
IRIS (U.S. EPA's Integrated Risk Management
Information System).

Offsite remediation  activities from  1982 to  the
present have  focused  on  ground-water extraction
and treatment to HI  cleanup levels, and ground-
water reuse and/or discharge.

The offsite B  Aquifer was divided into three zones
for the purpose of remediation evaluation (Refer to
Figure  2).   Zone boundaries  were  determined
based on the  estimated length of time required to
remediate  each zone to HI cleanup levels.  Using
this approach,  ground-water extraction  in each
zone, would be terminated when the B  Aquifer in
that zone  was remediated to concentrations that
correspond with  HI  cleanup  criteria.   With
reference to the October 1988 RAP, the estimated
time for remediation in each zone is 0  years, 2
years,  and 5  years  for  zones   1,  2, and  3,
respectively.  The frame of reference for these
                                                  48
                               0*77

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                                                                                 AQUIFER B ZONES AND

                                                          (Poor Quality Original)     WELL LOCATION PLAN
                                                          1         *  •»   '     FAnCHKDSEMCOMXJCTORSITE

-------
                                                                             Fairchild Semiconductor
 goals  is January  1989,  the  date  of  RWQCB
 acceptance of the RAP.

 During  the  interim  remedial  program,  which
 started in 1982, Fairchild installed 40 ground-water
 recovery wells  in onsite and  offsite locations.
 Recovery  wells  were  installed  in  Aquifers A,
 B,and C in downgradient areas west and northwest
 of the Fairchild plant.  Recovery well  locations
 were chosen using aquifer test results.  Recovery
 wells were also placed parallel to local roadways
 to  prevent  further  westward  migration of  the
 plume.  Only 36 of the 40 initial recovery wells
 were ever operated, and only six recovery wells
 were operating as of the end of 1988.

 Ground-water extraction was initiated  on January
 16,  1982, with  the  pumping  of approximately
 1,260 gpm from Well GO-13(M), an offsite water
 supply well.  This rate was increased steadily until
 January   1983,  when   9,600 gpm  were  being
 extracted.  Since January 1983, the total flow rate
 has   been   gradually   reduced.      Before
 implementation of the operational plan to reduce
 ground-water  extraction  in February  1989,  the
 pumping rate in Aquifer B was 960 gpm.  As of
 September  1990,  the   only   extraction  wells
 operating were three wells in Aquifer B~RW-2(B),
 RW-22(B),  and RW-25(B).   These wells  were
 operated at a total pumping rate of 655 gpm.  The
 locations  of these  three wells are  circled in
 Figure 2.

 As of September 1990, pumping in offsite Aquifer
 B  recovery Wells RW-2(B), RW-22(B), and RW-
 25(B) continued to maintain hydraulic control of
 contaminated ground  water.   The  pumping of
 onsite  extraction  wells ceased  in May 1990, in
 accordance with  RAP  activities.  Ground-water
 extraction flow rates from January 1990, through
 September 1990, for both onsite and offsite wells
 averaged  656  gpm (Refer to  Table 1).   Offsite
 ground-water extraction  between zones 2 and 3
maintained an  average  flow  rate  of 649  gpm
following the  termination  of  onsite pumping
activities. Offsite ground-water extraction rates for
zone  2 wells  only averaged 221 gpm.   Onsite
Wells AE-l(B), AE-2(B), AE-3(B), AE-4(B), and
RW-28(B) were reactivated in September 1990, to
evaluate  the application of the  treatment  and
reinjection system.   Reactivation of the system
lowered the water table in Aquifer B by 4.71  feet
to an average water-level elevation of 148.8 feet in
September 1990.
 In  mid-1986,  a  3-foot-thick  slurry  wall  was
 installed through Aquifers A and B to enclose the
 onsite portion of the site.  The slurry wall extends
 to the bottom of Aquifer B.  The slurry wall acts
 to prevent resaturation  of remediated areas from
 nearby percolation ponds and offsite migration of
 contamination.

 The head differential across  the slurry wall barrier
 has  been  measured on  an annual,  quarterly, and
 bimonthly basis to monitor the safety of the slurry
 wall system.  A head differential of less  than 24
 feet was  determined  to represent  an appropriate
 level of safety to prevent the loss  of fine-grained
 soils from the slurry wall system.  The slurry wall
 has  been  determined  to  be  very effective in
 reducing onsite pumping requirements.

 In June 1990, Schlumberger submitted a  systems
 design plan  for treating extracted ground water
 from onsite  wells  and offsite Well RW-25(B).
 The treatment system, which uses a Baltimore Air
 Coil (BAG)  water cooling  tower as the  primary
 treatment  system, has been  designed to meet the
 instantaneous  effluent  limitations  adopted  by
 RWQCB.  These limits are 5  ppb for TCA and
 1,1-DCE each. While the tower was designed for
 cooling, it has been adapted for use at this site as
 an air stripper to accommodate the pumping and
 treatment  of a  large volume  of  ground water.
 Beginning in  September  1990,  treated  ground
 water  was  to  be  reinjected into  Aquifer  B to
 resaturate the  B Aquifer  contained within  the
 slurry wall to water levels even with those outside
 of the slurry wall system.  Resaturation  through
 reinjection of extracted  groundwater is consistent
 with state water conservation initiatives.  After the
 desired water level recovery inside the slurry  wall
 has  been  achieved,  pumping  from some onsite
 wells may resume with continued  treatment and
 reinjection.

 In-situ soil  vapor  extraction,  which began  as a
 pilot study in October 1988, continues to be used
 to remove subsurface VOCs (including  NAPLs)
 from the  unsaturated soils in Aquifers A and B,
 and  the A/B aquitard.  Thirty-two air extraction
 wells and 5  ground-water recovery wells are used
 for the aeration process.  The wells are located in
 the vicinity  of  the former  underground  storage
 tank,  fiight air inlet wells were installed in areas
not affected by the contamination to facilitate air
flow through the affected soils.  The extracted air
is  treated  with granular activated  carbon before
emission to the atmosphere.
                                                     50

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O
Tablet
PUMPING SCHEDULE
FLOW READINGS (gpm)
1990

Well
Number
RW-2(B)
RW-22(B)
RW-25(B)
RW-28(B)
AE-l(B)
AE-2(B)
AE-3(B)
AE-4(B)
Total Flow


01/03
202
261
261
21
9
30
28
35
664


01/01
209
261
261
20
9
32
17
35
671

01/17
202
254
254
16
9
32
18
34
659


01/24
205
254
254
13
8
37
18
33
656


01/31
209
261
261
13
8
32
15
34
670


0207
205
261
261
' 13
7
32
11
33
660
Page 1 or 3

02/14
205
254
254
13
8
30
7
34
663

02/21
205
254
254
13
7
31
11
33
658

02/28
205
244
244
12
-<•)
32
12
34
646

03/07
205
248
248
13
_(«)
31
11
33
649

03/14
208
254
254
12
..(a)
32
9
33
668

03/21
202
261
261
13
8
30
10
33
664

03/28
205
254
254
14
7
30
10
35
665
Source: Canonic Environmental, 1990c
Notes:
(a)Wetl AE-l(B) shut down for maintenance.
                                                                                                                                                                 -n
                                                                                                                                                                 £.
                                                                                                                                                                 o
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to
Table 1
PUMPING SCHEDULE
FLOW READINGS (gpn)
1990
. Page 2 of 3
Well
Number
RW-2(B)
RW-22(B)
RW-25(B)
RW-28(B)
AE-l(B)
AE-2(B)
AE-3(B)
AE-4(B)
Total Flow
04/04
205
254
110
13
8
31
9
35
665
0411
205
254
104
13
8
32
10
34
660
04/1S
202
254
104
13
8
31
10
35
657
04/25
205
270
110
13
7
30
10
35
680
0902
202
267
114
12
7
29
10
34
675
05/09
199
254
111
11
7
30
10
34
656
0916
202
267
117
11
7
28
9
33
674
0923
183
244
111
11
8
28
10
33
628
0930
170
238
183
_(•)
_(•)
-(a)
-00
-(*)
591
06/06
195
254
199
-
--
'
--
-
648
06713
195
254
199
-
-
-
--
-
648
06/19
195
260
199
-
--
-
-
-
654
06/26
192
323(«>)
199
.
-
-
-
-
714
Source: Canonic Environmental, 1990c
Notes:
(a) Terminated pumping on May 24, 1990, as approved by RWQCB.
(b) Increased flow rate due to irrigation.
                                                                                                                                                    a
                                                                                                                                                    SP
                                                                                                                                                    o
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                                                                                                                                                    a

                                                                                                                                                    I

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Table 1
PUMPING SCHEDULE
FLOW READINGS (jpm)
1990

Well
Number
RW-2(B)
RW-22(B)
RW-25(B)
Total Row


07/03
192
319(a)
199
710

07/11
199
205
199
603

VJ/lt
195
205
199
599

07/25
195
209
202
606

own
194
176
199
569

Ot/M
222
238
199
659

08/15
205
31o(a)
199
714

08/22
215
205
199
619


08/29
195
192
199W
586

09/05
228
261
251
-------
                                                                           Fairchild Semiconductor
       EVALUATION OF SYSTEM
             PERFORMANCE

 Since December 1988, the last month covered by
 the  original  case  study,  the  only  chemicals
 detected outside the slurry wall enclosure in zone
 3 of Aquifer B were  TCA and 1,1-DCE.  Some
 TCA  concentrations were detected above cleanup
 levels.

 Aquifer  A,  which   was  dewatered  in  1984,
 remained dewatered in 1989 and 1990.  Aquifer C
 has continued to meet  offsite cleanup level criteria
 since  it was  remediated in late 1988.  However,
 low TCA concentrations have been observed in
 Aquifer C.  These detections  are lower  than the
 offsite cleanup criteria levels  established for the
 combined effects  of TCA and 1,1-DCE, and are
 within  the   range   expected  following  the
 termination of pumping in Aquifer C.

 Zone  1, the offsite area farthest from the Fairchild
 facility,  attained  cleanup  criteria  levels   by
 December 1989.  Ground-water  monitoring data
 from    1990   confirm   TCA  and    1,1-DCE
 concentrations within cleanup criteria levels (Refer
 to Table  2).   Zone  1  attained  cleanup criteria
 levels   in  less  than   one   year  from  the
 implementation of the  RAP. This schedule meets
 the system performance goals set forth in the RAP.

 In 1989, zone  2  and  3 ground-water extraction
 activities continued to provide  hydraulic control of
 the  chemical bearing  ground-water  plume  in
 Aquifer B. The average total Aquifer B extraction
 rate for  1989  was  650  gpm.   This  represents
 quarterly averages of 840, 648, 563, and 545 gpm
 for  the first, second,  third, and  fourth  quarters,
 respectively.  The  decreasing rates were due to the
 shutoff of recovery wells RW-19(B) on February
 7,  1989,  and  RW-27(B)  on April  11,  1989.
 Shutoff of these recovery wells was scheduled as
 part of the operational plan to reduce ground-water
 extraction in Aquifer B.

 By  December 1988,   ground-water  levels  in
 Aquifer B had declined 23 to 38 feet below April
 1982 levels as a result of ground-water extraction
activities.   A program  to reduce  ground-water
extraction in Aquifer B was initiated on February
7,  1989.   This  plan  involved  the  shutoff  of
individual offsite  wells.   By September 1990,
ground-water levels in  B had risen 13.4 feet above
February  1989 levels.    By  December  1988,
ground-water levels in  Aquifer C  had declined 40
feet below April 1982 levels. A program to reduce
ground-water extraction in Aquifer C was initiated
on  May  2,  1988.   By December 1989, ground-
water  levels in Aquifer C  had risen  25.5  feet
above  May  1988, levels.  Ground-water levels in
Aquifer C remained steady during  1989 and 1990.
September 1990 water levels for Aquifers B and C
are presented in Figures 3 and 4, respectively.

TCA concentrations at onsite Aquifer B wells have
decreased from a  maximum of 670,000  ppb in
1982, to a maximum of 2,000 ppb measured from
Well WCC-17(B) on August 29, 1990.  Figure 5
presents the distribution of  TCA in Aquifer B on
September 30,  1990, overlaid on contours  of the
TCA concentration on October 31,  1982, 9 months
after extraction  began. Figure 5 shows that offsite
TCA  concentrations have  been reduced by as
much as  two orders of magnitude in some areas,
and that  the  size of  the 10-ppb  plume  has
decreased to less then half of its original size.

Figures 6 and 7 show the contours of the Hazard
Index  of TCA and 1,1-DCE  concentrations in
September   1990,  in   Aquifers   B  and   C,
respectively.  The  Figures show that a substantial
offsite plume  of  contamination with  a  Hazard
Index greater than the standard of 0.25 still existed
in September 1990, in Aquifer B but was absent in
Aquifer C.

Figures 8,  9, and  10  show the  trend of TCA
concentrations in three offsite recovery wells in
Aquifer B-RW-2(B), RW-22(B), and RW-25(B).
All three of the wells were operating recovery
wells  as  of September 1990.  These three plots
confirm that TCA concentrations  in these wells
have decreased substantially from initial levels.
TCA concentrations appear  to have been reduced
to stable levels of approximately  20 ppb  in all
three  wells.    Figure 11  shows  that  the TCA
concentration in onsite Aquifer B recovery Well
RW-28(B) decreased substantially from September
1989, to September 1990.

Initial  startup of the in-situ soil vapor extraction
system began in October 1988, with full operation
beginning in January, 1989.  The total mass of
VOCs  removed  between   October  1988,  and
September  1990, is estimated  at 14,724 pounds,
2,724 pounds above the original projected recovery
rates for the system.  Table  3 presents a
                                                   54

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                 Fairchild Semiconductor

WeH
Number

Most Recent
Sampling Date
Table 2
WATER QUALITY DATA
Concentrations (ppb)
TCA
1,1-DCE
P«gt 1 of 2
Huud liv*fT
Votae
Hazard Index
Target Cleanup
Criteria
Zone 1: OflUte Wells
RW-1203)
RW-14(B)
RW-17(B)
RW-19(B)
RW-20(B)
RW-27(B)
WCC-7(B)
WCC-1303)
WCC-19(B)
WCC-26(B)
WCC-27(B)
74(B)
9/14/90
08/21/90
08/21/90
09/07/90
08/23/90
07/24/90
08/28/90
09/18/90
09A8/90
08/28/90
08/31/90
09/27/90
0.5
0.5
0.5
12.0
1.4
33
0.5
0.5
0.5
0.5
1.0
0.5
0.5
0.5
0.5
0.5
OS
OS
OS
OS
OS
OS
OS
OS
0.00125
0.00125
0.00125
0.1433
0.0903
'0.0165
0.00125
0.00125
0.00125
0.00125
0.0883
0.00125
0.25
0.25
0.25
0.25
0.25
0.25
0.25
0.25
0.25
0.25
0.25
0.25
Zone 2: Ofblte Wells
RW-2(B)»
RW-22(B)*
WCC-15(B)
WCC-25(B)
WCC-39(B)
WCC-23(C)
WCC-28(C)
72
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                 Fairchild Semiconductor
Table!
WATER QUALITY DATA
Page 2 of 2
Well
Number
Most Recent
Sampling Date
Zone 3; OflUteWelb
120(B)
126(B)
127(B)
128{B)
129(B)
WCC-37(B)
WCC-38(B)
WCC-42(B)
Onsite Wells

RW-28(B)
WCC-1(B)
WCC-2(B)
WCC-5(B)
WCC-16(B)
WCC-17(B)
WCC-20(B)
116(B)
122(B)
09/12/90
0701/90
09/14/90
08/31/90
07A3/90
08/30190
07/31/90
09/19/90


09/10/90
09/27/90
09/25/90
09A9/90
09/21/90
09/21/90
09/10/90
09107190
WA2/90
Concentrations (ppb)
TCA

OJ
1.0
0.9
9.1
OJ
OJ
0.6
OJ


1,300.0
660.0
48
18.0
610
330.0
120.0
1.1
OJ
U-DCE

OJ
OJ
OJ
3J
OJ
OJ
0 J '
OJ


230.0
25.0
1.4
1.0
25.0
50.0
13.0
OJ
OJ
Hazard Index
Value

0.00125
0.0883
0.0875
0.6288
0.00125
0.00125
0.086
0.00125

TCA Cleanup
Lewi (ppb)
200.0
200.0
200.0
200.0
200.0
200.0
200.0
200.0
200.0
Hazard Index
Target Cleanup
Criteria

0.25
0.25
0.25
0.25
0.25
0.25
0.25
0.25

U-DCE
Cleanup
Level
(P»b)
6
6
6
6
6
6
6
6
6
Source: Canonic Environmental, I990c
•Wells remaining in operation
56

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                                                                                                           DATA THROUGH SEPTEMBER 30,1NO
                                                                                                           FAKCHU.D SEMCONDUCTOR StTE
(Poor Quality Original)

-------
LEGEND:
    ***HOOM60 AND SEALED
    LMMC OMMCTEK WW1H tUTKY WCU
                                     »«3»T KCEHT DATA TMBOOOH OECCMEn M
                                                                                                               Hgur.7
                                                                                                               AOUFER C HAZARD INDEX VALUES
                                                                                                               DATA THROUGH DECEMBER 31. MM
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cr\
               OQ
               Q.
               O.
               O
               •— i
               l-i
               cc
UJ
o
o
o
cc
o
                    1,200
                    1,000-
                      800
                      600-
                     400-
                     200-
                            1982    1983    1984   1985   1986   1987   1988   1989   1990
        Source: Based on Canonie Environmental. 1990c
                                                                   Figures
                                                                   MULTIYEAR TCA CONCENTRATIONS
                                                                   IN OFFSITE WELL RW-2 (B)
                                                                   FAIRCHILOSEMICO»«>UCTOR SITE
                                                                                                                  O
                                                                                                                  a

                                                                                                                  I
                                                                                                                  8
                                                                                                                 §

-------
o\
1984      1985      1986      198?     1988
                                                                                    1989      1990
                                                                                        I
                                                                                        o
         Source Based CHI Canonie Environmental, I990c
                                                        Figure 9
                                                        MULTIYtAR TCA COMCEMTeATIONS
                                                        m OFFSfTE WELL RW-22 (B)
                                                        FAWCHILO ^MICONOOCTC« aTE
o
o
a

i

-------
           1,000
       flQ

       Q_

       Q_
       O
       a:
       1-1

       UJ
       o

       O
       O

       ai
       o
       1-1
800
             600-
400-
200
                      1984
                  1985
1986      1987      1988      1989      1990
I
o
3-
Source: Based on Canonie Environmental, 1990c
                                                                Figure 10

                                                                MULTIYEAR TCA CONCEMTRATtOMS

                                                                IN OFFSITE WELL RW-25 (B)

                                                                FAIRCHILD SEMCONCHJCTOH SITE
                                                                   o
                                                                   o

                                                                   a.
                                                                   c
                                                                   o

-------
                       12,000
                       10,001
                    %  0,000
                   g
  CTv ,
  Ut
                        8,000
                        4,000
                        2,000
                               SEPOCfWJVDECJINrEBMflRflPRMnYJUNJULBUeSEP
                                       1989                                 1990   *
-4
          Source  Based on Canonte Environmental, 1990c
Flflur«11
MULTIYEAR TCA CONCiHTn/OTONS
IN OFFSfTE WELL RW-28 (B)
FAIRCHILD SEMICCMIDUCTOfl SITE
(A
9
o"
O
a

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Fairchild Semiconductor
Table 3
SOIL VAPOR EXTRACTION SYSTEM
ESTIMATE OF MASS REMOVED"-1*
Page 1 of 2
Well
Number •
1,1,1-
TCA
Removed
(DM)
1,1-DCE
Removed
(Ibs)
PCE
Removed
(Ibs)
Xvlene
Removed
(Ibs)
Ftcon-113
Removed
(Ibs)
Acetone
Removed
(Ibs)
IPA
Removed
(Ibs)
Period
Total
(Ibs)
Aquitard A/B Wells
AE-1A
AE-2A
AE-3A
AE-4A
AE-5A
AE-6A
AE-7A
AE-8A
AE-9A
AE-10A
AE-11A
AE-12A
AE-13A
AE-14A
AE-15A
AE-16A
AE-17A
AE-18A
AE-19A
AE/A1-18A
AE/A1-19A
AE/A1-20A
AE/A1-21A
AE/A1-22A
AE/A1-23A
AE/A1-24A
AE/A1-25A
Subtotals
21
50
15
34
62
18
17
79
71
93
29
1,618
337
1,166
79
211
204
376
15
16
18
21
1
55
6
5
5
4,622
3
6
1
5
5
2
3
10
5
8
7
46
23
88
11
16
14
15
1
5
4
5
0
8
2
1
1
294
0
0
0
0
0
0
0
0
0
0
0
0
1
2
0
1
0
1
0
0
0
0
0
0
0
0
0
7
2
5
1
1
1
1
0
10
11
6
3
5,
24
10
15
34
25
38
0
0
1
0
0
2
0
0
1
196
0
0
0
0
0
0
0
0
0
0
0
2
1
2
0
1
0
0
0
0
0
0
0
0
0
0
0
8
1
4
429
2
8
429
1
1
2
444
0
320
1
30
230
916
275
186
225
0
0
5
0
1
17
0
0
3,526
0
0
113
0
0
143
0
0
0
47
0
17
0
0
20
195
96
9
76
0
0
2
0
0
0
0
0
720
26
66
559
41
77
592
22
101
89
598
39
2,010
386
1,298
355
1,374
614
623
317
21
23
35
2
66
26
6
6

Aquitard A/B Subtotal 9,373
 H87

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                 Fairchild Semiconductor

Well
Number

1,1,1-
TCA
Removed
(ibs)
Table 3
SOIL VAPOR EXTRACTION SYSTEM
ESTIMATE OF MASS REMOVED*1*
Page 2 of 2
1,1-DCE
Removed
(Ibs)
PCE
Removed
(Ibs)
Xylene
Removed
(Ibs)
Freon-113
Removed
(Ibs)
Aquifer A Wells
AE-20(A)
RW-15(A)
RW-16(A)
RW-23(A)
WCC-41(A)
Subtotals
286
74
115
6
2,301
2,782
5
14
12
3
34
68
2
0
1
0
5
8
127
8
18
0
162
314
0
1
0
0
2
3
Acetone
Removed
(Ibs)

0
0
0
0
545
546
IPA
Removed
(Ibs)
Period
Total
(Ibs)

0
0
0
0
22
22
420
96
146
9
3,071

Aquifer A Subtotal 3,742
Aquifer B Wells
AE-1(B)
AE-2(B)
AE-3(B)
AE-4(B)
WCC-16(B)
WCC-17(B)
WCC-20(B)
Subtotals
139
306
220
395
3
52
95
1,210
53
71
52
105
0
12
34
328
0
1
0
2
0
0
2
5
1
12
16
15
0
1
4
49
0
0
0
1
0
0
0
2
0
1
1
5
1
0
0
7
0
0
0
8
0
0
0
9
193
391
289
531
4
66
135

Aquifer B Subtotal 1,609
Individual Totals of Chemicals Removed

8,614
689
19
559
13
4,079
751


Grand Total 14,724
Source: Canonic Environmental, 1990b
9A1I values are rounded and may not sum correctly.
"All values are current through March 31, 1990.
67

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                                                                          Fairchild Semiconductor
breakdown of the mass of chemicals removed by
each  individual  soil   vapor   extraction  well.
Approximately  59  percent  of  the  mass  of
chemicals removed to date has been TCA.

    SUMMARY OF REMEDIATION

To  date, the remediation  system appears to have
been   effective   in   containing   ground-water
contamination and has prevented the contamination
of other public drinking water supply wells.

