United States
             Environmental Protection
             Agency
             Office of
             Research and Development
             Washington, DC 20460
EPA/600/2-91/052
September 1991
&EPA
Fate of Polychlorinated
Biphenyls (PCBs) in Soil
Following Stabilization with
Quicklime
                                      7','A Printed on Recycled Paper

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                                 EPA/600/2-91/052
                                 September 1991
  FATE OF  POLYCHLORINATED  BIPHENYLS  (PCBs)
IN SOIL FOLLOWING STABILIZATION WITH QUICKLIME
                      by
      Robert  L.  Einhaus,  Issa  Honarkhah
        Technology Applications,  Inc.
           Cincinnati, Ohio  45268
                      and
               Patricia  Erickson
    Risk Reduction  Engineering Laboratory
           Cincinnati,  Ohio   45268
          Contract Number  68-CO-0001
    RISK REDUCTION  ENGINEERING  LABORATORY
      OFFICE OF RESEARCH AND DEVELOPMENT
     U.S.  ENVIRONMENTAL PROTECTION AGENCY
            CINCINNATI,  OHIO  45268

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                                 NOTICE
The information in this document has been funded wholly or in part by
the United States Environmental Protection Agency under Contract Number
68-CO-0001 to Technology Applications, Inc.  It has been subjected to
the Agency's peer and administrative review, and it has been approved
for publication as an EPA document.  Mention of trade names or
commercial products does not constitute endorsement or recommendation
for use.  Mention of trade names or commercial  products does not
constitute endorsement or recommendation for use.

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                                FOREWORD

Funding for this investigation was provided by the U.S. Environmental
Protection Agency's Technology Innovation Office, Technology Support
Project.  The study consists of a series of experiments to reproduce and
amplify results reported in the scientific and general media suggesting
that application of quicklime to contaminated soils for the purpose of
stabilization/solidification has the subsidiary effect of decomposing
polychlorinated biphenyls (PCBs).  Experiments using synthetic soils
fortified with pure PCB congeners describe the effects of quicklime
treatment on PCB levels, occurrence of PCB dechlorination products and
volatilization.  Analytical  results for stabilized soil from a PCB-
contaminated site are presented and discussed in order to assess the
verity of anecdotal claims made of quicklime.

Additional copies of this report may be obtained at no charge from the
EPA Center for Environmental Research Information, 26 West Martin Luther
King Drive, Cincinnati, Ohio 45268.  When ordering, use the EPA document
number found on the report's front cover.

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                                ABSTRACT
Several researchers have reported the destruction of polychlorinated
biphenyls (PCBs) in contaminated soil by application of quicklime.
These reports are based on retrospective data from site remediation
programs, anecdotal information and results of one bench-scale project.
Accordingly, an investigation was conducted to verify claims that use of
quicklime alone can promote decomposition of PCBs.  Synthetic soil
samples were spiked with three PCB congeners (3,5-dichlorobiphenyl,
S^SjS'-tetrachlorobiphenyl and 2,2/,4,4/,5,5/-hexachlorobiphenyl) and
treated with quicklime and water.  Significant PCB losses (60% to 85%)
were evidenced after five hours of treatment.  However, evaporation and
steam stripping at elevated temperature conditions, rather than PCB
decomposition, accounted for most of the losses observed.  Low levels of
partially dechlorinated PCB congeners were detected in lime-treated
samples, but the quantities were stoichiometrically trivial.  The
amounts of observed dechlorination products were not dependent on the
duration of lime treatment and no evidence of phenyl-phenyl  bond
cleavage was found.  Quicklime treatment in closed reaction vessels
(designed to contain potentially volatile PCB breakdown products)
demonstrated similar levels of dechlorination products and practically
quantitative recovery of unreacted PCBs.  An archived field sample
(stabilized oil lagoon sludge) purportedly free of PCBs as a result of
in-situ lime treatment was analyzed by gas chromatography with electron
capture detection and found to contain Aroclors 1242 and 1254 at a level
of 200 ppm.  The use of quicklime alone as an in-situ treatment for
removal of PCBs is not supported by these results.

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                                CONTENTS
                                                                  Page
Notice	.' .  .  .     ii
Foreword	     iii
Abstract	     iv
Figures   	     vii
Tables	     viii
Abbreviations and Symbols 	     ix
Acknowledgment  	     xi
Introduction  	     1
Background  	     5
      PCB Regulation	     5
      PCB Destruction 	     5
      Alternatives to PCB Destruction 	     6
      Lime-Based Processes  	     7
Methods and Materials 	     9
      Quicklime Treatment 	     9
      Open Vessel  Experiments 	     9
      Closed Vessel  Experiments 	     10
      Analysis of Synthetic Soils 	     11
      Analysis of Aroclors in Site Sample	     14
      Instrumentation	%	     16
      Apparatus	     16
      Reagents,  Standards and Testing Materials 	     17

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                          CONTENTS (Continued)
                                                                  Page
Results and Discussion  	    19
      Open Vessel Experiments 	    19
      Closed Vessel Experiments 	    32
      Analysis of Site Samples	    34
Conclusions	    41
References	    43
Appendix A:  RMC Draft Report	    46
Appendix B:  Mass Spectra	    67
Appendix C:  Evaporation Model and
              Supplemental Calculations 	    107

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                                 FIGURES


Number                                                            Page

  1.  Project Flowchart 	  	    3

  2.  Reactor and apparatus used for closed
       vessel treatments  	  	    11

  3.  Percentage of PCB congeners remaining  in
       synthetic soil  over 72 hours of lime
       treatment in open vessels	    20

  4.  Percentage of PCB congeners remaining  in
       untreated control samples  	    25

  5.  Comparison of observed PCB losses and
       modeled evaporative losses for open
       vessel, treated samples  	    28

  6.  GC/ECD chromatograms of replicate sample
       extracts of stabilized sludge from the
       Westville site  and a standard of
       combined Aroclors 1242 and 1254	    36

  7.  Total  ion chromatogram of stabilized sludge
       extract	    38
                                  vii

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                                 TABLES


                                                                  Page

 1.    Analytical  Conditions for Measurement
       of Congeners by 6C/MS	    13

 2.    Recovery of PCB Congeners in Spiked
       Synthetic  Soil	    13

 3.    Analytical  Conditions for Measurement
       of Aroclors by GC/ECD  	    15

 4.    PCB Congener Concentrations in Synthetic
       