Water  quality data  from  Aquifer B  monitoring
wells  for September 1990, indicate that chemical
concentrations in  wells located  in  downgradient
zone 1 have remained below cleanup levels. Parts
of  offsite  zones 2  and 3  and  some  onsite
monitoring wells  are still above cleanup  levels.
Remediation activities for the onsite areas  will
continue until cleanup levels are  achieved.  These
activities include:  in-situ soil vapor extraction and
the  BAG treatment system.

The total amount  of contaminants  removed from
onsite and offsite  areas through  September 1990,
was 143,278  pounds-of  which  38,000 pounds
were removed from the soil;  90,500 pounds were
removed through  ground-water  extraction;  and
14,778 pounds were removed through in-situ soil
vapor extraction (Canonie Environmental, 1991).

   SUMMARY OF NAPL-RELATED
                 ISSUES

The possibility that contaminants are present in the
subsurface  in  the form  of nonaqueous  phase
liquids (NAPLs) has not been addressed in any of
the  site  documents reviewed.  However, the high
ground-water concentrations reported for TCA and
xylene in the original study suggest that they may
have been  present  in NAPL form.

The maximum concentrations reported for these
contaminants in 1982 were 1,900,000 ppb for TCA
and 76,000,000 for  xylene.  In both cases, the
readings were for a sample taken from onsite well
WCC-41(A),  in   Aquifer  A.   These  reported
concentrations are much  higher than the aqueous
solubility of either compound (950,000 ppb for
TCA and 15,000 to 213,000 ppb for xylenes).  The
reporting of concentrations well  above solubility
indicates that the ground-water sample contained a
greater mass  of the contaminant than could be
present in solution. The excess contaminant in the
sample was probably in the form of colloidal-size
globules of NAPL, indicating that the compounds
were present as NAPLs in the aquifer also.

It has  been   reported  that   the  contaminants
originated from  a leaking underground  waste
solvent  storage  tank.   This  suggests that  the
contamination was initially released in nonaqueous
form. Pure TCA is a dense NAPL (DNAPL)  and
would be expected to sink rapidly through  the
aquifer.   In this case,  however, it was  apparently
not  pure TCA,  but  a mixture  containing  a
considerable proportion  of xylene, a  compound
less  dense than water, as well as several other
constituents.  It is not known whether this mixture
would sink in the aquifer or float on the water
table. In either case, it would be likely to migrate
into the underlying  formations  because the water
table was lowered into Aquifer B by the ground-
water extraction system.

In 1987,  the  maximum  concentrations  of both
TCA  and xylene (100,000  ppb and 16,000 ppb,
respectively) were measured in well  WCC-17(B),
which monitors Aquifer B directly below the area
where the highest concentrations were found in
Aquifer  A  5 years  earlier.     This  time  the
concentrations  were approximately 10  percent of
the solubility limits for each compound.   These
concentrations,  although  much lower than  the
maximum readings of 1982, were still high enough
to be a strong indication that NAPLs were present
in the aquifer.  As noted previously, the overlying
portions of Aquifer A were dewatered in 1987,
and could not be sampled.

The  highest  TCA concentration  measured  in
Aquifer  B in  1990 was 2,000 ppb, again in well
WCC-17(B).      The  corresponding   xylene
concentration  was 100 ppb.  These considerable
reductions in  concentration over the  period of
record may indicate that the reservoir of NAPL in
Aquifer  B is nearly exhausted.   An  alternative
explanation may be that the contaminants never
actually  reached Aquifer B in NAPL form,  but
were retained  in the  A/B aquitard, from  which
they  leached  into  Aquifer  B,  producing high
concentrations.   If so, the  soil vapor extraction
system operating in Aquifer A and in the A/B
aquitard may  be responsible for the reduction in
contaminant levels.
                                                   68
                    HDJ

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                                                                         Fairchild Semiconductor
       UPDATE BIBLIOGRAPHY/
              REFERENCES

 Canonic Environmental.  October 1988. Revised
 Draft Report, Remedial Action Plan.

 Canonie Environmental.  February 1990a.  Annual
 Status Report January 1 through December 31,
 1989, Fairchild Semiconductor Corporation, San
 Jose Facility.

 Canonie Environmental.   June 19905.  Detailed
 Design  Waste 001  Treatment  System,  Fairchild
 Semiconductor Corporation, San Jose Facility.

 Canonie   Environmental.    November   1990c.
 Quarterly   Status   Report  July   1,   Through
 September 30,  1990,  Fairchild Semiconductor
 Corporation, San Jose Facility.

 Canonie Environmental.  February 20, 1991.  Fax
 from Mr. Dennis Curry, Project Manager Ground-
 water Extraction and Treatment Program, Fairchild
 Semiconductor Corporation, San Jose Facility.

 Regional Water Quality  Control Board. January
 1989.    Order  Number  89-16^  Site  Cleanup
 Requirements   for   Fairchild   Semiconductor
 Corporation   and   Schlumberger   Technology
 Corporation, Santa Clara  County.

 Schlumberger Technology Corporation.  February
 1989.  Annual Status  Report January 1, through
 December 31,  1988, Fairchild  Semiconductor
 Corporation, San Jose Facility.

 Schlumberger  Technology  Corporation.    June
 1989.     Pilot  Reinjection   Study,  Fairchild
 Semiconductor Corporation, San Jose Facility.

 Schlumberger Technology Corporation.  February
 1990a. Annual Status Report January 1, through
 December 31,  1989, Fairchild  Semiconductor
 Corporation, San Jose Facility.

 Schlumberger  Technology  Corporation.    May
 1990b.    Quarterly  Status  Report January 1,
 through March 31, 1990,  Fairchild Semiconductor
 Corporation, San Jose Facility.

 Schlumberger Technology  Corporation.   August
 1990c.  Quarterly Status Report April I, through
June   30,   1990,   Fairchild   Semiconductor
 Corporation, San Jose Facility.
                                                  69

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                                                   UPDATE OF CASE STUDY 7
                                                                   General Mills
                                                        Minneapolis, Minnesota
Abstract

The extraction system in both the shallow aquifer (five wells) and the underlying Carimona
Member Aquifer continued to operate through 1989, despite some operational problems later
in the year. The capture zone induced in the shallow aquifer since 1985 was maintained in
1989. TCE concentrations remained above cleanup standards in the shallow aquifer in some
areas, and  were considerably above  standards and increasing  in a  broad  area  of  the
Carimona Member Aquifer.  TCE concentrations in the Magnolia Member did not meet
standards. A  final decision to install an extraction system  to remediate this contamination
was made by  the MNPCA in 1990.  Residual sources such as DNAPLs are suspected by
MNPCA  regulators, but DNAPLs have not been observed directly.
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
Late 1985
Trichloroethylene
Tetrachloroethylene
1,1,1 -Trichloroethane
Glacial drift over fractured
sedimentary rock
6
390 gpm
110 acres
50 feet
Trichloroethylene 2,300 ppb
                                       70

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                                CASE  STIIDY UPDATE
                                   GENERAL MILLS

                           BACKGROUND OF THE PROBLEM
            INTRODUCTION

This  report describes  events  and  progress  in
remediation at the General Mills site through late
1989.  It is an update of the original case study
(U.S. EPA, 1989, Case Study 1), which presented
background information  and data from  ground-
water monitoring and extraction systems through
1988.

The  General Mills site is located approximately
1 mile northeast  of  the Mississippi  River on
Hennepin Avenue on the outskirts of  downtown
Minneapolis. Figure 1  shows the site location.
Site  contamination is  a result of disposal  of
chemical solvents  in a soil  adsorption pit  located
near the  southeast corner of the former  General
Mills property. The disposal occurred between
1947 and 1962,  when the  site was owned by
General Mills, Inc.   In 1981,  the  Minnesota
Pollution Control Agency (MNPCA) was apprised
of site contamination.

General Mills, Inc.,  and  MNPCA are  jointly
pursuing  site  cleanup  under a 1984 Response
Order by Consent  Operation of a ground-water
extraction and treatment system began in 1985 and
has functioned continuously  since then, exclusive
of routine maintenance  and repair.

Four  aquifers  underlying   the General  Mills
property  are   pertinent  to  aquifer  remediation
efforts at  the site-the  shallow aquifer,  the
Carimona and Magnolia Members of the Platteville
Formation, and the St. Peter Sandstone.

The shallow unconsolidated aquifer (also known as
the glacial drift aquifer) is unconfined and flows
southwest toward the Mississippi River.  A layer
of glacial till and the Decorah Shale, when present,
separate  the   glacial  drift  aquifer  from  the
underlying bedrock aquifer.   The layers  impede,
but do not prevent  downward  flow of  ground
water to lower  aquifers.
The   Carimona  Member  of  the  Platteville
Formation  underlies   the  glacial  aquifer  and
consists of three to four feet of fractured  and
weathered micrite, a fine-grained limestone.  The
piezometrie surface in  the Carimona is relatively
flat.  The Carimona Member is separated from the
underlying Magnolia Member by a thin bentonite
layer  that  impedes downward  flow.    In  the
northern portion of the site, the hydraulic head in
the Carimona Member is  on average 4 to 5  feet
higher than the head in the  underlying Magnolia
Member,  thus  indicating   the   potential  for
downward flow.  However, there appears to be a
net upward vertical gradient between the Magnolia
Member and the overlying Carimona Member in
the vicinity  of wells  ZZ and  13, and  in  the
southern portion of the site.

The Magnolia Member of the Platteville Formation
is approximately 8 feet thick.  Ground water in the
Magnolia Member flows to the northwest.  Below
this  aquifer  is a 22-  to 27-foot  thickness of
alternating layers of shale, limestone, and dolomite
that impedes  the downward ground-water flow.
The head difference between this aquifer and the
underlying St.  Peter Sandstone is 55 feet with a
downward flow.

The primary ground-water contaminants at the site
are  chlorinated  organic  solvents,   including
trichloroethylene (TCE), tetrachloroethylene (PCE),
1,1,1-trichloroethane (TCA),  and the degradation
products of these compounds. The most prevalent
compound detected was TCE,

Ground-water  contamination is  highest  in  the
glacial drift and Carimona aquifers with respective
maximum TCE concentrations of 1,300 ppb (Well
B, 1986) and 2,300 ppb (Well WW, 1985). Lesser
TCE concentrations were  found in the Magnolia
Member (440 ppb in Well ZZ, 1986),  and in the
St. Peter Sandstone (160 ppb in Well 200,  1987).
                                              71

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                                                                       General Mills
                                           Former General Mills  ^
                                           Disposal PK         ^
             1000     o    icoo    woo     1000    «no    woo    sea?    TOW mr
                                                                      (Poor Quality Original!
Source: USGS, 1972. % Paul West Quadrangf*.
Minnesota, 7,5 Minute Series (Topographic)
Figure 1
SITE LOCATION MAP
GENERAL MILLS SFTE.MWNEAPCL i
                                       72

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                                                                                General Mills
            UPDATE ON SITE
           CHARACTERISTICS

 The updated case study  is based  on 1989 data
 obtained   from   the   MNPCA,  consisting  of
 extraction  well  pumping  rates,   contaminant
 concentrations, and technical specifications for an
 additional pumping system.  File correspondence
 between MNPCA and General Mills, and personal
 communications   with   MNPCA   personnel
 supplemented the technical reports.  The MNPCA
 continues  to oversee  remediation activities at the
 General Mills site.

 Ground-water  elevations  were  measured  during
 April, July, and  October  1989,  for the following
 aquifers: Shallow Glacial Drift Aquifer, Carimona
 and Magnolia Members, St. Peter Sandstone, and
 the Prairie du Chien and Jordan formations.  The
 April 1989 ground-water  levels in  the  shallow
 aquifer, the Carimona Member, and the Magnolia
 Member  are  shown   in  Figures 2,  3,  and 4.
 Ground-water levels  in the these three aquifers
 remain consistent with  those levels found in the
 original  case  study.    The  surface  elevation
 monitoring data collected during  1989  also suggest
 hydraulic  gradients similar to those identified in
 1988.

 During  1989, ground water at the General Mills
 site was tested to determine the concentration of
 both  chlorinated and  non-chlorinated  volatile
 solvents. As identified in  the original  case study,
 TCE remains the most prevalent compound in the
ground water.

TCE concentrations in the shallow aquifer, the
Carimona  Member,  and  the Magnolia  Member
remained above consent order threshold levels at
several monitoring wells in  1989  (Barr,  1990).
According  to  the  original consent  order, General
Mills was  required to install an extraction system
in  the  Magnolia when  TCE  levels surpassed
27 ppb.

The detection of TCE above 27 ppb in upgradient
Magnolia  wells indicates  that the  General  Mills
site is not  the only source of contamination in the
Magnolia   Member.    Although  the  MNPCA
determined the proposed Magnolia system would
capture  contaminated  water  in  the Magnolia
aquifer in the area of the former adsorption pit, the
agency concluded that the Magnolia extraction
system would capture only a small portion of the
plume in the  Magnolia Member.  The  MNPCA
eventually  decided  to  proceed   with  system
expansion  in  October 1990,  even though  the
source of contamination in the Magnolia Member
remains  unknown.  The  notification  to proceed
with the installation of the system was received by
General Mills on January 15, 1991.

              REMEDIATION

        Design and Operational
       Features of Remediation
                  System

The goals of remediation, as stated in the Consent
Order, are  to minimize  further  migration of
volatile organics, particularly TCE,  and to reduce
TCE  concentrations to less than 270 ppb  in the
shallow aquifer and to less than  27 ppb  in the
underlying Carimona and Magnolia Aquifers.

The remediation system at the General Mills site
consists of two separate extraction systems-one
onsite andime downgradient. Both systems began
operating in November 1985.  The onsite system
includes three extraction wells-two in the shallow
aquifer  (Wells 109  and 110)  and one  in  the
Carimona Member (Well  108).  Since operation
began in 1985, the combined average  withdrawal
rate for 109 and  110  has been  70 gpm, and the
extraction rate for the Carimona well has varied
between  20 and  30 gpm.     Three   additional
extraction wells are located downgradient from the
site in the shallow aquifer system (Wells 111, 112,
113);  the combined extraction rate has historically
been about 300 gpm.

According to the water-level data from the original
case study, pumping rates of about 50 gpm at each
of the shallow-aquifer system  wells  (109,  110,
111,  112, 113)  would result in a capture  zone
extending 100 feet on either  side of the well.  The
earlier case study reported site data showing that
the three shallow downgradient wells produced a
wide capture zone, but the two shallow source-area
wells  produced limited capture zones. In a map of
the plume distribution in the original case study, it
appears that the 270-ppb TCE contour falls within
the originally identified capture zone.  Therefore,
the wells appear to be  limiting the extent of the
plume. Data obtained from 1988 pumping tests in
the Carimona indicate that a similar 50 gpm rate in
the Carimona Member  would produce a capture
zone extending beyond the monitoring wells.
                                               73

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                                                                      General Mills
                                               FORMER DISPOSAL-
                                               SITE

   //
  3TJ!
  ••«/(

  /.  '/
    Glacial drift monitoring well or site and
    downgraded pump-out WeH

    Water tabte contour (MSL)

    Estimated capture zone
                           10CO
Source: Barr, 1990
Figure 2
WELL LOCATIONS AND WATER LEVELS
IN THE SHALLOW AQUIFER, APRIL 1389
GENERAL MILLS SUE
                                         74

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                                                                    General Mills
                                               —FORMER DISPOSAL

Ul
w
£
*^

5
€






<0
(•
£
«M
1
Ul
i!
i
s :
I
ft

 ^    Carimona Member W«H

827 3   Carimona Pottntiomitric Surfac*
      Elevation (MSL)

 NM   Not Measured
                                                          Elm SI SE| I
Source: Barr, 1990
Figure 3
WELL LOCATIONS AND WATER LEVELS IN
CARIMONA MEMBER, APRIL 1989
GENERAL MILLS SITE  .
                                       75
                                                          HDS

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                                                                        General Mills
                       FORMER DISPOSAL
                       SITE
 (A)    Magnolia M*nb*rW«H

820.5 '  Magnolia Pot«ntiom«tric Surface Elevation (MSL)

       Magnolia Pot«nttom«tric Surface Contour (MSL)
                                      ICO
                                      	I
                                                                           Seal* i" '«•<
Source: Barr, 1990
Figure 4
WELL LOCATIONS AND WATER LEVELS IN
MAGNOLIA MEIISER, APRIL 1989
GENERAL MILLS SUE

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                                                                                  General Mills
 The extraction rates in the five shallow extraction
 wells  and  in  the one extraction well  in  the
 Carimona  were  reduced during parts  of 1989
 because  of pump malfunctions.  In the original
 case study, it was reported that the extraction wells
 for these systems operated continuously between
 1985 and  1988,  except for general maintenance
 downtime.  The extraction-well systems continued
 to operate during 1989; however,  electrical and
 mechanical  problems with system pumps resulted
 in downtime and  reduced extraction rates for both
 the shallow aquifer and Carimona Member.

 The 1989 combined average  monthly  withdrawal
 rate of the shallow source-area Wells 109 and 110
 was 75 gpm in 1989  (Barr 1990).  Although  the
 wells were operated at  maximum sustainable yield
 during most of 1989, extraction rates decreased to
 51 gpm during  the last 3 months of 1989 because
 of pump failures in both wells.

 The average  extraction rate  in  1989  for  the
 downgradient  wells  (Nos.  Ill,  112,  113)  was
 290 gpm, with  the  average  monthly rates  for
 individual wells ranging from 90 to 107 gpm.  The
 shallow downgradient system removed  150 million
 gallons of ground water in 1989.  A total volume
 of  42 million  gallons  of  ground  water  was
 removed from the shallow aquifer by  the source-
 area wells  (Nos.  109,  110) in 1989 (Barr 1990).
 Table 1  displays  the  average monthly  pumping
 rates and downtime at individual wells.

 In the Carimona  Member,  source-area Well 108
 continues to  withdraw  water as  part  of  site
 remediation.    Its  purpose  is  to  contain  and
 remediate ground water in the Carimona Member
 in areas  where  concentrations  of TCE exceed 27
 ppb. The average pumping rate for Well 108 was
 16 gpm in 1989.   A total volume of  8.7 million
 gallons  of ground water was  removed from  the
 Carimona Member in  1989.  This rate is reduced
 from 1988 yields  due to mechanical and electrical
 problems associated with Well  108, which resulted
 in 46 days of downtime in the last 3 months of
 1989.

No  major  modifications  were  made  to   the
extraction system in 1989.  In October 1989,  the
 MNPCA decided  to expand the extraction system
 into  the  Magnolia Member  of the  Platteville
Formation.    This  decision  was  postponed,
however,  so that  the  MNPCA  could review
remedial-action    alternatives   to"   ground-water
extraction (MNPCA  Correspondence  to General
MiUs, 1990).  In the first three quarters of 1989,
MNPCA personnel explored the possibility of soil
removal, but determined that contamination  had
migrated from the  soil  profile  into  the ground
water.  In  October  1990, the MNPCA approved
implementation of the proposed Magnolia system
as  the remedial alternative  which  represented
optimal use of remedial action  funds (MNPCA,
1990b).

After   the  MNPCA   selected   ground-water
extraction as the most feasible remedial alternative,
General Mills  submitted a work plan detailing the
methodology used to collect the hydrologic data.
The major analytical considerations  in designing
the Magnolia  extraction system  include aquifer
tests and capture-zone design, both of which are
still in the planning  stage.

Two  aquifer tests will be conducted  in both the
Carimona and Magnolia Members of the Platteville
formation.  The results will provide hydraulic data
on: (a) the  degree of hydraulic separation between
the Carimona and Magnolia members, (b) storage
coefficients and transmissivity of the Magnolia and
Carimona members,  (c) vertical hydraulic gradients
between  Magnolia  and  Carimona members,  and
(d) the  location  of  recharge   and  discharge
boundaries, if any  (General Mills,  1989).   The
aquifer tests require construction of two wells to
provide water-level data necessary to design  an
effective extraction system.

The extraction system,  and its resulting capture
zone, will be designed using an analytical ground-
water model  that will  be  calibrated  with  data
obtained from  the aquifer tests.  Modeling wiU be
conducted  using  the analytic element flow-code
SLAEM  (Strach, 1989).    The  model  will  be
calibrated to the observed steady-state piezometric
surface of the  Magnolia Member.  Model results
are  intended   to  provide  data  on:   (a) the
effectiveness of Well 108  in containing ground
water in  the Magnolia Member,  (b) the optimum
locations and  pumping  rates for  the extraction
wells,  (c) the  number  of  wells  required for  a
Magnolia extraction system,  and (d) the effects of
pumping in the Magnolia member on the vertical
hydraulic  gradients  between the Magnolia and
Carimona members (General Mills, 1989).
                                                77

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                                                                             General Mills
Table 1
1989 PUMPING RATES

Jan 1989
Feb 1989
Mar 1989
Apr 1989
May 1989
Jun 1989
Jul 1989
Aug 1989
Sep 1989
Oct 1989
Nov 1989
Dec 1989
Glacial Drift Pump-Out Well
Pumping Rate
(Ave. GPM)
109
41
51
47
57
50
49
48
202
8.21
O.O2
162
452
Source: Barr, 1990.
110
29
50
55
44
50
50
50
51
51
442
252
232
111
91
91
91
91
91
90
90
90
90
90
90
90
112
101
104
105
1061
1061
104
105
107
104
106
106
106
113
92
92
92
91
92
92
92
92
92
93
93
93
Carimona Pump-Out
Well
Pumping Rate
(Ave. GPM)
108
22
20
20
20
21
20
19
18
19
5.62
5.62
122

lFlow meter malfunction.
2Wells not pumping full-time due to faulty motor control.
      EVALUATION OF SYSTEM
            PERFORMANCE

            Shallow Aquifer

Total  VOC concentrations increased from April
1988 to April 1989, in four of the nine monitoring
wells  in the shallow aquifer.   TCE  contaminant
levels did not meet cleanup standards in shallow
monitoring Wells 3 and S in April  1989. Table 2
compares the  total VOC/TCE concentrations for
monitoring periods in 1984, 1^87, 1988,  and 1989.
These data  show  that  total  VOC  and  TCE
concentrations have generally decreased from 1984
to 1989 in most of the nine wells shown, but have
increased in Wells S and W.  Total  VOCs  have
also  increased in  well  1,  although  TCE  has
decreased.   In Well  V,  concentrations of  total
VOCs and  TCE decreased only  slightly.  The
increase in Well W suggests that the portion of the
plume  downgradient  and beyond the  zone of
capture of the shallow extraction system may be
migrating to the southwest across  Well W.   The
time series trend of TCE concentrations in several
monitoring wells, some of which are not listed in
Table 2, are shown in Figures 5, 6, and 7.

           Carimona Member

TCE  and  total  VOC  concentrations   in  the
Carimona  Member  are  also shown  in  Table 2.
Data presented in the initial case study showed
that TCE levels greater  than 27 ppb  extended at
least 250  feet from  source area in the north  and
800 feet or more to the south  and east  in 1988.
TCE concentrations increased from April 1988 to
April 1989 in all the monitoring wells  listed in
Table 2, except BB and RR. These data show  that
                                             78

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                                                     General Mills
                          Table 2
          TOTAL VOC AND TCE CONCENTRATIONS (ppb)
SHALLOW AQUIFER AND CARIMONA MEMBER WELLS/1989 AND EARLIER
SHALLOW AQUIFER*

WeU
B
Q
S
T
V
w
1
3
4
12/83 to 2/84
VOC/TCE
NA/1987
56/<1.3
850/770
BDL/<1.3'
100/78
11/7.5
NA/27 .
NA/800
NA/380
4-87
VOC/TCE
840/800
101/2.6
710/650
BDL/<0.2
180/160
34/24
3.2/2.7
810/740
130/120
4-88
VOC/TCE
a360/330
6.2/0.86
520/460
BDL/<0.50
180/160
67/43
ND/<0.50
480/440
60/55
4-89
VOC/TCE
270/250
13/1.1
910/860
BDU<0.50
140/130
86/57
8.6/0.80 I
350/320
58/55
CARIMONA**

WeU
108
BB
RR
SS
UU
ww
8
9
10
11
12
13
12-83/1-84
VOC/TCE
1300/1100
NA/1400
NA/33
NA/<1.5
NA/81
NA/1700
NA/96
NA/<0.50
NA/2.6
NA/120
NA/1.5
NA
4-87
VOC/TCE
510/450
1200/1100
120/110
17/1.2
12/12
310/290
97/86
6.5/5.1
130/120
160/160
BDL/<0.2
150/140
4-88
VOC/TCE
230/200
580/530
240/220
ND/<0.50
25/23
360/320
170/160
9.3/4.5
62/56
89/79
ND/<0.50
1.2/<0.50
4-89
VOC/TCE
570/530
390/340
220/180
21/1.3
51/38
540/530
420/380
17/9.8
170/160
120/110
ND/<0.50
J20/110
Source: General Mills, 1990; U.S. EPA, 1989; General Mills, 1991.
BDL=BeIow Detection Limits
NA - Not Available
*=TCE contaminant goal reduction level= <270 ppb
**=TCE contaminant goal reduction level= < 27 ppb |
                            79

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Source: Ban. 1990
                                                       Date
FiguraS
HPSTOHY OF TCE CONCENTRATION VARIATIONS IN
SHALLOW AQUIFER WELLS 3,4,8 AMI R
GENERAL HULLS SITE
L)

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oo
                  .a
                  &
                  CO
I
O
O
O
           Source:  Bear. 1990


                                                                       Date
                                                                     Figures
                                                                     HISTORY OF TCE CONCENTRATION VARIATIONS
                                                                     IN SHALLOW AQUIFER WELLS 1, B. AND V.
                                                                     GENERAL MILLS SITE

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       8

       g
       o
            tt-
Source: Barr. 1990
                                                     ^




                                                         Date
FIGURE?

HISTORY OF TCE CONCENTRATION VARIATIONS

IN SHALLOW AQUIFER WELLS G, T, AND X.

GENERAL MILLS SITE

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                                                                                  General  Mills
the  area  of  the  27-ppb  TCE  plume  in  the
Carimona Member appears  to  have  increased
considerably from 1988 to 1989.

According to the 1989 Annual Report for the site,
the effectiveness  of extraction  in  the  Carimona
Member  is  reflected  by a  70 to  90 percent
reduction in TCE  concentrations in most  of the
Carimona monitoring  wells since  startup (Barr,
1990). Water levels in 1989 also showed that the
capture zone established in 1985 continued to be
successful  in containing  contaminated  ground
water through  1989 (General Mills, 1991).  Time-
series plots presented in Figures 8 and 9, however,
show that while TCE concentrations continued to
decline in monitoring Well BB from 1988 to 1989,
contaminant levels  increased in extraction Well
108 and monitoring well WW.  In Well 108, TCE
concentrations remained above the target goal  of
less than  27 ppb in 1989.  TCE concentrations for
Wells 10, 11, and  13 on the southeastern periphery
of the plume also increased from April 1988  to
April 1989.  In April 1988, TCE levels in Well 13
were below the detection limit, but they increased
to 110 ppb by April 1989. Because of problems
in 1988 with laboratory quality-control equipment,
results were too low and thus, incorrect (General
Mills, 1991). If 1988 data are adjusted upward to
correct these potential  errors, some of the TCE
concentrations would  then appear to  have been
stable during 1988.  Nonetheless, a comparison of
1987  and   1989  data  in Table 2  shows  that
concentrations rose in several  monitoring  wells
from  1987 to 1989.  System operators contend
that, despite  these  increased concentrations,  the
contaminant plume is being contained.

Table 3  lists  the TCE concentrations detected  in
1989  and early 1990  in the  influent  to effluent
from the source-area treatment system.  These data
show that   influent  concentrations  were  stable
during this  period, except  for  December 1989
when influent levels decreased  to below effluent
levels (General Mills,  1991).   In the first three
quarters  of  1989,  the  effluent released after
treatment by air stripping  was consistently below
27 ppb, a 96 percent average treatment efficiency
for total VOCs. Due to electrical and mechanical
failures   in  the  Well 108 (Carimona  Member)
pump, system operators   recorded  46 days  of
downtime in the  last 3 months  of 1989.   Total
VOC levels in the effluent rose from 20 ppb in the
third  quarter to  200 ppb  in  the fourth quarter.
Additional  sampling in  January  1990  revealed
96 ppb TCE,  which is still  above the NPDES
maximum allowable average of 50 ppb and only
slightly  below the daily 100 ppb allowable daily
concentration.

Influent and effluent data are also displayed as a
time-series plot in Figure 10.  This figure shows
that, although  1989 concentrations of TCE were
higher than those in 1988, the TCE  concentration
of the influent  continued to  decline,  especially
compared to 1985 and 1986 concentrations.  The
December  1989  sampling  event   (Table 3),  in
which  the concentrations in  the  effluent were
higher than in  the influent, is not included in this
figure.

The Carimona  extraction system was shut down in
January   1990   because   of  elevated   VOC
concentrations.   Inspection  of  the air  stripper
revealed calcium carbonate  encrustation  on  the
interior  of the tower (Barr,  1990).  The  stripper
tower  was  cleaned  and the system  resumed
operation on April 19, 1990.

According  to  the 1989  Annual Report  for  the
General Mills  site,  water-level data obtained for
the Carimona  Member cannot be used to assess
the true capture zone of this system because of the
low observed  hydraulic gradients at the site and
the absence of monitoring points away from the
site.

            Magnolia Member

TCE  concentrations in  the  Magnolia Member
fluctuated from  1985  to 1989. Figure 11 shows
TCE contaminant levels ranging from more than
400 ppb to below the 27 ppb standard.  Although
TCE  concentrations  are  still  above the  consent
order  standard of 27 ppb, they appear to have
stabilized  well below the  levels first detected in
1985 and 1986. Sampling results from April, July,
and  October  1989,  revealed an  average TCE
concentration of 73 ppb.

The capture zone in the Magnolia has yet to be
determined, and will be estimated using  the results
of the aquifer  tests in the Magnolia and Carimona
aquifers, and  the calibrated ground-water model
that is based on the aquifer test results.
                                                83

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                                                    General Mills
                         Table 3
      TOTAL VOC AND TCE CONCENTRATIONS (ppb)
IN THE INFLUENT TO AND EFFLUENT FROM THE SOURCE-
           AREA TREATMENT SYSTEM IN 1989
                    AND EARLY 1990*
                        Influent
1-89
VOC/TCE
390/390
4-89
VOC/TCE
480/440
7-89
VOC/TCE
380/380
12-89
VOC/TCE
150/140
1-90
VOC/TCE
380/380
                         Effluent
1-89
VOC/TCE
9.8/9,8
4-89
VOC/TCE
18/13
7-89
VOC/TCE
20/20
12-89
VOC/TCE
200/1901
1-90
VOC/TCE
96/962
Source: General Mills, 1990; U.S. EPA 1989.

TCE contaminant reduction level goal = <27 ppb
Sample results received on January 15, 1990, indicated treatment
 system upset.
2Upset confirmation sample collected on January 16, 1990, and data
 received on January 19,1990.
*Influent water is a composite of shallow extraction Wells 109 and
 110 and deeper Carimona extraction Well 108.
                               84

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 00
r\
                 I
                 (0
                 g
                 I  "-1
                 O
                 O
           Source: Barr. 1990

                                                                   Date
FIGURES
HISTORY OF TCE CONCENTRATION
VARIATIONS IN CARMONA MEMBER
WELLS BB, 108, AND WW.
GENERAL MILLS SITE
O
O

-------
 oo
O
^
-4
                 o
                 O

                                                                     Date
           Source. Bur. 1990
FIGURE 9

HISTORY OF TOE CONCENTRATION VARIATIONS

IN CARMONA MEMBER WELLS 10,11, AND 13.

GENERAL MILLS SITE

-------
DO
-J
               B
               s
              •3
                                                                                                          DSCHRG

                                                                                                          INF

                                                                                                          EFF

                                                                                                          BMDL

                                                                    Date
        Source. Banr. 1990.
Figure 10
HISTORY Of TCECOMCENTRAT10N VARIATIONS IN
THE SOURCE-AREA TREATMENT SYSTEM INFLUENT
AND EFFLUENT
GENERAL MILLS SITE
O

-------
 OQ
 oo
O
6^
-^

-4
                I
                ¥
                2

                1
      o
      O
                     •tw-
Source: Barr, 1990,
                                           W-U'"'*^
                                               •      »Wwl      I       ******      1      3.SJP8      I

                                                         Date
Figure 11

HISTORY OF TCE CONCENTRATION

VARIATIONS IN THE MAGNOLIA WELLS

ZZ.DD.ANDVV
GENERAL MILLS SITE

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                                                                                 General Mills
    SUMMARY OF REMEDIATION

The  two  General  Mills  extraction  systems
continued to  operate in 1989,  but, in the fourth
quarter extraction rates were reduced because of
electrical and mechanical problems and elevated
concentrations in the source-area treatment system.
The construction of an extraction system in the
Magnolia Member was required by the MNPCA in
1990.

During  1989, average  extraction rates  in  the
shallow-aquifer extraction system decreased due to
electrical and mechanical malfunctions.   Water
levels in  the shallow-aquifer source area wells are
consistent with those identified in 1988, suggesting
that the capture zone established in 1985 has been
maintained through 1989.  TCE concentrations in
monitoring Well W downgradient of the extraction
wells increased from 1984 to 1989, suggesting that
the uncaptured downgradient portions of the plume
may be migrating to the southwest.

Reduced  pumping rates were also documented in
the Carimona Member extraction system during
1989. The limited-radius capture  zone identified
in 1985-86  was maintained until the fourth quarter
of 1989,  when electrical and mechanical failures
occurred  in the extraction system, further reducing
the limited capture-zone boundaries identified in
the original case study.  Limited capture is further
indicated   by  substantial  increases  in  TCE
concentrations in peripheral monitoring wells in
the Carimona from 1984  to 1989.   These data
suggest that the plume in the Carimona is getting
larger, despite extraction.

No major changes were made in the remediation
program; however, a decision was made in 1990 to
construct an  additional extraction system in  the
Magnolia  Member   because   historical  TCE
concentrations did not meet the  cleanup standard.
High   concentrations   triggered   renewed
consideration  of soil removal around the former
disposal pit and an assessment of the  sources of
the Magnolia contamination.  To date, the source
of  contamination   in  the  Magnolia  remains
unknown. MNPCA staff are unsure how this will
effect the remediation goals of restricting further
contaminant  migration and  improving  ground-
water quality.

Residual  contamination  in the form of NAPLs and
an adsorptive  layer of peat beneath the disposal pit
are still suspected by MNPCA staff to be potential
sources   of  contamination.     Because  water
contained in the aquifers is not used for a water
supply   and   contaminant-removal  costs   are
prohibitive,  additional   detection   efforts   and
remedial actions are not planned for either type of
suspected contamination.

Because  of the continued suspicion that residual
sources  of  contamination may be present at the
site, it appears unlikely that cleanup goals will be
achieved in the foreseeable future  in any of the
contaminated aquifers.

   SUMMARY OF NAPL-RELATED
                  ISSUES

The staff of the MNPCA suspect that DNAPLs are
present  at the  General Mills  site.  This appears
probable because of the nature and quantity of the
waste materials, the reported  means  of disposal,
and the persistence  of the contaminant plume in
spite  of more  than  5  years  of  remediation.
However, direct observation of nonaqueous liquids
in the subsurface has not been reported.

Chlorinated  solvents,  in quantities  of  up  to
1,000 gallons  per year, were poured into a small
pit for approximately 15 years.  If it were assumed
that  10,000 gallons  were  disposed  of  in  that
period,  the  total mass  of chlorinated  solvents
would be approximately 100,000 pounds. Figure 4
of the original  case study (U.S. EPA, 1989) shows
a map of the  total  dissolved VOC plume in the
shallow aquifer as it was estimated from field data
collected in March 1984, before the  start of
remediation. Assuming a retardation coefficient of
5 (reasonable for a sandy glacial drift), a porosity
of 0.25, and a saturated  thickness of 20 feet,  this
plume would contain approximately 3,000 pounds
of dissolved and adsorbed VOCs.  A substantial
portion of the remaining 97,000 pounds of solvents
may be present as a DNAPL.

Although no estimates  of the mass of contaminants
removed by   the  extraction   wells  have been
presented in the data reports, a rough  estimate
based   on    reported   pumping    rates   and
concentrations  would  be  200  to 400 pounds per
year.  At this  rate,  the system would take more
than  200 years to remove  the total  mass of
contaminants  thought  to  be present.   It is  not
surprising, therefore, that ground-water monitoring
at the site shows persistently high concentrations
in some areas. The primary  waste  constituent,
TCE, has an aqueous solubility of 1,100,000 ppm.
                                                   89
                            60(077

-------
This is much higher than the highest ground-water
concentrations  reported at the  site (2,300 ppb).
However,  it is  very common at  sites known to
have  DNAPLs  to  find  that  the  maximum
ground-water concentrations are far less  than the
aqueous solubilities of the contaminants.

It should be noted that soil concentrations of up to
2,000 ppm were reported  for TCE when  the soils
removed from  around  the  disposal pit  on the
General Mills site were sampled.  Although, the
sorption properties  of these soils have not been
measured,  it is  likely  that any ground water in
contact   with   them    would   have    solute
concentrations near the solubility limit.

      UPDATE  BIBLIOGRAPHY/
             REFERENCES

Barr  Engineering  Company.   May  8,  1989a.
Correspondence from  Peter  J. Sabee to  Kathy
Kramer, Minnesota  Pollution Control Agency.

Barr Engineering Company.  August 18, 1989b.
Correspondence from  Ray  W. Wuolo to Mark
Schmitt,   Minnesota Pollution Control  Agency,
Saint Paul, Minnesota.

Barr Engineering Company.  January 1990.  1989
Annual  Report:  General Mills  East Hennepin
Avenue Site. Minneapolis,  Minnesota.

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.

General Mills,  Inc.   1989.   Magnolia Aquifer
Testing Work Plan:  2010 East Hennepin Avenue
Site.

General Mills,  Inc.   May 30, 1991. Letter from
Peter Sakee to Jennifer Sutler of the EPA.

Minnesota Pollution Control Agency (MNPCA).
October 29, 1990a.  Correspondence from Rodney
E.  Massey, Director,  Ground  Water  and Solid
Waste Division  to William Taylor, General Mills,
Inc.

Minnesota  Pollution  Control  Agency,  Ground
Water  and Solid  Waste Division. October 29,
1990b. Internal  Memorandum from Mark Schmitt,
Re: Magnolia Aquifer Pump-And-Treat System.
                            General Mills

Minnesota Pollution Control Agency.  November
16,  1990c.     Personal   communication  with
Frederick Campbell, Hydrologist, Superfund Unit,
Site Response Section.

Minnesota Pollution Control Agency.  January 2,
1991.   Personal  communication  with  _  Mark
Schmitt,  General  Mills Site  Project  Manager,
Minnesota  Pollution Control  Agency, Ground
Water and Solid Waste Division.

Strach, 0. D. L. 1989.  Groundwater Mechanics.
Prentice Hall, Englewood Cliffs, New Jersey.
                                                  90

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                                                  UPDATE OF CASE STUDY 8

                                                          GenRad Corporation
                                                        Bolton, Massachusetts
Abstract

Ground-water extraction downgradient of the east plume has continued since late 1987 with
a 3-month down period each winter.   Contaminant concentrations  over most of the east
plume area have decreased since the extraction system began operating in  1987.  Ground-
water extraction  has not been initiated in the highly contaminated north plume.  The
migration  of the plume  is limited because it  discharges  into Great Brook.   Although
concentrations of contaminants in the north plume have decreased, concentrations remain
above drinking-water standards over most of the plume.
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
1984
Late 1987
VOCs
Glacial sand, silt, and gravel
2
40 gpm
10 acres
20 feet
Trichloroethylene >
5,000 ppb
                                      91
<5D3

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                                CASE STUDY UPDATE
                             GENRAD CORPORATION

                           BACKGROUND OF THE PROBLEM
            INTRODUCTION

This  report describes  events  and progress in
remediation at the GenRad Corporation site from
December 1988 through November 1990.  It is an
update of the original case study, which was based
on data from mid-1984  through late 1988 (U.S.
EPA, 1989, Case Study 8).

The  GenRad Corporation site is a manufacturing
plant  located   in   Bolton,    Massachusetts,
approximately  25 miles   west  of  Boston   (see
Figure 1).   Scientific and medical equipment are
manufactured   at  the plant,   resulting  in  the
generation  of  waste  sludge   containing  metal
hydroxide  and  wastewater  containing  industrial
solvents.    Prior  to  1984, these  wastes  were
discharged directly to a sludge-drying bed and a
surface impoundment. As a result of this practice,
the soil  and ground water at the site have been
contaminated  with volatile organic compounds
(VOCs), principally trichloroethylene (TCE),  The
site   remediation   is   administered   by   the
Massachusetts   Department  of   Environmental
Protection (DEP).

The problem was first discovered  in 1984 when a
ground-water  investigation performed  to  comply
with RCRA requirements for closure of the waste
management facility demonstrated that the ground
water was  contaminated  with  VOCs.    The
contamination was found in two separate areas—a
western plume centered near the sludge-drying bed
and an eastern plume emanating from the surface
impoundment  (see Figure 2). Beginning in 1984,
contaminated  soil  and  sludge were  removed,
underground storage tanks were  excavated and the
waste treatment facility was closed and demolished
in an effort to remove  the various sources of
contamination. Further investigation revealed that
the western plume had not migrated far, but that
the eastern plume originating  from the surface
impoundment  had migrated offsite approximately
600 feet.   Operation of  a long-term remediation
system to  extract and  treat   the  contaminated
ground water  in this eastern plume began in late
1987.
The   GenRad  facility   is   underlain  by
unconsolidated glacial  deposits  and metamorphic
bedrock.   The thickness of the unconsolidated
deposits is highly variable, but in general a 15- to
20-foot-thick unit of sand and gravel, present at
the  surface  over  most  of the  site,  overlies
approximately  11 feet of glacial till. In low-lying
areas, several feet of organic sediments overlie the
sand  and  gravel deposit at the surface.  The
bedrock that  underlies the  glacial till  was not
penetrated  deeply  during  monitoring  well
installation at the site; however, it is known to be
slightly to moderately fractured metamorphic rock.
The bedrock surface is  irregular and slopes to the
northeast toward Great Brook.  The slope of the
bedrock surface northeast of Great Brook was not
reported.

The permeable sand and gravel deposits act as an
unconfined aquifer at the site.  The transmissivky
of these permeable sediments was measured and
estimated to be between 350 and 10,000 ft2/day.
The  transmissivity of the fractured bedrock was
not reported in the original source documents but
was   estimated  to-   be   comparable  to  the
transmissivity  of the glacial till,  that is, low in
relation to the  sands and gravei.  However, some
water-supply wells in the area are installed in the
fractured bedrock.  The depth to water ranges from
0 to 20 feet but is generally  approximately 5 feet
The horizontal direction of  ground-water flow is
easterly, with flow to the east-northeast in the area
of the  former sludge-drying bed and to the
southeast in  the  area  of  the former  surface
impoundment.  The horizontal transport velocity of
the ground water  was  estimated to  be  between
0.05  and 0.08  feet/day.

The  two plumes of VOCs are oriented  in the
predominant directions  of ground-water flow: that
is, the north plume is oriented to the east-northeast
and the east plume is  oriented to the southeast.
The  primary contaminant of concern within the
two   plumes   is  trichloroethylene  (TCE),  but
secondary contaminants include 1,1-dichloroethane,
methylene chloride, 1,1-dichloroethylene, trans-1,2-
dichloroethylene,   1,1,1 -trichloroethane,
tetrachloroethylene, and vinyl chloride.
                                              92
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                                                                  GenRad Corporation
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                                                                                GenRad Corporation
One key characteristic of the north plume is that it
appears to have migrated only a short distance
from its original source location.  The explanation
for the lack  of  lateral migration  reported  by
GenRad's  consultant is that Great Brook acts as a
hydraulic barrier to the northeastward migration of
the north  plume.   Cross  section A-A'  in  the
original case study appeared  to show that Great
Brook  was a gaining stream  that would  form a
hydraulic barrier to ground-water flow by acting as
a sink  to  contaminated ground water.  However,
concentration contours presented  in  the original
case study show contamination northeast of Great
Brook,  indicating  that Great  Brook  may  not
consistently  act as  a  hydraulic barrier to ground-
water flow, possibly because of seasonal lowering
of the  water table.   Nonetheless,  it appears that
contaminated ground  water from the north plume
discharges to Great Brook at least part of the year
and   that  Great    Brook   generally   inhibits
contaminant migration northeast of this drainage.
Because of  the lack of migration,  there is  no
remediation    system    in   place   to   extract
contaminated ground water from the north plume.

In contrast to the north plume, the east plume had
migrated  substantially  from  its original source
location by early 1987.  This  migration is further
complicated   by the  fact  that  the  plume  has
migrated  offsite across  both  city   and  county
boundaries.     For   this  reason,  ground-water
extraction   at  the  GenRad  site  has  focused
exclusively on  remediating contaminated ground
water   in  the  east   plume.     The   maximum
concentrations of total VOCs in the north and east
plumes in  1986 were approximately 5,000 ppb and
1,000 ppb, respectively.

            UPDATE ON  SITE
          CHARACTERISTICS

The   information  on  site   history,  geology,
hydrogeology,  waste  characteristics,  and   the
administration of remediation  presented  in  the
original case study   remains  current in  most
respects.  Some additional data about  the geologic
and hydrogeologic characteristics of the area near
Great Brook have been  gathered in a  1990  study
of bedrock conditions (GZA,  1990b).   One of the
findings of this 1990 study was that Great Brook
appears to follow a line of bedrock  fractures as
shown  by  regional fracture trace analysis.  During
the bedrock investigation, three deep bedrock wells
and two  associated  shallow   overburden  wells,
referred to as Series  VI monitoring  wells,  were
installed  near  Great Brook.   Water  level data
collected from well pairs near Great Brook in 1990
showed that the vertical gradient was downward at
well pair G-VI-1A7B at some distance from Great
Brook,  and upward  at  well pair  G-VI-3A/B
adjacent to Great Brook.  This pattern of vertical
gradients is  consistent with the  conclusion that
Great Brook  is a gaining  stream that receives
direct discharge from the area of the north plume.
The  hydraulic  conductivity   of  the  fractured
bedrock was also  measured in 1990.  The con-
ductivity was low, less than  0.02 feet/day, near G-
VI-1B at a distance from Great Brook, but was
low to moderate, 0.01 to 5.5 feet/day, near G-VI-2
and G-VI-3B,  adjacent to  Great  Brook.   The
higher conductivity near Great Brook is consistent
with the higher fracture densities expected in that
area.     More  complete   information on  site
characteristics  can  be  found in the original case
study.

              REMEDIATION

        Design  and Operational
       Features of Remediation
                  System

The objectives  of  remediation of  the east  plume
were  to  prevent  further   offsite  migration  of
contaminants  and  to clean  up the contaminated
ground  water  to  drinking-water  standards.  No
actions, beyond source  removal,  were taken to
remediate the north plume because it was believed
that "natural dilution" would remediate the ground
water in this area without a significant degradation
of the surface water quality in Great Brook. The
east plume  extraction system  consists of  two
extraction  wells   (PW-B   and PW-C)   located
approximately  100  feet apart near the eastern limit
of  the  east  plume.   The well  locations  and
pumping rates  were chosen based on computer
modeling   and  hydrodynamic   response  data
gathered from  testing a pilot extraction well, PW-
A, installed as part of Phase I of the remediation.
The total design pumping rate of the two existing
Phase II extraction  wells is 40 gpm (GZA, 1990a).
The system was  designed  to be shut off for
3 months each  year during  the coldest period of
the winter. The two extraction wells discharge to
an  air stripper treatment system.  The effluent
from the air stripper is discharged to two recharge
trenches on the eastern boundary of the site, south
of the east plume  (GZA, 1990a).   Each quarter,
16 monitoring  wells are sampled  to monitor the
                                                95

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                                                                                GenRad Corporation
progress of remediation and the migration of the
plume.  Hie Phase n extraction system has been in
operation since late  1987.

 EVALUATION OF PERFORMANCE

The  ground-water  elevation  contours  at  the
GenRad site  in  November  1989 are shown in
Figure  3.  These  data show  that the two-weE
extraction system is effective in capturing ground
water over a broad area of the sand and gravel
aquifer.  Specifically, it appears that contaminated
ground  water from the entire eastern  plume  is
being captured by the  existing extraction  system.
Ground  water from   the  north  plume  is  not
captured.  This result is consistent "with the water-
level  data  from  an  extraction  period in October
1987  presented  in  the original case study  (not
shown).  The  practice of recharging treated ground
water  to  two trenches south  of  the  surface
impoundments has changed the direction of flow
near  the surface impoundments  from  southeast
before  recharge  began to  northeast afterwards.
This  effect  is  probably  due  to ground-water
mounding in  the area  of recharge.  Water level
contours suggest that  this  ground  water  turns
southward and is captured by the extraction system
over time.

The concentrations of total  VOCs at the GenRad
site in  November  1989 are shown  in  Figure 4.
Comparison of Figure  4 to the early 1987  data
shown in Figure 2 shows that the concentrations of
total VOCs in the east plume decreased from early
1987  to November  1989.   The reduction  of the
size of the 100 to 500-ppb plume and its migration
away from the surface impoundment from early
1987  to November  1989 are both indications of
this  reduction.  Figure 4  also  shows that the
western two-thirds of the east  plume  migrated to
the northeast,  whereas the contaminated area south
of  the  extraction wells  migrated to  the  north.
These patterns of plume migration are consistent
with the directions of horizontal ground-water flow
observed during periods of extraction in 1988 and
1989.

Three trends  in the  shape of the  north plume are
evident  in  comparing Figure 4 to the early 1987
data for total  VOCs presented in  Figure 2. From
early  1987 to November  1989,  it appears  that:
(1) the'  upgradient  edge   of the north  plume
migrated to the northeast away from  the original
source  area,  (2) the downgradient edge  of the
north  plume  continued to  be limited  by Great
Brook, and  (3) the north plume  became wider.
These  three  characteristics  suggest  that  the
contaminated ground water in the sand and gravel
aquifer is dispersing laterally as  it migrates to the
northeast toward  a discharge zone along Great
Brook.

The results of the October 1990 sampling of the
Series VI  monitoring  weEs, consisting  of  three
bedrock wells  and two associated shallow wells,
are shown in Table 1 and Figure 5. These results
show that VOC contamination in the north plume
was more extensive in the bedrock aquifer than in
the sand and gravel aquifer in late 1990. Although
only these three  bedrock sampling points  were
available in late 1990, it is clear from comparison
to Figure 4 that the contamination in  the bedrock
is  more   extensive   both   upgradient   and
downgradient of the existing plume  in  the sand
and gravel aquifer.  The concentration of total
VOCs is greatest in G-VI-2, located 200 ft down-
gradient of the sludge-drying bed.  This result is
notable bectase vertical gradients are expected to
be  upward,  not  downward,  at  this  location.
Although  all three existing  bedrock  wells  show
some    contamination,    the   fuE   extent  of
contamination  in  the  bedrock  has  not  been
characterized to date.

Figure 6 shows the concentration of TCE in  north
plume wells G-III-14A and G-HI-14B from mid-
1984 through November 1990.  This  well pair is
located  on the south bank  of Great  Brook near
bedrock well G-VI-2 at the downgradient eastern
tip of the 500-ppb plume. The  figure shows that
the concentration  of TCE in shallow well G-III-
14A decreased steadily from the  time of source
removal  in  1984 through early 1988, and  then
remained  steady  from early 1988  through late
1990.  The  overall decrease may be due to the
relatively efficient discharge of the shallow ground
water to Great Brook.

Figure 6 also shows that the concentration of TCE
in deep well G-III-14B decreased from 1984 to
early  1989,  and  then increased from early  1989
through  late  1990.  This later increase may be due
to the migration of the highly contaminated renter
of the plume toward Great Brook.  The increases
seen in the spring sampling periods in  1988,  1989,
                                               96

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                                                              I


                                                             1987
 I  '  '


1988
                                                                     1989
1990
                                                                                            1991
                                                                  YEAR
                                                                          Figure 6

                                                                          COI«ZI*TliAt!OM OF TCE W G4IM4A

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                                                                                GenRad  Corporation
Table 1
TOTAL VOC CONCENTRATIONS IN SERIES VI MONITORING WELLS,
OCTOBER 17, 1990
Well
G-VI-1A
G-VI-1B
G-VI-2
G-VI-3A
G-VI-3B
Interval
Upper Sand and Gravel
Fractured Bedrock Aquifer
Fractured Bedrock Aquifer
Upper Sand and Gravel Aquifer
Fractured Bedrock Aquifer
TCE
(ppb)
<1
960
3,700
<1
25
Total VOCs
(ppb)
<1
1,009
3,748
<1
61
and 1990 occurred after the system was shut down
temporarily  during  the  cold  months.    The
concentration of TCE in the deeper interval of the
sand and gravel aquifer remained high (2,000 ppb)
at the end of 1990.  The slower rate of discharge
to Great  Brook  from  deeper intervals of  the
aquifer may result in a slower rate of reduction of
the  TCE  concentration  than  over   shallower
intervals;   however,   because   of   higher
concentrations, the reductions in contaminant mass
may still be significant.

Figure 7 shows the concentrations of TCE in east
plume shallow well PT-4 from  early 1987 through
November   1990.     Well   PT-4  is   located
approximately  200 feet   west  of  the  south
extraction well, PW-B.  The figure  shows that the
concentration   of  TCE  in   PT-4  decreased
substantially  from  340 ppb  in May   1988 to
110 ppb in November  1988, and then decreased
slightly  to 100 ppb through November 1990. This
substantial initial  reduction in  TCE concentration
was  probably  due to  the startup  of the nearby
extraction system  in late 1987.

Figure 8 shows the  concentration of TCE  in  the
influent to the  air stripper from December 1987
through  October  1989.    The  concentration
decreased from 31 ppb in December 1987 to 5 ppb
in December 1988, and then increased to 21  ppb at
the end  of  October  1989. The concentration was
highly variable over this entire period. The reason
for the increase after December 1988 is unknown.
    SUMMARY  OF REMEDIATION

Ground-water extraction downgradient of the east
plume  has continued  since late  1987 with a 3-
month  down period  each winter.  The east plume
extraction system has  continued to contain and
capture contaminated ground water from the east
plume  since 1988, despite the winter down period.
Concentrations over most of the east plume area
have decreased since the extraction system began
operating  in late 1987.  A considerable reduction
in the size of the 100 to 500-ppb plume, probably
due to the extraction  system, has been observed
since system startup.  Some northeastern migration
of the  western two-thirds of the plume has been
observed,  but it is expected that this ground water
will  be captured in the future  by the existing
extraction system. It is expected that several more
years will be necessary to clean up all of the east
plume  to drinking-water standards.

No extraction of  ground water in  the  highly
contaminated  north  plume  has  been  initiated
because of the  limited migration of the  north
plume  because of its  direct discharge to  Great
Brook. The eastward migration of the north plume
has continued to be  limited by  Great Brook since
late  1988.    The  eastward  migration  of the
upgradient edge of the plume and the widening of
the plume both suggest that  the contaminated
ground water in the sand and gravel aquifer in this
area continues to migrate away from its original
source  and toward Great Brook.  Some decrease in
overall concentrations, has been observed; however,
                                               101

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 I
1988
 1
1989

 YEAR
 I
1990
                                                                                          1991
                                                                       Figura?
                                                                       CONCENTRATION OF TCE IN PT-4 (EAST PLUME)
                                                                       GENRADSITE
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                8
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                                 1988
 I
1989
                                                               YEAR
                            1990

Figure 8
CONCENTRATION OF TCE IN THE INFLUENT TO
THE AIR STRIPPER
GENRAD SITE
-4
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                                                                             GenRad Corporation
concentrations   of   contaminants   remain
considerably above drinking-water standards over
most of the north plume.  Concentrations of VOCs
were  found to be  significantly  greater  in the
bedrock aquifer than in the sand and gravel aquifer
during sampling in 1990.  The natural cleanup of
the north plume to  drinking-water standards via
ground-water discharge to Great Brook is expected
to take many years, and may take decades.

   SUMMARY OF NAPL-RELATED
                 ISSUES

The presence of nonaqueous phase liquid (NAPL)
contamination  at the GenRad  site has  not  been
reported to date. The relatively low concentrations
of contaminants  in  the  east plume  and the
significant  progress  in  concentration reduction
from  early  1987 to late  1989 suggest that this
plume consists  of dissolved VOC constituents that
do not have a NAPL source.

There  is a possibility of  some  dense  NAPL
(DNAPL) contamination in the north plume.   The
concentrations  of total VOCs in the north plume
are considerably higher than in  the  east plume,
particularly  at depth.  The location of the highest
concentration of contaminants in the lower part of
the sand and gravel aquifer, as well as in the frac-
tured  bedrock  that  underlies  it, may  be  an
indication    of   some   amount   of   DNAPL
contamination.   For example in well pair G-VI-
3A/B, located adjacent to the  sludge-drying bed,
the concentration  of total  VOCs was less  than
1 ppb at the top of the sand and gravel aquifer and
1,009 ppb within the underlying fractured bedrock
aquifer in October 1990.  This difference may be
caused by a DNAPL lens of halogenated organics
that has descended through  the sand and gravel
aquifer and pooled within the  fractured bedrock.
The highest concentration of total VOCs within the
bedrock (3,748 ppb) was  measured  in  G-VI-2,
which  is  in a location  where a high  fracture
density is expected.  If DNAPLs are present, they
would have  the potential to migrate downward
through the  abundant fractures in this area, despite
upward hydraulic gradients.  Additional  wells
would need to be  installed in  the  bedrock to
investigate the extent of  bedrock contamination
before the possibility of DNAPL contamination
can be confirmed.

The increases in VOC concentrations  observed in
spring of 1988, 1989, and  1990 occurred after the
system had been temporarily shut down during the
winter  months.  This increase may indicate that
residual sources such as DNAPL are present hi the
area.

       UPDATE BIBLIOGRAPHY/
              REFERENCES

Goldberg,  Zoino  & Associates,  Inc.,   (GZA).
March  1987. File  No. 3863.6.

GZA.     February 14,   1990a.     Letter   to
Massachusetts  Department  of  Environmental
Quality   Engineering:      Monthly    Report
November 1, 1989 to December 1, 1989.

GZA.  November 29,   1990b.     Letter   to
Massachusetts  Department  of  Environmental
Protection:   GenRad  Bolton  Facility  Bedrock
Exploration Program.

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.
                                              104
                   585

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                                                   UPDATE OF CASE STUDY 9

                                                             Harris Corporation
                                                              Palm Bay, Florida
Abstract

Remediation systems at the  Harris facilities  and. General  Development  Utilities  (GDU)
continue  to extract contaminated ground water.  The introduction of extraction Well GS-
131S in mid-1988 has enhanced the effectiveness of the shallow extraction system in the
Harris south campus. However, some contaminated ground water still extends beyond the
shallow zone of capture.  The area of the deep plume has been reduced since system startup
in 1985.   Concentrations of total VOCs  in  the influent to both the Harris  and GDU
treatment systems decreased significantly after startup but have remained relatively stable in
the last 3 to  4 years.
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
1982
April 1984
VOCs
Sand and shell with
clay layers
24
310 gpm
60 acres
90 feet
Total VOCs 37,
120 ppb
                                       105

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                                CASE STUDY UPDATE
                              HARRIS  CORPORATION

                           BACKGROUND OF THE PROBLEM
             INTRODUCTION

This  report  describes  events  and  progress in
remediation at the Harris  Corporation site from
early 1989 through January 1991.  It is an update
of the original case study, which was based on
information from  1984 through  February 1989
(U.S. EPA, 1989, Case Study 9).

The  Harris Corporation  site is located in the town
of Palm Bay, Florida, The site encompasses three
facilities:  the Harris Semiconductor facility in the
northern part of the site  (the Harris north campus),
the  Harris Government Systems facility  in the
central part of the site (the Harris south campus),
and the autonomous General Development Utilities
(GDU) water and wastewater treatment facility in
the southern part of the site (see  Figure 1),  The
main activity  of   the  north  campus  is  the
manufacture of electronic components, especially
semiconductors   and   other   microelectronic
components.  The activities of  the south campus
have  varied since  the  facility  was occupied by
Harris, in  1967,  but have  included electroplating,
photoprocessing,  painting, and computer hardware
assembly.   The  GDU  facility  includes a water
treatment plant that produces the drinking water
for Palm Bay, a  wastewater treatment  plant, and
several water supply wells,

Overall site remediation of the three facilities was
administered  by  the  Florida  Department  of
Environmental Regulation  (FDER),  but  is now
administered  by  Region IV  of  the  U.S.  EPA
(FDER,  1991).

Ground-water contamination was  first discovered
in March  1982 after samples collected from the
Finished water of the GDU water treatment plant
were  found to  be contaminated with  volatile
organic compounds (VOCs).  Subsequent actions
at the GDU facility included;  (1) sampling of all
18 water supply  wells, leading to  the termination
of pumping in five contaminated wells in April
1982; (2) startup  of  a  prototype  air stripper
treatment system  at the GDU facility in November
1982, and  of a  permanent full-scale system in
April 1984; and (3) restoration of  four of the five
wells to full production after the GDU treatment
system began operation.

Following a period of site assessment and planning
from 1982  through  late  1984, a separate  Harris
ground-water extraction and air stripper treatment
system was  installed and began operation  at the
Harris south campus in two stages  during 1985.
In May 1985, four deep  wells near  the boundary
with GDU  (GS-123D, GS-124D,  GS-125D,  and
GS-127D), a system  of 10 shallow weUpoints near
Building 5,  and the  Harris air stripper treatment
system, began operation.  In September  1985,
three additional deep wells (GS-35D, GS-37D, and
GS-43D) and three additional shallow wells (GS-
35S, GS-37S, and GS-43S), all located in me area
of highest contamination near Building 6, were
added  to the extraction  and  treatment system.
Later changes to the system through 1988 included
the replacement of the 10-wellpoint system with
two  conventional  extraction wells  (GS-44S  and
GS-18S) in mid-1987, and the addition of shallow
extraction Well GS-131S  to the three existing
shallow extraction wells in June 1988,

Five main geologic units underlie the Harris/GDU
study area. These five units, in order of increasing
depth are: (1) a 42-foot  thick unit of sand, silty
sand, and sandy silt that contains shells  in  the
bottom 5 to  10 feet; (2) a 22-foot-thick clay unit
that acts as a leaky aquitard; (3) a permeable sand
unit  which occurs from depths of 65  to 95 feet;
(4) the Hawthorne Formation, a low permeability,
clay-confining unit  with  a thickness  of 100 to
200 feet; and (5) the  Floridan aquifer, a 1,000-foot
unit of limestone and dolomite.

The two aquifer zones of concern are the shallow
silty sand unit and the deeper permeable sand unit
of the surflcial  aquifer (units 1 and 3 above).
These two zones are referred to, respectively, as
the shallow-aquifer  zone and the  deep-aquifer
zone, and wells  within these units are referred to
as "shallow"  and "deep,"  The general direction of
horizontal  ground-water  flow  is  to  the  south-
southeast in  the shallow-aquifer zone  and  to the
southeast in the  deep-aquifer zone.  A downward
vertical head gradient exists between the two
                                              106
                    SD5   VM1

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                                                                 Harris Corporation
       HARRIS SEMICONDUCTOR
      HARRIS GOVERNMENT
      SYSTEMS
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                                                        GENERAL SPTE LOCATION MAP
                                                        HARRIS CORPORATION SITE
                                                        PALM BAY, FLORIDA
                                          107
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                                                                                Harris Corporation
aquifer  zones, especially in  the  vicinity of the
extraction and production wells.

Volatile   organic  compounds  are   the   main
contaminants  of concern.  The VOC plume is
made up of several constituents, including Trans-
1,2-dichloroethylene  (Trans- 1,2-DCE),
trichloroethylene (TCE), vinyl chloride, methylene
chloride, and  chlorobenzene.  The main plume of
total VOCs extends diagonally northwest-southeast
across most of the south campus.  The highest
total VOC concentrations are found southeast of
Building 6 in the east-central part of the south
campus.  Some of the potential, but unconfirmed,
sources  of  ground-water   contamination  are
corroded storm sewer  lines, solvent sumps, leaking
industrial pipelines, drum storage areas, drainage
ditches, and several waste ponds and neutralization
lagoons in both the north and south campuses.

           UPDATE  ON SITE
          CHARACTERISTICS

The  information on  early site history,  geology,
hydrogeology, administration of remediation, and
waste characteristics and sources presented  in the
original case study is  believed to be current. One
minor change is that the south campus is now
referred to as  the Electronic Systems Sector (ESS)
campus in some  site  documents.  More complete
information on site characteristics can be found in
the original case study (U.S. EPA, 1989).

             REMEDIATION

        Design and  Operational
       Features of  Remediation
                 System

When the initial case study was written, there were
two separate extraction and treatment systems—one
operated  by Harris in the south  campus, and a
second operated by GDU. The objectives of the
GDU remediation system are to provide drinkable
water for  public consumption  and  to prevent
contamination from migrating  to uncontaminated
production wells.  The GDU system consisted of
four production wells  (GDU-2B, GDU-3, GDU-5,
and GDU-8)  that discharged  to  an  air stripper
treatment system. Treated water from this system
is blended with water from uncontaminated GDU
production  wells, and then  treated again  using
conventional water treatment technology.
The objectives of the Harris remediation system
are to clean up the aquifers underlying the Harris
site to meet established standards and to prevent
additional GDU production wells  from becoming
contaminated. Currently, the Harris south campus
remediation system consists of 11 extraction wells
and  an  air  stripper  treatment  system.   The
extraction wells are located in 4 areas in the south
campus.   These are: (1) three deep  barrier wells
(GS-123D, GS-124D,  and  GS-125D)  near  the
Harris/GDU  property  boundary,  (2) two deep
(GS-50D and  GS-43D) and two shallow  (GS-50S
and  GS-43S)  wells near  the main  body  of the
plume   southeast   of  Building 6,  (3) one deep
(GS-127D) and one shallow (GS-131S) well in the
parking  lot area  between  Building 6  and  the
Harris/GDU  property   boundary,  and
(4) two shallow wells (GS-18S and GS-44S) near
the northeast plume near Building  5.  Two former
extraction wells, GS-37S and GS-37D, were taken
out of production  in August 1990,  and  replaced
with GS-50S  and GS-50D,  which  are  located
200 feet  west of the GS-37 wells.  This change
was  made because of the low production of the
GS-37  well cluster and  was intended to  improve
plume capture to the west.  The Harris remediation
system in operation at the end of 1990 is shown in
Figure  2.  The shallow wells are screened near the
bottom  of the  surficial  silty  sand unit from
approximately 33  to 38 feet,  and  the deep wells
are screened from  68 to 78 feet in the permeable
sand  unit  underlying  the clay  aquitard.   An
extensive  system  of monitoring wells has been
installed  in both   the  north and  south  Harris
campuses.  Ground-water samples from  a select
number of these wells are collected  and analyzed
for VOCs each quarter.

The  GDU remediation  system  has not been
modified extensively  since early  1989.   In  the
original case  study, it  was  reported that only
four GDU production wells  (GDU-2B,  GDU-3,
GDU-5, and GDU-8) were connected to the GDU
treatment  system.   Recent documentation states
that three additional wells (GDU-4, GDU-6, and
GDU-7)  were also discharging to the treatment
system in early  1990 (GDU, January 16,  1990).
The date of the addition of these three wells was
not reported.  The average pumping rate  of the
entire GDU production well network in December
1989 was 4.3 million gallons per day, or 3,000
gpm (GDU, 1989). The seven  wells discharging
to the GDU air stripper produced an average  of
0.7 million gallons per  day  or  490 gpm during
December 1989.
                                                 108
                     SC5

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Modified After  CH2M HILL, 1986
                                                                                       Hgur»2
                                                                                       HARRIS CORPORATION REMEDIATION
                                                                                       SYSTEM, LATE 1990
                                                                                       HARRIS CORPORATION SITE
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 The  configuration  of  the  Harris  south  campus
 remediation system was changed in August  1990,
 with  the replacement of GS-37S and GS-37D with
 extraction  Wells GS-50S  and  GS-50D.    The
 influent flow rate to the Harris air  stripper in late
 1990 was  approximately 260 gpm, slightly less
 than  the rate of 281  gpm in late-March  1987
 reported in the original case study (Geraghty &
 Miller,   January 25,   1991b).     The   Harris
 remediation did experience two interruptions of
 service in 1989 to provide for system maintenance.
 These periods of shutdown  were from March 3 to
 April 21 (Harris, June 20, 1989), and for a 4-week
 period  during  May 1989  (Geraghty  & Miller,
 November  30, 1989).

 Other remedial activities at the Harris/GDU site
 were the installation and startup of a second Harris
 remediation system in the north campus area and
 preparations   for   additional   extraction  near
 Building 100,  west  of Troutman Boulevard.  The
 north campus  remediation system was completed
 in July 1990. It consists of 1 deep and 12 shallow
 extraction  wells  that discharge to a  small  air
 stripper. The treated water is  discharged to the
 north  campus industrial  wastewater  treatment
 plant.  The extraction system  borders the  large
 north campus retention pond on the south and east,
 as shown in Figure 2.   The combined extraction
 rate   of  the   system  was  estimated  to  be
 approximately 25 gpm  in late 1990 (Geraghty &
-Miller,  1991a). Total VOC concentrations in the
 influent to  the north campus air stripper decreased
 from 1,430 ppb on  June 28, 1990,  to 637 ppb on
 October 31, 1990, probably as a result of the north
 campus extraction system.

 Harris Corporation is currently preparing to initiate
 additional   ground-water   extraction   near
 Building 100.  The  proposed system, described in
 a  1990 feasibility study/remedial action plan, is
 expected to consist of three wells that will extract
 ground   water from  the   40-foot  zone  near
 Building 100   (Geraghty   &  Miller,   1991b).
 Ground-water   modeling    simulations   were
 performed  to determine appropriate pumping rates
 and extraction well spacings for the system, which
 is expected to extract a total of  30 gpm.   The
 water would be treated using the  existing  south
 campus air stripper. Two  new monitoring  wells
 were installed  west  of Clearmont Street southwest
 of Building 100 in January  1990.  As of June
 1991, construction of the proposed Building 100
 extraction system was awaiting FDER approval.
                              Harris Corporation

  EVALUATION OF PERFORMANCE

 Figure 3   shows   average   1990   total  VOC
 concentrations   in  the  shallow-aquifer   zone
 superimposed  on  a  contour  map   of  the
 potentiometric surface of the shallow-aquifer zone
 on January 4, 1991. The capture zones associated
 with the three areas of  shallow  ground-water
 extraction are also shown.  The extent of capture
 is similar to that of late March 1987, illustrated in
 the original  case  study,  except that extraction
 Well GS-131S  has extended  the  overall zone of
 capture   considerably   downgradient   from
, Building 6. Comparison of the average 1990 total
 VOC isopleths to  the approximate capture zone
 shows that almost all of the areas of ground-water
 contamination with greater than 50 ppb total VOCs
 were being captured by  the  existing  system in
 December 1990. The 100 ppb plume southwest of
 Building 100 was not being captured in December
 1990; however, planned extraction activities in this
 area are expected to rectify this deficiency.  The
 distribution of ground-water contamination in areas
 with concentrations less than 50 ppb is not shown
 in Figure 3; however, some areas of ground-water
 contamination  with concentrations  of  less than
 50 ppb were probably outside  the capture zone of
 the shallow extraction system in December 1990.

 Figure 4  shows  the average  1990  total VOC
 concentration isopleths  in  the  deep-aquifer zone
 superimposed  on  .a  contour  map   of  the
 potentiometric  surface of the deep  aquifer for
 December 1990.   The approximate limit of the
 capture zone of the central control  wells and the
 barrier  wells  is also shown.  These data show that
 the most of the deep plume was being captured by
 the deep extraction wells in December 1989.  The
 plume is generally narrower and smaller than the
 1987 plume  presented in  the original case study,
 indicating  progress in ground-water remediation.
 The areas of contaminated ground-water south of
 the barrier  wells were  apparently not  being
 captured  by the  Harris  remediation  system in
 December 1990. This relationship was also shown
 by the  1987  isopleths of total  VOCs presented in
 the original case study.  As before,  it is expected
 that the portion of the plume not captured by the
 Harris  extraction  system will be  captured  and
 treated  by the GDU production well and treatment
 system.    The   distribution   of  ground-water
 contamination with concentrations less than 50 ppb
 is not shown in Figure 4.  However, the capture
 zone shown in Figure 4 did not encompass the
                                                   110
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1990 50 ppb isopleth, so it is expected that most
or  all  of  the  low-concentration contamination
upgradient  of  the barrier  wells  would  also be
contained by the Harris system.

Figure 5 is  a time series plot of the concentrations
of total VOCs in  the influent to the Harris south
campus air  stripper from early May 1985 through
October 1990.   These  data show a significant
decrease in  total VOC concentrations from 1985 to
the end of  1988.  Concentrations from early 1988
through late 1990 were essentially stable except
for   a  concentration   peak   in  mid-1989.
Approximately 80 percent of the increase in total
VOC loading in mid-1989 can be attributed to the
central control wells  (GS-37S,  GS-37D, GS-43S,
and GS-43D) but some increased loading was also
observed in the barrier  wells (Geraghty & Miller,
November 30,  1989).  This increase may have
been caused by system shutdowns for a combined
total of 2 1/2 months in March, April, and May
1989.   The'fact  that little actual  downgradient
plume migration  has occurred since startup,  as
shown by  comparison of early plume maps (not
shown) with Figures 3 and 4,  suggests that  the
increase was not  due to plume migration during
shutdown.   The repair of the pump in GS-43D in
May 1989,  after a period of minimal pumping of
the highly contaminated central plume area, may
have contributed to the increase.

The concentration of total VOCs in the influent to
the GDU air stripper from April 1984,  through
January 2, 1991, is shown  in Figure 6. The time
series shows a significant initial decrease in  total
VOC concentrations followed by a period of stable
concentrations  of  approximately 60 ppb  during
1986.  This was  followed  by  a third period  of
stable  concentrations  in the range of 10-15 ppb
from early 1987'through the end of 1990.  It is not
known  when   the  three  low   concentration
production  wells   were added  to  the  influent
stream.

    SUMMARY OF REMEDIATION

Remediation systems at the GDU and  Harris
facilities continue to extract contaminated ground
water.  The effectiveness of the shallow extraction
system in the Harris  south  campus was enhanced
significantly by the introduction  of GS-131S  in
mid-1988, as shown by comparison of data in the
original case study with that of Figure 3.  Some
contaminated  shallow  ground  water  south  of
GS-131S in the  main  plume continued to be
beyond the  shallow  capture zone  in  December
1990.   Remediation  of the north  campus  total
VOC plume south of the retention pond began in
mid-1990, and has shown some progress to date.
The shallow plume southwest of Building 100, in
the area west of the south campus, is not currently
being captured.  However,  an  extraction system
designed to remediate this plume is expected to be
approved by the FDER and constructed in 1991.

The size of the deep total  VOC plume has been
reduced by  the  extraction  system  since system
startup in  1985.  An area of contaminated ground
water south  of the barrier  wells continues to be
beyond the capture zone of the Harris extraction
system, but  within the capture  zone of the GDU
production wells that discharge to  the GDU air
stripper.   Concentrations  of total VOCs in  the
influent to both  the  Harris and GDU treatment
systems  decreased  significantly  after  startup.
However,  influent concentrations in both systems
have been relatively stable in the last 3  to 4 years.

   SUMMARY OF  NAPL-RELATED
                  ISSUES

The presence of dense non-aqueous phase liquids
(DNAPLs) at the Harris/GDU site is not currently
suspected.     However,   some   characteristics
observed at  the Harris/GDU site may suggest the
possible  presence  of DNAPLs.    One of  the
characteristics  of  DNAPL   contamination  is  the
persistence of high concentrations of contaminants
over long periods despite efficient extraction rates.
The persistence of total VOC  concentrations  of
approximately  1,000  ppb  in the  influent to  the
Harris air  stripper observed  since early 1988  may
be  an  indication  of  an   abundant   source  of
contaminants.     This  source   of  dissolved
contaminants could be a DNAPL pool; however,
the source could also be contaminants adsorbed
onto soil particles  in  both the  saturated  and
unsaturated  zones.     Significant  increases  in
ground-water contamination after periods of no
pumping  are  another  indication  of DNAPL
contamination.   A  three-fold  increase in  the
concentration of the composite of the four central
control wells near Building  6 was observed from
March  1 to July 26, 1989, after  periods of system
shutdown  from March  3 to April 21   and for 4
weeks  in May.  Neither the persistence of  high
concentrations nor the observed concentration peak
                                                  113
                      5U

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8
8
                     1886
                                      1987
                                                      1988

                                                      YEAR
                                                                       1988
                                                                                       1990
                                                                       Figures
                                                                       CONCENTRATIONS OF TOTAL VOCs IN THE INFLUENT
                                                                       TO THE HARRIS SOUTH CAMPUS AIR STRIPPER
                                                                       HARRIS CORPORATION SITE
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     500
     400  -
     300
u
u

o
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      200  -
          1384
1991
1992
                                                                    Figures

                                                                    CONCENTRATIONS OF TOTAL VOCs IN THE INFLUENT

                                                                    TO THE GDU AIR STOPPER

                                                                    HARRIS CORPORATION SITE
                                                                                                                    I
                           a
                           o

                           1

                           I
                           3

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                                                                              Harris Corporation
 following a period of shutdown are proof of the
 presence of DNAPLs at the Harris/GDU site. A
 longer period of observation is necessary before
 the potential for  DNAPL  contamination  at  the
 Hanis/GDU site  can  be  assessed  with greater
 confidence.

       UPDATE BIBLIOGRAPHY/
             REFERENCES

 CH2M  HELL.  April  1986. ' Assessment  of the
 Harris Corporation Remediation Program.

 Florida Department of Environmental Regulations.
 May 22, 1991.  Letter to Jennifer Sutter  of the
 U.S. EPA.

 General Development Utilities (GDU). December
 1989.  Water Treatment Plant Operation Report.
 December 1989.

 GDU. January 16, 1990. Letter from Jose Peralta
 of GDU to Karen 'Knight of Tfibaseo, addressing
 request  for  1989 operational data on  GDU
 production wells.

 Geraghty & Miller.  November 30, 1989.  Letter
 to Robert Sands, re:   Response to GDU/CH2M
 HILL Letter Concerning  the July  1989 Weekly
 Analysis Report.

 Geraghty &  Miller. '  January 1991a,   Harris
 Corporation Semiconductor Complex  Remedial
Action Report.

Geraghty & Miller. January 25, 1991b.  Letter to
Robert Sands of Harris, re:  FDER Review of
Building 100 FS/RAR

Harris  Corporation.   June 20, 1989.   Monthly
Status Report, April/May  1989, letter to FDER
from Robert Stands.

Post,  Buckley,   Schuh,    and Jernigan,   Inc.
December 1983.   Harris Corporation Task  B-4
Hydrogeologic Study.

U.S. Environmental  Protection  Agency  (U.S.
EPA).   October 1989.  Evaluation of  Ground-
Water Extraction  Remedies:  Volume  2,  Case
Studies 1-19, Interim Final.  EPA/9355.4-03.
                                                116

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                                                 UPDATE OF CASE STUDY 10

                                                                   IBM-Dayton
                                                           Dayton, New Jersey
Abstract

Between  1978 and 1984, a system of up to 20 ground-water extraction wells was operated
with the goal of aquifer remediation. After pumping was stopped in 1984, the plume of
ground-water contamination began to reemerge.  Residual dense nonaqueous-phase liquids
(DNAPLs) were determined to be the cause, and a new system of wells for plume reduction
and control was designed.  The  new system began operating  in late 1990.  As yet, not
enough performance information is available  for judging its effectiveness.
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
March 1978
Volatile Organic Compounds
Sand and silt with clay layers
21 (Original system)
4 (New. system)
1,000 gpm (Original system)
100 gpm (New system)
60 acres
80 feet
1,1,1-Trichloroethane 9,590 ppb
Tetrachloroethylene 6,132 ppb
                                      117.

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                                CASE STUDY UPDATE
                                      IBM-DAYTON

                           BACKGROUND OF THE PROBLEM
             INTRODUCTION

 This  report discusses events and progress in the
 remediation of the IBM-Dayton facility from early
 1989 through November 1990.  The report is an
 update of the original case study, which was based
 on data collected through the end of 1988 (U.S.
 EPA, 1989, Case Study 10).

 The  IBM-Dayton  site is  in  South Brunswick
 Township,  New Jersey, just west of the town of
 Dayton (see Figure  1).  Until 1985,  IBM-Dayton
 was  a  manufacturing  facility  whose activities
 included producing  computer  punch cards  and
 inked ribbons  for printers.  The facility is  now
 used  for administrative activities and repairing
 electronic equipment.  Past  site activities resulted
 in  the contamination of  local ground water by
 chlorinated  organic  solvents.    Site  remediation
 continues to be under the jurisdiction of the New
 Jersey Department  of  Environmental Protection
 (NJDEP).

 The problem was first discovered in December
 1977, when contaminants were detected in a Sooth
 Brunswick  Township production well (Well  SB-
 11).  The  NJDEP determined that  IBM-Dayton
 was one of the major contributors to ground-water
 contamination  at SB-11.   IBM determined  that
 chemical-storage tanks  near Building 001  (see
 Figure  2)   were the  likely   sources  of  the
 contamination originating from the IBM site.

 Operation of tBM's  first ground-water extraction
 well  began in March  1978.    By 1984,  the
 remediation system consisted  of   14   onsite
 extraction wells and 7 offsite extraction wells.  For
 a short period in 1982, nine onsite injection wells
 were also operated.  In September 1984, pumping
 in the extraction wells stopped after the plume was
 reduced to the area  around  the   source;  the
judgment was that additional pumping would not
 reduce the  plume   further.   At that time,  the
 ground-water remediation  system wa$ reduced to
 only a well  head treatment system on water  supply
 Well  SB-11.   Eight, months  after  the  onsite
 remediation system was terminated, water-quality
 monitoring   showed  renewed.  growth  of  the
contaminant plume; by 1986, the plume had spread
to the downgradient property boundary.  In early
1989, the NJDEP approved IBM's long- term plan
for ground-water extraction  and  monitoring  to
contain  the contaminants near their onsite source,
and  final  peimits  were obtained in September
1990.   Well  testing and intermittent  start-up
pumping  of  the  three  onsite  wells  began  in
October 1990, and continuous pumping of the new
system began in November 1990.

The   site  is  underlain  by about  110 feet  of
unconsolidated deposits—primarily formations  of
silty sand, gravely sand, or clay—above bedrock.
Two  interconnected aquifers  are involved in the
grotind-water  contamination problem.  They are
(1) the  shallow unconflned aquifer consisting  of
the Pensauken Formation {Pleistocene; silty  sand
with  occasional  zones of gravel)  and the Old
Bridge Sand member  of the  Magothy Formation
(Cretaceous;  silty  sand);  and  (2)  the  lower
semiconftned aquifer consisting of the Farrington
member of the  Raritan Formation  (Cretaceous;
sand  with  gravel).   These  two  aquifers  are
separated by the Woodbridge Clay member of the
Raritan  Formation (Cretaceous; interbedded  sand
and clay); the Woodbridge Clay is locally absent
under some parts of the site and the affected area
(including at Well SB-11).  The Brunswick Shale
bedrock underlies the Farrington Sand.

The Woodbridge clay  is absent in the vicinity  of
Well  SB-11,  so ground water withdrawn from
Well  SB-11 is derived from  both  aquifers.  The
direction of ground-water flow in both the shallow
unconflned and the lower semiconfined aquifers is
dominated by production Well SB-11 northeast of
the site.   There  is also potential  for downward
vertical flow from the shallow aquifer to the lower
aquifer through the intervening clay layer.

Estimates of local aquifer properties are limited to
the shallow aquifer. Aquifer tests showed a range
in horizontal hydraulic conductivity of 7x10"3  to
1.5x10"'   centimeters   per  second   with   no
discernible  pattern,   indicating  that  there  is
significant areal and vertical heterogeneity in the
                                              118

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SITE PLAN AND LOCATIONS OF

EXTRACTION WELLS

IBM-DAYTON SITE
                HL.WAI. 1987
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                                                                                          IBM-Dayton
 shallow aquifer (REWAI,  1987).   The average
 ground-water transport rate reported for theshallow
 aquifer at the IBM property is approximately  4
 feet per day toward Well SB-11.

 The primary  contaminants  of  concern are the
 volatile  organic  compounds   (VOCs)   1,1,1-
 trichloroethane  (TCA)  and  tetrachloroethylene
 (PCE).  Lower levels of trichloroethylene (TCE),
 1,1-dichloroethylene   (DCE),   and   1,1-
 dichloroethane   (DCA)   were  also  identified.
 Initially, TCA  was  the  dominant contaminant
 relative to PCE.  With the termination of pumping
 in 1984, data indicate that PCE has become the
 dominant contaminant.

 The change  in  relative  concentrations  between
 TCA and PCE may be related to the solubility of
 these two chemicals (Groundwater Sciences Corp.,
 1988a).  TCA is more soluble and  less readily
 sorbed to soil than PCE is, .Therefore, pump-and-
 treat systems are more effective in removing TCA
 than PCE.

 The suspected  sources   of the  ground-water
 contamination originating from  the IBM site are
 underground  chemical-storage  tanks  that  were
 removed in  1978, just after the onsite extraction
 system was  started up.  The VOC  plume centers
 on  the  area  of the tanks, and highest concen-
 trations of  total  VOCs  are found in  the shallow
 aquifer.    Concentrations  of  total  VOCs  in
 monitoring Well GW32 (GW32  is installed in the
 shallow aquifer in the vicinity of the original spill)
 decreased from about  15,000 ppb (1978) to 600
 ppb  (1984)  while  the extraction  system was
 operating and then increased to about 6,000 ppb
 (1987)  after the system was shut off. Much lower
 levels (less  than 100 ppb  in 1984) of total VOCs
 were found  in the offsite plume, which extended in
 a lobe toward Well SB-11, in response to pumping
 from that well.

            UPDATE ON SITE
          CHARACTERISTICS

 Since the time of the original case study,  there
have   been   no  significant  changes   m  site
 administration or in the  understanding  of the
hydrogeologic setting or of waste characteristics.

The densities of ground-water contaminants TCA,
 PCE, TCE, DCE, and DCA are greater than the
density of water, so  they have the potential to be
present  as   dense   nonaqueous-phase   liquids
(DNAPLs).  The fact sheet for the New Jersey
Pollutant Discharge Elimination System (NJPDES)
permit (NJDEP, c. 1990) discusses an increase in
the concentration  of contamination in the ground
water with depth  near the source and relates this
increase  to the  presence  of  DNAPL.    The
reappearance  of  elevated  concentrations of  the
contaminants   after the  onsite    ground-water
extraction system  was shut off and the absence of
residual soil contamination near the ground surface
have led to the conclusion that residual DNAPLs
in one or both of the aquifers are the source of the
ground-water contamination. IBM feels that the
DNAPLs are  limited to  the shallow aquifer,  but
the NJDEP does not necessarily share this view.

              REMEDIATION

        Design and  Operational
       Features of Remediation
                  System

The objective  of the ground-water remediation
system installed in 1978  was to restore ground-
water quality in both aquifers to levels that would
be  suitable for  the municipal  drinking  water
supply.   In 1984, when  NJDEP  authorized  the
reduction  of   the  remediation  system to only
wellhead treatment at Well SB-11, an action level
of  100 ppb  for  TCA in  any one  of the   12
perimeter wells for two consecutive  months was
established as  the  point   at  which  IBM  was
required  to notify the NJDEP to determine  the
need  for  further  remedial  action (Groundwater
Sciences Corporation, 1988b).  Even though this
criterion had not been exceeded, IBM decided in
1987 to initiate further remedial action to control
the reemerging plume.

The system in place between  1978  and  1982
consisting of 13  onsite  extraction wells  in' the
shallow aquifer and 1 extraction well (GW-18E) in
the  deep  aquifer  (see   Figure  2),  operated
intermittently  La conjunction with Well SB-11.
Ground water extracted from the onsite wells was
treated by air  stripping and then returned to  the
ground-water   system  by   means of  a  spray-
irrigation field  located on the western part of the
IBM site (see  Figure 2).  In 1982, an additional
offsite  pumping center was added to the system
midway between  the IBM site and Well SB-11.
For a short time, the ground water extracted from
the offsite wells was treated and then reinjected to
a line of nine  injection wells along the northern
                                                  121

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                                                                                           IBM-Dayton
 site boundary.  The use of the injection wells was
 eventually  stopped   because   their   injection
 capacities were reduced by well deterioration.  The
 effectiveness  of  the remediation  program  was
 monitored  by testing  the  water  quality  and
 measuring  the hydraulic  performance  of both
 aquifers in nearly 100 monitoring wells. By 1984,
 the determination was that  continued pumping
 would not further reduce  the concentrations in the
 ground water, so the system  was shut down and
 the concentration of TCA was monitored to alert
 IBM  and  the NJDEP of  the need for appropriate
 action.

 The  objectives of  the  long-term  remediation
 program implemented in October 1990 are control
 of the boundary and source of the  plume.   The
 determination  was that the  residual source of the
 contaminants cannot effectively  be removed by
 ground-water  extraction.   The remediation  is
 focused on the shallow aquifer.   Initially a three-
 step approach consisting of only boundary control
 (step  1),  followed by combined boundary  and
 source control  (step 2), and  ending with source
 control  (step 3) was planned.  Boundary control
 (step  1) was to be achieved by pumping Wells
 GWI-8 and GWI-9R (Figure 2) at 15 and 35 gpm,
 respectively. Step 2 (boundary and source control)
 of the remediation  plan consisted of installing two
 new wells (GW32R and GW33R)  in  the same
 location as previous Wells GW32 and GW33 and
 pumping them  at  25 gpm each.  Concurrently,
 boundary   control  would   be   maintained  by
 continuing to pump  GWI-9R at 30 gpm.   IBM
 anticipated  that  this  phase  (step  2)   of  the
 remediation plan would continue for a minimum of
 2-1/2  years.

 After  concentrations were  reduced  to the point
 where boundary control was no longer necessary,
 step 3 (only source  control)  would be initiated.
 This  phase  of  the remediation  plan consists of
 pumping Wells GW32R and GW33R at 25 gpm
 indefinitely to  control the source and prevent the
 reemergence of the chemical plume.  Start-up was
 delayed during the permitting process and steps  1
 and 2 were combined at  the  initiation  of the
program.
 Currently,   boundary-control Wells  GWI-8  and
GW1-9R and source-control Wells GW32R  and
GW33R (see Figure 2) are pumping.  The rates are
 15 gpm for Well GWl-8,  35 gpm for Well GWI-
9R, and 25 gpm for Wells  GW32R  and GW33R
(IBM,  1991b).   All four of  these  wells  are
screened in the shallow aquifer.
 The ground water is extracted, treated for metals,
 then run through an  air stripper to remove VOCs
 before it is  finally discharged to a spray field on
 the site.  After  the plume between the boundary
 and the source is reduced to permitted levels (10
 ppb for PCE and 33 ppb for TCA), pumping at the
 boundary wells  can be  stopped, leaving  source
 control as  the  final remedial  procedure.   The
 expectation  is  that a minimum of about a year and
 a half of combined source- and boundary-control
 pumping will  be necessary before the system  is
 reduced to only source control.

 EVALUATION  OF PERFORMANCE

 At  this time, there can be no in-depth evaluation
 of the performance of the new system since it was
 started in October 1990, and the data available for
 this report extend to only mid-November of 1990.
 Quarterly samples continue to be collected,  and
 consultants  for  IBM Dayton are evaluating the
 effectiveness of the  system.   Their evaluation
 should be available in late 1991.  Evaluation of the
 former system remains  as described in the original
 case study.

 Well testing  and  intermittent start-up pumping
 began in October 1990, and continuous pumping
 began in November 1990. Figures 3  and 4 show
 the water-level distributions in  the  shallow  and
 deep  aquifers  that were  measured in November
 1990.     According-   to  IBM,  however,  the
 measurements  used to construct these ground-water
 contour maps  were collected after the  wells were
 shut  off  for  12  hours.   These ground-water
 elevations, therefore, do not reflect the response of
 the water table to pumping of the extraction wells.
 Well  SB-11  was pumping and a distinct zone of
 influence can be seen around this well in both the
 upper and lower aquifer.  Not known is whether
 other nearby wells also were exerting influence on
 the ground-water elevations at the same time.

Figure 5 shows  the  VOC plume  in the shallow
 aquifer as it  was observed in 1987, when  the need
 for  long-term  migration  control  was becoming
 apparent. Total VOC concentrations of more than
 1,000 ppb were measured in the onsite plume.

Figures 6 and 7 show the areal distribution of the
summed TCA  and PCE concentrations measured
in  the two  aquifers  in November 1990,  shortly
after  the   migration-   control   system   began
operating. The summed concentrations are not
                                                   122

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                         TOTAL »OC ISOCON
                         IN (ppbl
                                                                                     •M*
                                                                                                           •a«'
                                                                                            SCALE IN FEIT
         Suucc*  HE WAI. 1987
                                                                           FtauraS
                                                                           TOTAL CONCENTRATIONS OF VOLATILE ORGANIC
                                                                           COMPOUNDS IN THE SHALLOW AQUIFER, APRIL
                                                                           1987
                                                                           IBM-DAYTON SITE
                                                                                                  09
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                                                                                          IBM-Dayton
directly comparable  to  the  total  VOC  readings
shown in Figure 5, but TCA and PCE are the
major constituents of the VOCs at the site, and the
inference   is   that   the   November  1990
concentrations were generally lower than those of
April 1987.

Figures 8, 9, and 10 show histories of TCA  and
PCE concentrations in three  onsite wells in the
centra]  plume  area.    They show  that  PCE
concentrations peaked in 1988 for Wells GW-16B
and GW-32.  A similar peak is shown in  1989 for
Well GW-25, which is farther from the source area
than the  other two wells are. All three figures
show  that  PCE  concentrations  were  declining
naturally before the migration-control  system  was
started up in October 1990.

Figure  11  shows that  the TCA   and PCE
concentrations at  production Well SB-11 have
remained fairly stable at between 20 and 40  ppb
since  1985.  It is too early to tell what effect the
migration-control system will have on Well SB-11.
The  effect  may  not  be  dramatic because  the
NJDEP has  determined that the IBM-Dayton
facility is not the  only source of the VOCs  that
contaminate  this well.

    SUMMARY OF REMEDIATION

Ground-water remediation  began  at the IBM
Dayton site  in 1978.  Between 1978 and 1984, a
system of as many as 21  extraction  wells  was
operated  in  an attempt  to restore  the levels of
ground-water quality to  make the water suitable
for a public  water supply.  In 1984, ground-water
extraction was stopped with  the expectation  that
natural attenuation  processes would complete the
restoration  of the aquifer.   However,  it soon
became apparent that VOC  concentrations were
rising again.  By 1987, the maximum  total VOC
concentration  in   the  reemergent  plume   was
approximately  40 percent   of  the   maximum
measured in  the 1978 plume.

The new plume  was narrower and more sharply
defined  than the  original,   appearing  to   be
influenced by the hydraulics of Well SB-tl.  This
well was shut down from January to June 1978, in
response   to  the   discovery  of  ground-water
contamination.  During that period, ground-water
contamination was relatively  widespread on  the
IBM property. Well SB-11 was then restarted  and
has since been used to control the  spread of the
plume.   Also possible is that additional minor
pools or stringers of DNAPL may have  been
present at the site in 1978 and were cleaned up by
the ground-water extraction system, leaving only
the solvent-tank area as a distinct residual source
of VOC contamination.

Hydrogeologic and water-quality appraisals of the
site  conducted in  1987  and  1988  led  to the
conclusion  that the resurgence of VOC contam-
ination   was   caused   by   residual  DNAPL
contamination (Groundwater Sciences Corp., 1988a
and  1988b).   Because  of this  conclusion, the
determination  was  that   the  goal  of  aquifer
restoration should be abandoned and that long-term
migration control would be necessary instead.  A
permit for the migration-control system was issued
in 1989, but complications in the permitting of the
ground-water treatment facility delayed the start of
pumping until October 1990.  Since then, IBM has
collected three rounds  of ground-water data-in
November  1990, February 1991, and May 1991.
Data  on ground-water  elevation  were collected
while the extraction system was operating  in May
1991. IBM states that this is the only set of data
that shows the effect of pumping on ground-water
elevations.  The  data are being studied by IBM's
consultant and are not available for inclusion in
this report.

   SUMMARY OF NAPL-RELATED
                  ISSUES

As noted previously, the  reappearance of elevated
concentrations  after  the  onsite  ground-water
extraction system was shut off, coupled with the
absence  of residual  soil  contamination near the
ground surface, suggested the presence of residual
DNAPL  as  the  source  of  the ground-water
contamination (Groundwater Sciences Corporation,
1988b).

Well  cluster GW42,  among others, is located in
the vicinity of a suspected source of ground-water
contamination.    It consists  of  a shallow,  an
intermediate, and a deep  well within  the shallow
aquifer.  The NJPDES permit for this facility notes
that  the  water-quality data from  this well show
increases  in   contaminant  concentrations  with
depth, and presents this  as  an  indication that
DNAPLs are  present beneath this  site.  Table  1
shows the concentrations  of TCA in these wells.
Some other well clusters show similar patterns, but
                                                   126

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      PCE concenMfen (pfb)
NS   . Not campled
NO    Notdetected


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                                                                                     Figurafi
                                                                                     CONCENTRATXJNS OF TCA AND PCE IN THE SHAL-
                                                                                     LOW AQUIFER, NOVEMBER 1990
                                                                                     IBM-DAYTON SITE
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                                                                                          flgui* 7

                                                                                          CONCENTRATIONS OF TCA
                                                                                          AND PCE IN THE DEEP
                                                                                          AQUIFER, NOVEMBER 1990
                                                                                          IBM-DAYTON SITE
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                       6000
                       5000
                   _.   4000  -
                       3000
                  o
                  o
                  o   2000
                       1000
                             1978   1979   1980    1981    1982    1983    1984    1985    1986   1987    1988    1989   1990
                                                                    YEAR
           NoU
               Data reported as 6-mooih average
               concentrations in ppb.
               Oala comptted from various sources
HtSTORVOFTCAANDPCE
VARIATIONS IN EXTRACTION
WELLGW-168
IBM-DAYTON SITE
W
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                        1,200
                              1978   1979   1980  1981  1982  1983   1984   198S  1986   1987   1968   1989   1990   1991
                                                                     YEAR
             Data reported as 6-month avcraga
             concmnVMtomtnffti
             Dau compMcf (rwn v4f oo* sounds
Flguns:
HGTORYOFTCAANDPCE
VARIATIONS IN MONITORING
WELLGW-25
IBM-DATTON SITE
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             15,000
          ^ 10,000
          I
          1
          8   5,000
                    978   1979  1980
1981   1982   1983   1984   1985
                      YEAR
Mot*
   Daia reported as 6-month average
   concentrations in ppb.
   Data competed from various sources.
1987  1988   1989   1990   1991
                                                      Figure 10
                                                      HISTORY OF TCA AND PCE
                                                      VARIATIONS IN EXTRACTION
                                                      WELLGW-32
                                                      (BM-DAYTON SJTE
                                               m,
                                               z
                                               I
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   I
       500
       450
       400
      350
      300
      250 -
   O  200

   O
   O
      150
       100
       50
              1979  •   1980
                               1981       1982      1983       1984      1985
                                                     DATE
                                                                           1986
                                                                                    1907
           1988
                     1989
                             1990
   LEGEND

   TCA  	

   PCE  	
Compiled Irom various sources
Figure 11
HISTORY OF TCA AND PCE VARIATION AT
PRODUCTION WELL SB-11
IBM-DAYTON SITE
                                                                                                                              00
                                                                                                                              Z

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                                                                                       IBM-Dayton
Table 1
SIX-MONTH AVERAGE CONCENTRATIONS OF TCA (ppb)
Well
Number
GW42D
GW42I
GW42S
JJ 1985
3608
15 .
6
JD 1985
2809
1
4
JJ 1986
3115
3
60
JD 1986
5146
1
130
JJ 1987
5020
1
53
JD 1987
7362
1
44
JJ indicates June through July
JD indicates July through December
of  important note is that  this pattern  is fiot
necessarily the same for all the other contaminants
or for all the other well clusters in the vicinity of
the suspected source.

      UPDATE BIBLIOGRAPHY/
             REFERENCES

Groundwater Sciences  Corporation.     1988a.
Groundwater Remediation Plan:   IBM Dayton,
New Jersey Facility.

Groundwater Sciences Corporation, S. Feenstra,
and J. Cherry.  1988b.  DNAPL Geochemistry and
Remedial  Feasibility;  Farrington Sand Aquifer;
Dayton,  New Jersey.

IBM  Corporation.    1989-1990.    Bimonthly
Amended Administrative  Consent Order Reports
for January 2989 to December 2990.

IBM  Corporation.    1990.    NJDPDES/DGW
Monitoring Data  Quarterly  Reports for  March
through  December 2990.
IBM  Corporation.    1991a.    NJDPDES/DGW
Monitoring  Data  Report  for  November 2990,
January 20, 2992.

IBM   Corporation.      199 Ib.     Personal
communication with Mr. Jeff Wilson. May 1991.

New  Jersey   Department  Of   Environmental
Protection. Undated (c. 1990). NJPDES Permit to
Discharge Into the Ground Waters of  the State.
 Permit No. NJ0000426.

RJE. Wright Associates, Inc  (REWAI).   1987.
Report  on   the  Investigation   of  Chemical
Reappearance in Groundwater at the IBM Dayton
Site.

U.S.  Environmental  Protection   Agency (U.S.
EPA).   October  1989.  Evaluation of Ground-
Water  Extraction Remedies:  Volume 2,  Case
Studies 2-29. EPA/9355.4-03.
                                                 133

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                                                  UPDATE OF CASE STUDY 11

                                                                  IBM-San Jose
                                                            San Jose, California
Abstract

The final ground-water extraction system includes 23 new and existing wells.  Several of
the wells  in  the new system began  operating in  October 1990.   The  remaining  new
extraction wells were scheduled to begin operating in early 1991. Between 1988 and 1990,
little change was observed in the extent of the contaminant plumes. Previously, between
startup and 1988, the  size of the plume decreased. Freon 113 concentrations in the A
aquifer decreased by 1  to 2 orders of magnitude between 1984 and 1990 except for the high
concentration area near building 004.
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
1978
May 1982
Volatile Organic Compounds, Oil
Alluvial sand and gravel with silt and clay
layers
30
6,000 gpm
760 acres
250 feet
Freon 113: 16,000 ppb
                                       134

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                                CASE STUDY UPDATE
                                     IBM-SAN JOSE

                           BACKGROUND OF THE PROBLEM
             INTRODUCTION

The original case study for the IBM  General
Products Division site  (U.S. EPA  1989, Case
Study 11) summarized the remediation of ground-
water contamination through May  1989. The IBM
facility is located at 5600 Cottle Road in San Jose,
California (Figure 1).  Magnetic disks and heads
for computer hardware are  manufactured at this
site, using a variety  of process chemicals and
materials.   Ground-water contamination was first
discovered  at the site in  1978.   The  primary
contaminants wereFreon 113,1,1,1-trichloroethane
(TCA),   I,l-dichloroethylene  (1,1-DCE),  and
trichloroethylene (TCE).  In 1985, there  was an
onsite spill of hydrocarbon  (Shell Sol 140) that
caused  additional  ground-water  contamination.
Ground-water extraction in the onsite source areas
first began in 1982. Extraction systems at the site
boundary and in the midplume area offsite started
operating in 1983.  In 1984, an extraction system
was installed offsite near the downgradient end of
the plume.   The cleanup is  proceeding under  the
authority of the California Regional Water Quality
Control Board.

The IBM  facility is located  in the  Santa Teresa
Basin in the southern part  of the Santa Clara
Valley.  Bedrock underlies the Santa Teresa Basin
and forms the surrounding mountains. Most of the
bedrock  consists  of  consolidated  sandstones,
shales, cherts, serpentinite,  and ultrabasic rocks.
The valley floor  is  underlain  by Quaternary
alluvium, consisting of unconsolidated clays, silts,
sands, and gravels. The thickness of the alluvium
ranges from zero in the surrounding highlands to
approximately 400 feet near the center  of  the
basin.

The monitored aquifer zones are referred to as  the
A, B, C, and D aquifers, in order of increasing
depth.  Deeper aquifers are in some areas, and  the
aquifers merge  in some locations  because  of
discontinuities in  the  aquitards.   The B  and C
aquifers ate coarser-grained  than the  A  aquifer.
The B aquifer generally consists of two or three
sand or gravel  units separated by  silt  or clay.
Declining  water  levels from  1983 to 1988 had
caused the B  aquifer to become unconflned  in
much of the study area.  Water levels have since
recovered, and the  B aquifer  is  confined once
again.   The C,  D,  and deeper aquifers remain
confined.

The release  of contaminants to soil and ground
water may have been the result of surface spills
and leaking underground piping.  Contamination is
found in all five aquifers and is found both onsite
and offsite.  Remedial measures have been taken
only for the A, B, and C aquifers, although all five
aquifers  are  monitored.    Target  remediation
standards  are  specific for  each  aquifer.   No
extraction  wells were  installed  below  the  C
aquifer. Contamination of the A aquifer generally
appears to be limited to  areas within  or near the
site boundary.    The  B  and  C aquifers are
contaminated both onsite and offsite. As reported
in  the initial case study,  Freon  113  and TCA
concentrations  in the  B aquifer  were below target
remediation  standards in the fourth  quarter  of
1988.

In  one area onsite, .Shell Sol  140 was released
accidentally in late November 1985. Shell Sol 140
is a light cutting oil with  properties  similar  to
those of kerosene.  Shell Sol 140 contamination
was limited to  the A  aquifer. In December 1985,
product-recovery and  hydraulic-control  activities
were  implemented at the Shell Sol 140 release
area including  installing  six  A-aquifer extraction
wells.    Product-removal   skimmers   are  used
whenever  recoverable amounts  of free product
accumulate in the wells (HLA, 1990d).

            UPDATE OF SITE
          CHARACTERISTICS

This case-study update is based on ground-water
monitoring data through September  1990, and
additional  field  investigations  conducted after
1988.  Additional hydrogeologic information was
collected during the predesign investigation  for the
A-aquifer extraction  system (HLA, 1989b).  The
purpose of the  hydrogeologic investigation  was  to
find the most transmissive areas of the aquifer.
                                              135
                               6*77

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                                                              IBM-San Jose
            NovttO«
           0         10 miles

          Approximate Scale
  DRAFT
Source: HLA, 1987
Rguni
REGIONAL MAP
IBM-SAN JOSE SITE
SAN JOSE. CALIFORNIA
                                    136

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                                                                                        IBM-San Jose
These areas would be the most favorable locations
for extraction wells in the A aquifer.

The source areas are underlain  by unconsolidated
alluvial sediment  composed of sand,  gravel,  silt,
and clay.  The A-aquifer zone is underlain by the
A/B aquitard, which consists of a blue-gray clay.
The A aquifer consists of point-bar and channel
deposits  that  were deposited  in  a  braided  or
meandering  stream  environment  (HLA,  1989b).
The point-bar deposits are composed primarily of
fine-grained  sand and silt and have relatively  low
transmissivity. The channel deposits are primarily
mixtures of sand and gravel (HLA, 1989b).

Ground-water flow in the A  aquifer is controlled
by  the deeper  and more  continuous  channel
deposits, particularly  when water levels are low.
The channel deposits are deepest  in areas  where
the A/B aquitard is thinnest. These thin zones are
also where  contaminant migration from  the A
aquifer to the B aquifer is most likely to occur. A
map of the high-conductivity channels is presented
in Figure 2.

Since  the fall of 1985, a general  seasonal pattern
of decline and recovery  in water levels has been
observed.  However, water levels began a seasonal
recovery in the fall of 1988 and continued to  rise
through the first quarter of 1990  in most B-  and
C-aquifer wells (HLA,  1990d).   Water levels in
many of the  wells rose more than  20 feet between
1988  and March  1990.  Water  levels began  a
seasonal decline in most B- and C-aquifer wells in
April  1990,  and  the decline continued  through
August 1990. Water levels began  increasing again
in September 1990 (HLA, 1990d).  Water levels in
approximately 40 percent of the monitoring wells
in the  A  aquifer  remain too low for obtaining
representative   ground-water   samples   (HLA,
1990d). Ground-water conservation is a concern
and was a significant consideration in the remedial
design.

         Waste Characteristics

Freon 113, TCA, 1,1-DCE, TCE,  1,1-DCA, PCE,
and chloroform are the contaminants of concern in
the A aquifer.  The primary contaminants in the B
aquifer are Freon 113, TCA, and 1,1-DCE.  Freon
113, TCA, and 1,1-DCE have been detected at  low
concentrations in the C aquifer.

Concentration-contour  maps  were  presented  for
TCA  and 1,1-DCE in  the  original  case  study
because they were the contaminants of greatest
concern.     Freon  113,   a  much  less  toxic
contaminant,  is  suspected  to  exist as a  dense
nohaqueous-phase liquid (DNAPL) near the Tank
Farm 067  source  area.   Concentration contour
maps for Freon 113 during the second quarters of
1984 and 1986 in the  A,  B,  and C aquifers are
presented  in  Figures 3, 4, and  5.   The  target
remediation standard  for Freon 113 is  1,200 ppb
for the A aquifer, and 4,500 ppb for the B aquifer.
The maximum Freon  113 concentrations observed
in ground water in 1988 were well  below target
remediation goals.

Nonaqueous Shell Sol 140 has  been observed since
the 1985 spill.  The areal extent of Shell Sol 140
free  product during 1988  is shown  in  Figure 6.
The  area in which aqueous-phase Shell Sol 140
historically has been detected is also  shown  in
Figure  6.  The target remediation  standard for
Shell Sol 140 is 1,000 ppb.

              REMEDIATION

        Design and Operational
       Features of Remediation
                  System

As reported  in  the  original  case  study, three
interim ground-water extraction systems consisting
of 30 wells were installed at the site: (1) an onsite
system near known- source areas,  (2)  an  onsite
boundary system, and (3) an offsite system. The
remedial measures at the site  were considered  an
interim response, pending the approval  of a final
cleanup   plan.      In    1986,   a   long-term,
comprehensive  ground-water  cleanup  plan was
submitted to the California Regional Water Quality
Control Board, the Department of Health Services
(DHS),  and the EPA.   In 1988, the  long-term
cleanup plan was approved by all three agencies.

As part  of  the  long-term  cleanup plan,  new
ground-water extraction systems  were  proposed.
The  predesign field investigation was  conducted
between September 1988 and February 1989. The
areas selected for remediation were those with
high   aquifer   transmissivity   and   pollutant
concentrations  that  exceed  target  remediation
goals.  In the A aquifer,   these areas  generally
correspond to the locations  of the channel features.
                                                   137
                       605  £01,77

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                            IBM-San Jose
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                                                     IBM-San Jose
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                                                     IBM-San Jose
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                                                                                   IBM-San Jose
                                                                    EXPLANATION
                                                                              id Stall Sol 140
                                                      «"~ •«« hM DMO aonrmwd ki grauna-tmttr Minpiit
                                                            wNteMd during KM pMod ip*6ii*d m tut tiUt.
                                                            DfMelion Umtt • O.CO • 0,1 ppm.

                                                            Appfoximitt VMI Mtnt of fc«t product «i
                                                            nwaiuwtf durtng 8M p«rioa tpteHiM in ttm till*

                                                       O   Moortorins or sbtMvttion well

                                                       A   E«tf«ctlon will
                                                           h.N   X^v V-
                                                           i'a-K. V.   \ x>*.•""'•••
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                                                                                        IBM-San Jose
The final remedial ground-water extraction system
was designed  to  minimize  the  potential  for
dewatering the B aquifer and deeper aquifers. The
remedial action plan was developed on the basis of
stable   ground-water  conditions  and  included
contingencies  for  .recovering  and   declining
conditions (HLA, 1989c). An analysis of ground-
water  and  hydrologic  conditions  showed that
ground-water  conditions   were likely  to   be
relatively  stable;  therefore,  the  remedial  action
plan  was   implemented without  contingencies
(HLA, 1989c).

Ground-water conservation is a concern because of
steadily  declining  regional  water  levels,   so
alternatives  for onsite  ground-water reuse were
explored.   This led to  the implementation of a
pilot-scale ground-water recharge program, which
is discussed later in this case-study update.

 Design  of Final  Extraction System

The final extraction  system  consisted  of wells
installed as part of the interim remedial  measures
(1RM)   program   and  new  wells   installed  as
specified in the plan for long-term cleanup. The
three  separate extraction systems are  described
below.  The final system  is expected  to begin
operating in 1991.

Onsite  Extraction System.  The interim  onsite
extraction system  was centered on  the  A-aquifer
source  areas at Building 001, Tank Farm 067, and
Building 006 (shown in Figure 2).   The  interim
onsite system included 8 extraction wells, and the
final extraction  system  includes 10  extraction
wells.  The A-aquifer well locations are  shown in
Figure  7.  The onsite B-aquifer well locations are
shown  in Figure 8.  The three areas selected for
ground-water extraction  and  their corresponding
extraction  wells  are  listed  below.   The wells
identified as existing were installed as part of the
interim remedial work.

1.   Tank Farm 067 area.  (Four existing  A-aquifer
    wells:   RA-11, RA-12, RA-14, A-53. Two
    new B-aquifer wells:  RB-7 and RB-8.)

2.   Area around Building 005 and Building 006.
    (Two new A-aquifer wells: RA-26, RA-27.)

3.   Building  001/100  area.     (Conversion   of
    existing  A-aquifer  monitoring well:   A-17.
    Three new A-aquifer wells:  RA-22, RA-234,
    and RA-25.)
Wells RA-25,  RA-26, RA-27, RB-7,  and RB-8
began operating in October 1990.  The remaining
extraction wells were scheduled to begin operating
in early 1991.

Boundary  Extraction  Systems.   The  interim
onsite boundary extraction  system consisted  of
eight A-aquifer wells, seven B-aquifer wells, and
two C-aquifer  wells.  All eight A-aquifef wells
except RA-2 operated from June 1983 to late 1983
or to early 1984,  when they were  shut down
because  of low  water  levels (HLA,  1990b).
Extraction  Well RA-2  was  pumped from June
1983 through  October  1984.   The  pump was
replaced with one of lower capacity, and pumping
from RA-2  began again in September 1985. Well
RA-2 is  located in a deep part of the onsite sand-
channel deposits (HLA, 1990b).

The  final  onsite A-aquifer  boundary extraction
system includes four new extraction wells (RA-29
through  RA-32) and one existing well  (RA-2)
(Figure  7).   A-aquifer  ground-water extraction
from Wells RA-29 and RA-30 began in  October
1990 (HLA, 1990b).  B-aquifer  boundary wells
also are in  the  final boundary  extraction system;
they  include existing Well RB-2,  which  supplies
water to the deionized water system  and a new
well, ORB-6,   which  is  adjacent to the plant
boundary (HLA, 1990b).

Offsite Extraction System.  The  interim offsite
extraction system  included three B-aquifer wells
(ORB-1,  ORBC-2,  and  ORBC-3) and  one  C-
aquifer well (ORC-1). Wells ORC-1 and ORBC-2
were shut down in- April 1988.   Well ORBC-3
operated until July 1990.  Well ORB-1 continued
to operate in February 1991  (HLA,  1991).  The
final extraction system includes  5 wells: 2 new  A-
aquifer wells (ORA-04 and ORA-05),  1 converted
A-aquifer monitoring well (12-A), and 2 new  B-
aquifer wells (ORB-6 and ORB-7). Well ORB-6
was installed in February 1990. Well ORB-7 was
installed in November  1989.  The  locations  of
offsite monitoring and extraction  wells in the B
and C aquifers,  respectively, are shown in Figures
9 and 10.

Ground-Water Extraction  Rates. Most of the
extraction wells in the interim and  final extraction
systems  have  not  been  operated continuously.
Ground-water volumes extracted from each well in
1988, 1989, and 1990 are shown in Table 1.
                                                   143

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                                              IBM-San Jose
•i X
                        fTrw^n
         /
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                                                                                   IBM-San Jose
                                                                  EXPLANATION
                                                             Momtortntj *•* with ktontincation number

                                                             Extinction wtll with fdintifieilion numbtr

                                                             R*chara* w*t with kUnUfcjiiion number
                                                                     moniloring «nril
                                                             with idmttfieuian number
                                                                      1000
                                                                      =i=
                                                                  SCALE IN FEET
Source: HLA, 1991
                                                           SSSSnOMMQ AND «™ACTONIWEUS
                                                           IN THE QUOTE B-AQUIFER ZONE
                                                           IBM-SAN JOSE SITE
                                                  145

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                      IBM-San Jose
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  146

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       i VI II.U
                                                                                              EXPLANATION
                                        SCALE IN FEET
III A. 199!
FlgunlO

NKH«TORtNG AMD EXTRACTION WELLS

IN THE C-AQUIFER ZONE

IBM--SAN JOSE SITE
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2



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                      IBM-San Jose
Table 1
TOTAL VOLUME PUMPED FROM EXTRACTION WELLS
1988 - 1990
IBM-SAN JOSE SITE
Page 2 of 2
Year

1990

















Well Number

RA-2
A-53#
RA-11#
RA42#
RA-14#
RA-24#
RA-25*
RA-27#
RA-29#
RA-30#
RB-2
RB-3ft
RB-7#
RB-8#
ORB-1
ORB-6t
ORB-7*
ORBC-3tt
TOTAL
Source: HLA, 1991
Volume Pumped
(million gallons)
9.20
0.02
0.02
0.02
0.02
0.02
0.66
1.29
0.24
1.18
147.34
74.41
8.59
8.54
57.10
34.65
80.92
97.92
522.14

Wells on in: *May, fJuty, #Oct. - Dec.
ttWells off in July
Other unmetered low-flow wells: A-17, 12-A, RA-22, RA-26, RA-31, RA-32,
ORA-4, ORA-5
148
G6I

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                 IBM-San Jose
Table 1
TOTAL VOLUME PUMPED FROM EXTRACTION WELLS
1988 - 1990
IBM-SAN JOSE SITE
Page 1 of 2
Year

1988












Well Number

RA-2
RB-1*
RB-2
RB-3
RB-4*
RB-5*
RB-6*
C-l*
RC-1*
ORB-1
ORC-1*
ORBCr2*
ORBC-3
TOTAL
Volume Pumped
(million gallons)
14.31
56.63
138.60
94.83
4.12
40.00
59.74
22.82
72.47
29.29
47.20
130.08
522.60
1232.69
*Wells off in April
1989




RA-2
RB-2
RB-3
ORB-1
ORBC-3
TOTAL
3.09
173.47
131.39
38.27
237.36
583.58
149
6*77

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                                                                                         IBM-San Jose
Operation  from  1983 through  1990  represents
interim  ground-water  extraction  that  continued
during the construction of the final extraction and
treatment  systems.    Flow  rates were adjusted
according to well-water levels. The ground-water
treatment  system was started up  in late  1990.
Before the  new system was constructed, extracted
ground  water  was  discharged directly to  storm
drains with no pretreatment (HLA,  1991).  Site
operators  have stated  that the discharged  water
contained   only  very  low   concentrations   of
contaminants.   During startup,  extraction rates
varied,  depending on treatment  plant capacity.
After startup of the treatment plant  is completed,
and when either drought conditions no longer exist
or a reuse is established for the  entire  flow,
ground-water will be extracted from each well at
or near the design flow rate (IBM,  1991).  The
design extraction rates for the final system  are
shown in Table 2. The total design ground-water
extraction rate is  870 gpm.  The final  extraction
and  treatment  system  is expected to  be operating
in 1991 (IBM, 1991).

        Ground-Water Recharge

Recharge of extracted ground water after treatment
is being considered as an onsite ground-water use.
Pilot  testing for ground-water recharge began  in
late  1990.  The pilot study is being conducted at
one  well   to  evaluate recharge  rates,  aquifer
response, and  well efficiency (McLaren,  1990).
The  proposed  recharge areas  for  the  A and  B
aquifers are shown  in Figures 7 and 8.  At  the
conclusions  of the  pilot recharge  testing,  the
feasibility    of  full-scale   recharge  will  be
determined.

It is estimated that 20 gpm could  be  recharged
through the proposed A-aquifer recharge area.
However, cost analysis has shown that recharge to
the A aquifer would not be a cost-effective means
of reusing ground-water at such a low rate (HLA,
1990a).  A-aquifer recharge is proposed only if the
A-aquifer  extraction  system becomes ineffective
because of low water levels.

The recharge areas were identified on the basis  of
hydrogeologic  analyses.   The areas are  located
upgradient of the chemical  plumes to minimize the
potential of spreading the  plume and to enhance
the  extraction  systems by flushing  contaminated
ground  water  through  the aquifer  zone.   In the
recharge area, the  A aquifer consists of as much as
30 feet  of permeable sand and  gravel having a
saturated  thickness of  13 feet (HLA,  1990a).
Water levels could rise quickly in a discontinuous
sand and gravel lens; therefore, careful monitoring
would be required.  The B aquifer is better suited
for recharge.   It contains up to 45  feet of highly
permeable  sand and  gravel  that  are  relatively
homogeneous and continuous over the site.

         Soil-Vapor Extraction

Pilot-scale tests of soil-vapor extraction (SVE) are
also being  conducted.  The intent  of SVE  is to
reduce VOC concentrations in onsite source areas.
The preliminary SVE areas are shown in Figure
11.  The Shell Sol 140 spill area  is one of the
areas.   Table 3 gives the estimated cumulative
mass of contaminants removed by SVE  through
the third quarter of 1990.  In  the Building 004
area, 1,177 pounds of VOCs were removed in 340
hours of operation.  In the Shell Sol 140 area, 8
pounds  of petroleum hydrocarbons  were removed
in 56 hours of operation.  IBM plans to install a
full-scale SVE system.
         •*»  •      	    .

 EVALUATION OF PERFORMANCE

           Hydraulic  Control

Figure 12 shows that the  water-level contours in
the A aquifer in September 1990 were  similar to
those in June 1986, presented in the original case
study.   The effect of extraction well RA-2  (near
Poughkeepsie Road) is apparent in both 1986 and
1990.  No other A-aquifer extraction wells  were
operating  in  September  1990.  Flow in  the A-
aquifer zone is to the southwest over much of the
site but is  northeast to northwest in  the  western
part of the site.

In September 1990, flow in the B-aquifer  zone at
the site  was to the northwest, as shown in Figure
13. Extraction wells operating in September 1990
include RB-2, ORB-1, ORB-6, and ORB-7. These
wells do not appear to have a significant effect on
ground-water  flow in the B-aquifer zone. In  1986,
however, the cones of depression around extraction
wells ORBC-2, ORBC-3, ORB-1, and RB-3 were
evident.    The  extraction rate   from  the  B
aquiferwas  1,550 gpm in  1986 and 400  gpm in
September  1990.  The final design extraction rate
for the  onsite  and offsite B-aquifer wells  is
approximately 800 gpm.
                                                   150

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                         IBM-San Jose
Table 2
ESTIMATED FINAL SYSTEM EXTRACTION RATES
IBM-SAN JOSE SITE
Well
12A
A-17
A-53 .
ORA-04
ORA-5
ORB-06
RA-2
RA-11
RA-12
RA-14
RA-22
RA-24
RA-23
RA-25
RA-26
RA-27
RA-29
RA-30
RA-31
RA-32
RB-02
RB-07
RB-08
TOTAL
Flow Rate
Final Conditions
(gpm)
2
6.0
3.8
2
2
195
33.5
3.8
3.8
3.8
1.8
8.5
•5
13.5
3
41
33.5
22
7.5
10
260
105
1-5
872
Source: Kennedy, Jenks, Chilton, 1989.
151

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                                                                              IBM-San Jose
                                                                              SHEUSOL
                                                                              AREA
                                                               aim. 001/100   BUM. 001
                                                                            SUMP AREA
                          500
1000
                     SCALE IN FEET
                                                                     EXPLANATION

                                                                     Approximate area ictemitwa
                                                                    : for soil-vapor extraction
                            .  Approximato location of
                               lolt-vapor extraction wan
Sourcs: HLA, 1990d
                                                                   Bflur»11
                                                                   PHEUMINARY AREAS FOR
                                                                   SOIL-VAPOR EXTRACTION
                                                                   IBM-SAN JOSE SITE
                                              152

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                                                                                                                                         03
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                                                                                                                                         I
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                                                                                                                                         o
                                                                                                                                         CA
                                                                                                                                         a

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 Ul
o
50
TabteS
SUMMARY OF PRELIMINARY SOIL-VAPOR EXTRACTION
THIRD QUARTER 1990
IBM-SAN JOSE SITE

Area
Building
004
Shell Sol
140
Building
001/100
Building 006,
Tank Farm 067
Building 001
Sump
Estimated Cumulative Mass Removal (Ibs)
VOCs
Petroleum Hydrocarbons
Total Operating Time (hrs)
Average Extraction Rate (cfm)
1177
0
340
154.4
0
7.8
56
119
15.2
280
277
105
69
0
16.3
120
262
69
339
22
Estimated Mass Removal Rate (Ib/day)
VOCs
Petroleum Hydrocarbons
83
0
0
3.3
1.3
24
110
0
18.5
4.9
Source: HLA, November 1990
                                                                                                                    CD
                                                                                                                    s
                                                                                                                    o

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                                                                                        IBM-San Jose
Ground-water extraction from the C aquifer has
not occurred since April  1988.  September  1990
water levels in  the C-aquifer zone are shown in
Rgure 14.   Ground-water flow in the C-aquifer
zone at the  site is to the northwest.

Reductions   in   Mass  and  Concentrations  of
Contaminants

Monitoring-well  data  from  September  1989, to
September  1990, indicate little change in the area!
extent   and.  concentration  of   most   of  the
contaminant plumes in the A, B, and C aquifers in
comparison  to  what  is  shown   in  1988  data.
Figures 15,16, and 17 present the September 1989
to September  1990  mean  concentration-contour
maps of Freon 113, TCA, and 1,1-DCE in the A
aquifer.   In the  A aquifer, Freon 113 and  TCA
concentrations    remained   below   the   target
remediation standards of 18,000 ppb and 200 ppb,
respectively.     The  maximum  concentrations
observed during  the fourth  quarter of 1990  were
9,500 ppb  for  Freon 113 and 100 ppb  for  TCA
(HLA,  1990d).     The   maximum  1,1-DCE
concentration during the fourth quarter of 1990 in
the A  aquifer was 33 ppb, which exceeds the
target remediation  standard  of   6 ppb  (HLA,
1990d).  This standard was  exceeded in parts of
the onsite  area in 1989 and 1990,  as shown in
Figure 17.

The   only   contaminant   plume   that   showed
significant change was Freon 113 in the A aquifer.
Some decrease  in Freon  113 concentrations was
observed. Figures 3 and 15 present concentration-
contour  maps for Freon 113 in 1984, 1986, and
1990.  Freon concentrations in the  northern and
western parts of the site have been reduced by 1 to
2  orders of  magnitude.   However, the  high-
concentration area in the southeast has  not been
affected significantly.

B-aquifer concentration-contour maps of  Freon
113, TCA,  and 1,1-DCE  are presented in figures
18,  19,  and   20.    The  maximum   detected
concentrations were 1,100 ppb for Freon 113, 26
ppb  for TCA, and 8.2 ppb for 1,1-DCE (HLA,
1990d).     The  areas  of  greatest  Freon   113
contamination in  the B  aquifer are the same as
those in the A  aquifer,  suggesting downward
migration of Freon 113 from the A aquifer to the
B  aquifer.  In the B  aquifer, TCA concentrations
were below the target remediation  standard (50
ppb) in  1990; however, 1,1-DCE was detected at
8.2 ppb in one monitoring well, which exceeds the
1.5 ppb standard  (HLA,  1990d).   TCE  was
detected at 8.4 ppb,  which exceeds the 3.1 ppb
target remediation standard (HLA, 1990d).

Figures  21,   22,  and   23  present  C-aquifer
concentration-contour maps for Freon 113, TCA,
and 1,1-DCE.  Contaminant concentrations in the
C aquifer are significantly lower than in the A and
B   aquifers.     The  maximum  concentrations
observed were 90 ppb for Freon 113, 9.8 ppb for
TCA, and 0.7 ppb  for  1,1-DCE (HLA,  1990d).
All pollutant  concentrations were  below target
remediation standards in the C aquifer during  1990
(HLA, 1990d).

Although  ground-water  concentrations for  most
pollutants have not been reduced significantly by
the extraction  system since  1988, the system is
recovering pollutants.  Table 4  lists the estimated
mass  of Freon  113, TCA,  TCE, and  1,1-DCE
recovered during 1990.  The estimates are based
on average 1990 extraction-well concentrations and
the total ground-water volume extracted from each
well.  Most of the contaminants were recovered
from the B aquifer, where the extraction rates  were
highest.

Since the startup of a  Shell  Sol  140 recovery
system in 1989, approximately 2,500 gallons  of
product  have been recovered (HLA, 1991).  The
free product is recovered from skimming pumps
installed in wells throughout the plume.  The water
table is  depressed in- the plume area to facilitate
the recovery of free product.  Figure 24 shows the
extent of the nonaqueous and dissolved plumes of
Shell  Sol  140 in 1990.  The extent of the  free-
product  plume decreased somewhat from 1988 to
1990. Since 1990, concentrations of Shell Sol 140
in ground-water samples taken from wells with no
free product have decreased from 1 ppb or less to
below detection limits (IBM, 1991).

    SUMMARY OF REMEDIATION

Between  1988  and  1990, little   change  was
observed in the  area! extent of the contaminant
plumes.   Previously, between  startup and 1988,
there had been some reduction  in the plume.  The
Freon  113  concentrations  in the  A   aquifer
decreased by 1 to 2 orders of magnitude between
1984 and  1990 except for the  high-concentration
area near Building  004.  Although  no significant
reductions in concentration have been observed for
the other primary contaminants  since 1988,
                                                   156

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                                                            EXPLANATION

                                                       H.    SmiH •ocumolatkxw ol wnuWIM or
                                                            (MM predocl msMur*d in w«l during
                                                            eumni raped period.

                                                       O    Monitoring or obf*iv*lion w*l
                                                                               «l to
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                                                            m*Murad durtne in* period «p»f«»d in th* I
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                                                                                      200
Source: HLA, 1990d
                                                          pOM»IAti BCTENT OF SIELL SOL 140
                                                        IM THE A-AQUIFER FROM
                                                        JUNE 25,1990TO SiPTEMiER 28,1990
                                                        IBM-SAN JOSE SITE
                                                    167

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                        IBM-San Jose
Table 4
MASS OF POLLUTANTS RECOVERED FROM GROUNDWATER
. EXTRACTION WELLS IN 1990
Pollutant
Freon 113
TCA
1,1 -DCE
TCE
Estimated Mass Recovered (Ibs)
300
60
6
1.5
Source: HLA, 1991
168

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                                                                                        IBM-San Jose
 significant masses of contaminants were recovered
 by extraction wells.  The concentration of Freon
 ,113, TCA, TOE, and  1,1-DCE exceeded target
 remediation standards for the A aquifer in the third
 quarter of 1990.  TCE  was the only contaminant
 that exceeded the remediation standard for the B
 aquifer during the third quarter of 1990. 1,1-DCE
 and TCE were detected at concentrations  as high
 as 10 ppb and 8  ppb, respectively^  It is expected
 that recovery of  pollutants will  be  slow  at such
1 low concentrations.

    SUMMARY OF  NAPL-RELATED
                   ISSUES

 Two .types of nonaqueous phase liquids (NAPLs)
 are known or suspected to be present at the IBM
 San Jose site; light NAPLs  and dense NAPLS
 (DNAPLs).   The  spill  of approximately 8,100
 gallons of  Shell  Sol  140 in  November 1985,
 produced a floating layer of nonaqueous, or free-
 phase,  hydrocarbon,  as  shown in  Figure   6.
 Subsurface  leaks of Freon  113 and chlorinated
 solvents from storage tanks  and pipe lines may
 have also resulted in parts of the A aquifer being
 contaminated  with  DNAPLs.    The  areas   of
 suspected   and   known  NAPL  contamination
 correspond   approximately   to  the  areas    of
 preliminary soil-vapor extraction  shown in Figure
 11.              , 	

 NAPLs  in  the  Shell  Sol spill area are being
 remediated  by a  combination of SVE  and free-
 product skimming from recovery wells.   So far,
 approximately 2,500 gallons of free  product have
 been recovered from the system. The combination
 of recovery  techniques  appears  to have  the
 potential  to  remediate  the   Shell  Sol problem,
 according to experience with other hydrocarbon
 spills. Comparison of the NAPL-contaminated
 areas in Figures 6 and 24 indicates that the area of
 the floating NAPL layer was reduced considerably
 between 1988 and 1990.

 The suspected DNAPLs  consist primarily of Freon
 113, TCA, and 1,1-DCE.  The areas most  heavily
 contaminated with Freon 113  are in the A aquifer
 around Tank Farm  067  and the southwest corner
 of Building 004.  The solubility of Freon in water
 is approximately  170,000 ppb,  and  its specific
 gravity is about 1.48. Concentrations of Freon 113
 near 10 percent of its solubility have been detected
 in ground-water samples taken from the A aquifer
 in  the  Tank Farm 067 area,  suggesting  that
 DNAPL Freon may be present in this area.  Freon
concentrations greater than solubility have  been
detected in ground water from borings in this area
(HLA, 1987).

Comparison  of Figures  3 and 15  indicates that
there  has been  a considerable decrease  in the
extent of the Freon 113 plume over the course of
the remediation  and  that the maximum  ground-
water concentration of the Tank Farm 067 area has
decreased. However, there has been no significant
decrease  hi  the  concentrations around  Building
004. In  1990, the highest concentration of Freon
in  a  ground-water  sample  was  9,500  ppb,
measured in  A-aquifer  well A-69.    Freon
concentrations hi  the B aquifer also have  always
been highest in the Tank  Farm 067 area.  This is
directly below the parts of  the A aquifer that
initially had  the highest concentrations.  This may
be  indicative  of  the  downward  migration  of
DNAPLs through the A/B aquitard  in this  area;
however, hydraulic gradients are also downward in
this area, so downward  advection  of dissolved
constituents  is also possible.  The highest Freon
concentration in the B aquifer in 1990 was 1,100
ppb, measured in Well  B-22.   Likewise,  the
highest concentrations in  the C  aquifer are the
vicinity of Tank Farm 067,

The highest  concentrations of TCA and 1,1-DCE
have consistently been  in the A  aquifer  near
Building 001. The high concentrations in that area
have been persistent over the 6-year period  of
record, indicating that these  compounds  may be
present as DNAPLs.

Freon 113 concentrations in  the Tank Farm 067
area of  the A  aquifer, where  DNAPLs  are
suspected, have declined substantially since 1986.
A possible explanation for the decline is that the
potential  DNAPL has penetrated the A/B aquitard
in this  area,  leaving the relatively thin part of the
A aquifer below  the water table with Freon at no
more than residual saturation.  Because Freon is
volatile, it might not persist long above the water
table.
                                                   169
                        70S  6*77

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                                                                                    IBM-San Jose
      UPDATE  BIBLIOGRAPHY/
             REFERENCES

Harding Lawson  Associates (HLA).  June 1987.
Appendix B:   Summary of Hydrologic Studies,
Draft Comprehensive  Plan,  IBM  Groundwater
Restoration Program.

HLA. January 1989a.  Quarterly Report - Fourth
Quarter 1988, Groundwater Monitoring Program,
IBM Storage Systems Products Division, San Jose,
California.

HLA.    June 30,  1989b.     Predesign  Field
Investigation:  A-Aquifer Zone Extraction System,
Cottle Road Boundary Area.

HLA.  August 15, 1989c.  Criteria for  Decision
Analysis  of  Final  Plan  Implementation  and
Contingency   Proposal,   IBM  Groundwater
Protection Program, San Jose, California.

HLA.  January 18,  19~90a.  Recharge Evaluation
and Proposed Pilot Study, IBM General Products
Division, San Jose, California.

HLA. April 13, 1990b.  A-Aquifer Zone Boundary
and  Offsite Extraction  System, IBM  General
Products Division, San Jose California.

HLA.  May 14,  1990c.  Quarterly Report-First
Quarter 1990, Groundwater Monitoring Program,
IBM Storage Systems Products Division, San Jose,
California.

HLA.  November 2,  1990d.  Quarterly Report-
Third Quarter 1990,  Groundwater Monitoring
Program, IBM Storage Systems Products Division,
San Jose, California.

HLA.  June 19,  1991.  Personal communication
with Steven Walker, engineering geologist, HLA.

IBM.  February  1991.  Personal communication
with Marian Duncan of IBM.

Kennedy, Jenks, and Chilton.  August 1989. IBM
Groundwater   Protection   Program,   Onsite
Groundwater  Utilization, IBM General  Products
Division, San Jose, California.

McLaren Environmental Engineering.  March 20,
1989.  Preliminary Design Report,  International
Business Machines.
McLaren Hart.  October 1, 1990.  Groundwater
Recharge Pilot  Study and  Sampling  Plan, IBM
Storage  Systems Products  Division,  San  Jose,
California.

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.
                                                 170

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                                                UPDATE OF CASE STUDY 12

                                                         Nichols Engineering
                                          Hillsborough Township, New Jersey
Abstract

During 1990 and 1991, ground-water extraction has continued at the site. Since the system
startup in January 1988, CC14 concentration in ground water has been reduced by 80 to 90
percent in some wells. As of June 1991, site operators were in negotiations with NJDEP to
cease ground-water recovery operations 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
1987
January 1988
VOCs
Fractured shale, siltstone, sandstone,
and conglomerate
4
65 gpm
2 acres
100 feet
Carbon Tetrachloride 980 ppb
                                     171

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                               CASE STUDY UPDATE
      NICHOLS ENGINEERING  AND RESEARCH CORPORATION
                          BACKGROUND OF THE PROBLEM
            INTRODUCTION

The   original   case   study  for  the   Nichols
Engineering  and Research Corporation (NERC)
site (U.S. EPA, 1989, Case Study 12) was based
on monitoring data through October 6, 1988.  This
update is based on additional progress reports that
present monitoring data collected through April 4,
1990.   Ground  water at the site occurs in a
fractured rock  aquifer and has elevated  levels  pf
volatile   organic   compounds   (VOCs).
Administration of site cleanup is  being conducted
in accordance with the New Jersey Department  of
Environmental  Protection's   (NJDEP)
Environmental  Clean-up  and Responsibility Act
(ECRA).
The NERC site is located at  the southwest comer
of the intersection  of Willow and Hillsborough
Roads   in   HUlsbprough Township,   Somerset
County, New Jersey  (see Figure 1).   Figure 2
shows the site layout and the location of the  12
original  onsite monitoring wells.

The NERC facility was  involved in combustion
research from the early 1970s to 1983.  Ground-
water sampling beneath the NERC site performed
in 1986 and early  1987  revealed contamination
with  VOCs near  a subsurface wastewater settling
basin adjacent  to the west side of the pilot plant
(see Figure 2).  The basin is suspected  of being
the  source of the ground-water contamination
beneath  the site.  Results of water quality analyses
from the ground-water sampling program indicate
that three contaminant plumes of the VOCs carbon
tetrachloride  (CC14),  chloroform (CHC13), and
tetrachloroethylene (PCE) are centered near wells
MW-1 and MW-2, with the CC14 plume being the
most extensive.  The dashed outline in  Figure 2
indicates the approximate extent  of the plume  in
1988.

Remediation  began  in January  1988 with the
installation  of  a  ground-water recovery  system.
The original system consisted of one extraction
well at MW-3.  This well was selected because  of
its central location in  the contaminant plume and
because  aquifer test results suggested that it would
provide  the necessary capture zone.  Subsequent
revisions to  the extraction system  are discussed
below.

Based on  an analysis of pump test data, Storch
Engineers,  the environmental  consultants  for
Nichols,  postulated  a complex  aquifer  system
composed   of  two  marginally   independent
fractured-rock  aquifers.      The  uppermost
water-table  aquifer,  exhibiting  delayed  yield
behavior,  is  separated  from the  lower high
transmissivity, semi-unconfined zone by a 10- to
20-foot-thick   stratum   of   poorly   fractured
sedimentary   rocks.    The  confining  layer  is
penetrated by a number  of  vertical  or nearly
vertical fractures. The transmissivity tensor for the
lower zone,,is anisotropic, with  the major axis
parallel to the long axis of the contaminant plume
in a southeast to northwest orientation.

The water table ranges from 20 to 40 feet below
the ground surface  across the NERC site.  The
natural direction of ground-water flow is generally
toward the northwest.   However, during  certain
times  of the year there is a ground-water divide
near  well  MW-4  .(see   Figure 2),  and  water
southeast  of this  divide  flows toward  Royce
Brook. Estimates of the natural hydraulic gradient
vary between 0.034 and 0.007 depending on which
wells are used.  This indicates nonuniform flow,
which is typical of fractured-rock  aquifers.

           UPDATE ON SITE
          CHARACTERISTICS

Despite the addition of two new deep monitoring
wells at the NERC  site (MW-10D and MW-2D),
in January  1989 and January  1990, respectively
(see   Figure  3),   the   description   for   the
hydrogeology of the  site  has  not  been revised.
The new wells are 100 feet deep, with steel casing
from the ground surface down to a depth of 61
feet and open, unscreened well bores from a depth
of 61 to 100 feet (Storch Engineers, 1990). Well
MW-10D  is  200  feet  downgradient  from  the
suspected  contaminant source,  and MW-2D  is
immediately  downgradient.   The addition of  the
two  new  wells  brings   the  total number   of
monitoring wells at the site to 14. No core
                                             172

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                       Nichols Engineering
Nichols Engineering
       Site
        SITl LOCATION MAP
        NICHOLS ENQINffiWNa SfTE
        HIHS10ROUQH TOWN»«P. NEW JERSEY
  173
                     7/H

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                                                                   Nichols Engineering
       V
                                            APPROXIMATE  LIMIT
                                                                  (DESIGN}
       l*fl»ncl
       -$-  Monitoring Well (shown without MW prefixes)

            Recovery Wed
Sourn: Starch EnginMn, 1868b
Rgur»2
INITIAL MOMITORINO AND RECOVERY WELL
LOCATION MAP SHOWING GROUND-WATER DIVIDE
NICHOLS ENGINEERING SITE
                                           174

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                                                                                Nichols Engineering
samples were collected during (killing. Therefore,
the exact depth of different hydrogeologic layers is
unknown.  All of the wells  are open-bore rock
wells,  with a  depth of between 50 feet and lOO
feet.  Table 1  gives the well depths and estimated
casing depth  for  all  wells  (Storch  Engineers,
1991).

In  their  June  1989  progress   report,  Storch
Engineers asserts that evidence from the continued
sampling  of all wells  and discrete sampling of
wells MW-3, MW-H, and MW-12, and from the
site history indicate that the contaminants that have
been detected are present as a dissolved phase near
the top of the water-table aquifer, not as a dense
nonaqueous phase liquid (DNAPL).

The evidence used by system operators to rule out
the presence  of DNAPLs  includes the relatively
low 'concentrations  encountered   compared  to
concentrations expected if the pure product were
present, the higher concentrations near the surface
of   the   water  table,   and  the   decreasing
concentration   resulting   from   ground-water
extraction.     According   to  system   operators,
evaluation of trends in contaminant concentration
over time indicates  that the primary contaminant
source is located in the vadose zone rather than at
depth where the pure product (DNAPLs) of the
primary site contaminants would sink because they
are denser than water.  However, Storch Engineers
acknowledges  the  possibility mat DNAPLs might
be present in fractures deep beneath  (he site. Rock
fractures   at  the  site  are believed  to  extend
considerably below  the  deepest monitoring well
currently installed (Storch Engineers, 1991).

Continued monitoring  at  the  site revealed the
presence   of   additional  possible  ground-water
contaminants:   carbon   disulfide   (CS2),
trichloroethylene  (TCE),   toluene,  2-butanone
(MEK),   and  methylene   chloride   (DCM),
However, the predominant ground-water pollutants
are CC14, CHCI3, and PCE.

CS2 was  found in  the  two new deep  wells at
increasingly  greater concentrations following  its
initial detection in MW-10D in April 1989.  Site
operators suggest that the data are indicative of a
plume of CS2 in a dissolved phase at depth below
the water  table.  No evidence is offered for the
presence  of  CS2  as  a nonaqueous phase  liquid
(NAPL).
occasion at 160 ppb in MW-5. Storch Engineers
is  investigating whether the TCE detected  in
samples taken from wells  other than MW-5 is a
ground-water   contaminant   or  a  laboratory
contaminant  The high TCE levels in wel MW-5,
along with the discovery of other VOCs in that
well,  have  been  attributed  to other pollutant
sources and will not be discussed  in this case
study update.

Storch Engineers attributes the presence of toluene,
ethylbenzene, and xylene in MW-10 and MW-10D
to  exhaust   fumes  from   the  sampling  van,
generator, or traffic within  the immediate vicinity.
These  two wells are located in  a  parking  lot.
NJDEP does not dispute this possible explanation
(NJDEP, 1990).

MEK  contamination  of  MW-1,   MW-2, and
MW-11,  was  attributed to  the introduction  of
contaminants  into the ground-water during  the
installation of new  recovery  pumps  in these
monitoring wells.   Specifically,  the  suspected
source of MEK is the glue used to join segments
of the sampling tubes introduced into these wells.
MEK was no longer detected after removal of the
sampling tubes.

DCM  is  suspected  of   being  a  laboratory
contaminant.

              REMEDIATION

        Design and  Operational
       Features of Remediation
                  System

The   recovery  system   has  been   operating
continuously since January 22, 1988.  The initial
system consisted  of one pumping well (MW-3).
Modifications to the recovery system undertaken in
December 1988 and January 1989  included the
installation of submersible  pumps  in  MW-1,
MW-2, and  MW-11  (depths  for these  wells are
shown in Table 1).  Figure 3 shows  the modified
system.   The  total  pumping rate  of the four
recovery wells was maintained during the first half
of 1989 at the same rate of approximately 60 gpm
as that drawn from MW-3 initially. The individual
wells  were pumped at a rate of 30  gpm  (MW-3
and MW-11), 2 gpm (MW-2), and 1 gpm (MW-1).
Thereafter, the total pumping rate was reduced to
                                                   175
                     ia

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                                                                         Nichols Engineering
                                                                           \
                                                                        SAMPLING LOCATION
                                                                        METBi PIT
                                                               (DI«CHAft4E|OOIl
                                                                         w HUUA seweff-
     Legend
             Proposed Recovery wed
             Exiting Monitoring Well
             Existing Recovery WeB
             Meier Pft
             Now Discharge/Electrical Trench
             Existing cBsdiiigeffilectrtcallireneh
Source: Starch Engineers, 1990
NO*. •>"• —r t-ffrnii tii lin —-"*— -«'fn -H innp^
                                                  176

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                                                                                 Nichols Engineering
Table 1
MONITORING WELL DATA FOR
NICHOLS ENGINEERING SITE
Well No.
MW-1
MW-2
MW-2D
MW-3
MW-4
MW-5
MW-6
MW-7
MW-8
MW-9
MW-10
MW-10D
MW-11
MW-1 2
Well Depth
(ft)
60
60
100
100
65
60
60
60
50
55
60
100
100
100
Approximate Casing Depth
(ft)
15-20
15-20
61
15-20
15-20
15-20
15-20
15-20
15-20
15-20
15-20
61
15-20
15-20
between  36 and 42  gpm.  As  of May 9, 1990,
TCE was found intermittently at levels below the
reporting limit in wells MW-1, MW-2, MW-10,
and MW-11, and on one 53,700,000 gallons of
ground water had been recovered and discharged
into the Hillsborough Municipal Utility Authority
sanitary sewer system.

The reason for adding new wells to the extraction
system was to expedite ground-water remediation
by increasing the  rate of VOC reduction per unit
of ground  water removed.  The selection  of the
three additional recovery wells was  based  on the
observation that well  MW-11 was not showing any
significant  decrease in contaminant concentration.
Also,  all three of the new  wells are outside the
estimated zone  of capture of well  MW-3  in the
lower geologic stratum".
The  original extraction  system design analysis
incorporated  average  hydraulic  properties  and
assumed that  the aquifer  behaves as  a  single
homogeneous medium (see  Figure  3  in original
case study).   Capture-zone  analyses conducted
separately for the upper and lower hydrogeologic
strata show that wells MW-11, MW-1, and MW-2
lie within the capture zone of recovery well MW-3
within  the upper low transmissivity stratum but is
located beyond the capture zone that theoretically
develops in the lower high  transmissivity stratum
(see  Figures 4 and 5).  The capture-zone analyses
are  based  on  the  capture-zone  type  curves
developed by Javandel and Tsang (1986).  These
type curves assume a homogeneous and isotropic
porous  medium   with  uniform  natural  flow  of
ground  water.     The  technique  was  applied
separately  to  three separate  estimates  of  the
regional   ground-water  gradient   within  each
hydrogeologic  layer and the  resulting  capture
                                                   111
                       701

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                                                                                Nichols  Engineering
zones  were composited  using  best professional
judgement (Storch Engineers, 1991).

 EVALUATION OF PERFORMANCE

Figure 6 shows a  comparison of the  cone of
depression for the integrated potentiometric surface
(recall that  monitoring wells are open  throughout
their length below the water table)  associated with
the initial recovery system pumping at 60 gpm on
January 3,  1989, the modified recovery system
pumping at 60 gpm on  July 13,  1989, arid the
modified system pumping at 36 gpm on  June 21,
1990.  Storch Engineers has asked the NJDEP to
authorize further modification  of  the  system  by
relocating the MW-3 recovery pump to MW-10D
and by pumping the recovery wells intermittently.
The relocation of a recovery pump to MW-10D is
intended to reduce the CS2 level, which has been
detected  in  MW-10D  and   MW-2D.    The
intermittent  pumping  schedule  was  proposed
because  it  may  improve the   efficiency  of
contaminant recovery from the vadose  zone  by
allowing the water table to rise and saturate some
of the unsaturated zone.  Table  2  lists the results
of ground-water sampling in the monitoring wells
since  the start of remediation (Storch  Engineers,
1990).

Monitoring   wells  MW-1  and   MW-2   have
historically  exhibited   the   highest  VOC
concentrations.   Figures  7 and  8 present the
concentrations  of CC14  detected in target wells
MW-1, MW-2, MW-10,  and MW-11.  Isopleths
for CC14 and CHC13, which are  shown in Figures
9 and  10, provide a comparison between the size
and configuration of the  contaminant plume  on
January 6, 1988, and April 4, 1990.
               ..."        ,                , ,j
Based upon the results of the January 29-30, 1990,
and   April   4,   1990,  sampling  rounds,   CC14
concentrations  in monitoring Wells MW-1  and
MW-2 have been  reduced by  92.3 percent and
86.9 percent, respectively, since January 22, 1988.
The target  cleanup level  of 5 ppb for individual
VOCs (10  ppb for total VOCs) would require a
99.5 percent reduction of the original concentration
of CC14 in MW-1 and a 99.2 percent reduction in
monitoring  Well MW-2.  Figures 9 and  10 show
that the current recovery system has been  effective
at  lowering  the peak contaminant levels within the
plume and reducing the volume of ground water in
which the VOC concentration exceeds the target
cleanup level.   However, the rate of  decline of
CC14  in MW-1, MW-2,  and MW-11 decreased
during 1989 and 1990.  In each of their successive
progress reports, Storch Engineers re-estimated the
time required  to reach  cleanup  levels  based on
best-fit curves of VOC concentrations over time.
Because  of the decreasing  removal  rates,  this
estimate increased from 950 days in June 1989 to
1,400 days in August of 1989, to as much as 150
years in July of 1990  (Storch Engineers, 1989a,
1989e, and 1990).

Storch Engineers (1990) postulates a  number of
physical  and chemical  factors that  could  have
reduced the efficiency  of the recovery  system
being used at the MERC facility. Heterogeneities
in the aquifer can  result in  advective dispersion
that yields extremely long  flow paths  for portions
of the contaminant  plume.  Strataof reactive clays
or high organic content can retard portions of the
contaminant plume in relation to the  main body.
Precipitation may also result in flushing of residual
contamination   from  the  unsaturated  zone at
extremely slow rates.  Free-phase product may be
pooled in small, poorly connected fractures in the
unsaturated   zone,   providing   a   continuous
contaminant source.

Although   clear evidence  of  the  effects  of
heterogeneity and chemical retardation have not
been  provided, Storch  Engineers  has  shown  a
potential  correlation between high precipitation
levels  and  increased concentrations of VOCs in
ground  water  at the  MERC site (Figure  11).
Though the evidence 'is not without its ambiguities
because of the periodic nature of the ground-water
sampling data versus the continuous nature of the
precipitation records, the pattern  of fluctuation of
contaminant concentration  indicates a contaminant
source in the unsaturated zone (Storch Engineers,
1990).  Storch Engineers  (1990) postulates that
VOCs in the unsaturated zone are being mobilized
by   infiltrating  precipitation,  which  carries
dissolved  contaminants  into  the saturated  zone.
However, NJDEP does not agree that the evidence
for this correlation  is conclusive enough to justify
experimenting  with an induced infiltration system
(NJDEP,  1990).

    SUMMARY  OF REMEDIATION

The  NERC site has reported elevated levels of
VOCs (mainly CC14) in  the  ground  water.  A
ground-water recovery well has been in continuous
                                                   178

-------
                                                                   Nichols Engineering
                                                         CAPTURE  ZONE
                                                         UPPER STRATUM
      Ot STANCE (fttt)
     >  I t I i  i	-t	i t«(
           900      1000
Souret: Skxtti EnginMis. 19S8b

Nam: W»to thown wtwut MW pnribaw
Figur*4
CAPTURE ZONE (MW-3)
OPPiH STRATUM
NICHOLS ENGINEEPiNG
                                            179

-------
                                                               Nichols Engineering
                                                        CftPTURf ZONE
                                                        LOWER STRATUM
                                                        iKb«*SiJO"lft*/min.J
                                                        70-100* ft.dftpth
       100  200   3»   400
Source: Storch Enoin«ore, 1968b
FlgunS
CAPTURE ZONE (MW-3)
LOWER STRATUM
NICHOLS ENGINEERING -
                                          180

-------
  oo
                                                                                        ••BOW
                                                                                                                                IM
                                                                   MMMC(N)
              Potantbmalric «wrt»o» 01/03/M (tt abpva mtl)
                       MW-3 Pumping 60 gpm
      ace 07/13/89 (tt abov* ml)
MW-3, MW-11. and MW-2
Pumping Total of 80 gpffl
                                •  1M  2M  3M  4N  CM  «M
                                           DISTANCE (ft)
PaMnfaiMtrfc ttntec* 06/21/90 (ft abov* mil)
    MW-3.MW-11. MW-1. and MW-2
       Puniplng Total of 36 0pm •
         Soufca Stench EngioMCt. 1990
-4
                                    Figure 6
              (Poor Quality Original)  POTENTJOMETRtC SURFACE IN RESPONSE
              ^oor uuamy wnHinaij  JQ DrFERENT PUMPWG CONFIGURATIONS
                                    NICHOLS ENGINEERING SITE
                                               O
                                               £_
                                               (0
                                               m
                                               (Q

                                               
-------
oo
KJ

o
            o
            c
                    1000
                     800  -
                     eoo
                     400  -
                     200  -
                                                                                                               MW-1
                                                                                                               MW-2
                          1988
                                                                "T"
                                                                 1989
                                                                                                        1990
       Source • Data m TsH* 1 in Starch Enghwwt. 1890
                                                                                                      Figure 7

                                                                                                      CCU CONCENTRATION OVER TIME

                                                                                                      IN MW-1 AND MW-2

                                                                                                      NICHOLS ENGINEERING SITE
z~
o
o.
5"
m
to
                                                                                                                                     CD

-------
  oo
                     20
o
I

i
3
                      10
                         1988
-o
         Sourc* Data n T«M« 1 in Starch EngtfKwt. 1990
                                                                                                          1990
                                                                                                                             O
                                                                                                                             o.
                                                                                                                             (A
                                                                                                                             m
                                                                                           Figures
                                                                                           CCU CONCENTRATION OVER TIME   
-------
                                         TABLE 2. SAMPLING RESULTS (JANUARY 1988-APRIL 1990): NICHOLS ENGINEERING AND RESEARCH CORPORATION


                                                                                  (ConcwutMlm In ppto)
                                                                                                                                                                PAGE 10F5
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-------
                                                         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



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7/13*9

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-------
                                                        T*fitEZ.

                                                                                                                                                                               PAGE 5 Of 5
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                                             Nichols Engineering
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-------
                                                                         Nichols Engineering
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NICHOLS ENQINEERIMG - '£
                                               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

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                       Olin Corporation
196

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                                                                             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

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                            Olin Corporation
                                  i


                                fill!

                                  t

                                  I
                                  !
                                   §
,'••»
     198

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                      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

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          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
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                                                                     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

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                                                              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
                                                                                            o
                                                                                           •3
                                                                                            o-
                                                                                            I
                                                                                            o
                                                                                            3

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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

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                     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)\

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                      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

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                                                                       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

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                                                 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

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                                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

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                                                                    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

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                                                                                     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

-------
                                    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

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                                                             Savannah River Site
Source: U.S. DOE, 19iOa •
Figure 2
RECOVERY WELL LOCATIONS •
SEPTEMBER 19S9
SRS A/M-ARE6 SOT
                                       222
     •90fr   M77

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                                                                                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

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                                                                                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

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                                                                    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

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COMPARATIVE FAJUMETEM KHt CONTAMINANTS OF CONCERN-SAVANNAH HVBX POINT OF COMPLIANCE WELU (pf*>)

Wc«
MSB:
1A
2A
3A
4A
5A
6A
7A
8
13A
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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
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DW
458
292
220
314
DW
DW
8
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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

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DW
20
32
26
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<5.0
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                        Savannah River Site
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    227

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          Savannah River Site

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                 Savannah River Site
229
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       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
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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

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                                                                                  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

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                                                                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

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                                                                               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

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                                                                             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

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                                                  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

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                                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

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                        Site A
V

f
        /
                     ii
                    Hi
                O i	
                      i
                      I
                   O  m
                   £  I


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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
                                                                                                                               
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                                                                                                 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

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                                       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

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                                                                                 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

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                                                                                                 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

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                                                                                             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

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                                                  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

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                                                            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

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 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

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                                                                  Utah Power & Light
Source: Dames & Moors, 1989a
                                   {Poor Quality Original)
EXTRACTION AND MONITOR INO
WELL SYSTEM, MARCH 1989
LfTAH POWER & UQHT SITE
                                          249

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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
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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

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   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

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                                                                   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

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                                                                   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

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 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"

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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

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                                                  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%

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                                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

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                                                                 Verona Well Field
                                                             MAW
                                                             TWHKWWmt,
                                                             IUIWOAO
                                                             MAMMALLWa
                                                             YAM>
                                                                          4000 tL
ModHMtram: CH2M HILL, 1»68
srre LOCATION MAP
VERONA WEa FIELD SITE
                                        259

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                                                                          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

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                                                                            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%

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                                                                          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

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  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.

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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

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                                                                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

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               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

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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

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  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

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                 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

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                                                                  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

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                                                                            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

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-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"
_

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                  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

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                                                                            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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    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
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      ToMVOCs
                               1987
1988
                           1989
                                     200
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    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

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      RECORD OF CUMULATW VOC
      REMOVAL BY THE SOJL VAPOR
      EXTRACTION SYSTEM
      VETONA WELL FIELD SfTC

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                                                                          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

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                                                                     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
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     Source: EPA, I986c
                                                                                        LOCATION OF MID-SOUTH WOOD SITE
                                                                   (Poor Quality Original)    M RELATION TO MEHA, ARKANSAS
                                                                                        MID-SOUTH WOOD, MENA. ARKANSAS
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             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
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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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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
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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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         Mid-South Wood Products
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
IIDI

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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

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                             Mid-South Wood Products
§ti
                                         Hi Hi
                       302
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                                                                         SELECT CLAY

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            FABtttC WRAPPED

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            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
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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.
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                                                                                        i
                                                                               Rgureli
                                                                               OIL RECOVERY SYSTEM
                                                                               MID-SOUTH WOOD PRODUCTS STO

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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
                                                                                                                                                          o
                                                                                                                                                          a
                                                                                                                                                          I

                                                                                                                                                          I

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su
 O
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

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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

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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

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                                                                  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

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                                                                 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

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                                                                 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

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    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

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                                                                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

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                                      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

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             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?

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                                                                         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

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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

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                                                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

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                                                                       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

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              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

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                                                           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

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                                                          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

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                                                                         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

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                                         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

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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

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                                                                (Poor Qualttv Ortaliw!)   CONTOUR PLOTS OF WATER LEVEL ELEVATIONS
                                                                (roorwu»nyung,n»u   WTHEDEEpZONEf1if8 AND 1990


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                      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^  /   #

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DBCP Concentration Isoptelhs
                                                                                                       Sourc*: Wwton, Inc., 1990
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                      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
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                                                                              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
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                                                                         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

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   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
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    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
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                                                                           Figure 16
                                                                           MONTHLY AVERAGE CONCENTRATION OF DBCP (ppb)
                                                                           IN THE TREATMENT PLANT INFLUENT,
                                                                           1982 TO MARCH 1990
                                                                           OCCIDENTAL CHEMICAL SITE
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 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

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    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

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                                                                   SyIvester/Gilson Road
         0    1000   2000
           SatoinFMt

Sourc»: USGS, P«pp«mll Qusdnngto. 1979
Figui»1
STTE LOCATION MAP
NASHUA, NEW HAMPSHIRE
                                              343

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                                                Sylvester/Gilson Road
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                             344

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                                                                              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

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                  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

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                                                       Sylvester/GHson Road
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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

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                                                              Sylvester/GHson Road
Source: Western, 1989
                                                     Rgui»7
                                  (Poor Quality Original)  SLURRY WALL
                                              *     SYLVESTSW3JISON ROAD SITE
                                        353

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              Sylvester/Gilson Road
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                   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

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                                                                              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

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                   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

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  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
                                        0)
                                        "S.

                                        
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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

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                                                                         Tyson's Dump
       •"' ''^^^tSSSS^&^^^t^m-^ -H
                                                                 I  PENNSYLVANIA  /
Seal*       .            mim

 Source: SSP&A, I988a
                                      {Poor Quality OriglnaJ)
Figure 1
SITE LOCATION
TYSON'S DUMP SfTE
KING OF PRUSSIA, PENNSn
                                            376

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o

-J
                     Schuy*® Rv&r
            It
            u
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
                                                                                                                                             O

                                                                                                                                             •o

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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
                                                    379

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response to hydraulic loading and barometric
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on the island, was found to respond strongly to
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the river, and direct hydraulic connecdon between
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almost immediately to changes in river stage. The
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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

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               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

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              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

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                                                                      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

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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

»

to

-------
                                                                          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 
-------
-4
•  IJNO-MJM ft*
•  t-1.000 pjb
O  Mn din til I
17  «MNWIM>
                             ram PMOMIT FOtuuTMtr
(Poor ChuHty Orlglnrt)                         *™"
                                                                                                                                                                I
•o
5

-------
                                                    IUJMflfWM.1.
                                                    wen. WHIT i«?«i
                                                    IHFH.TMTIOH frSTCM
                                                 *  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

-------
        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

-------
                                                         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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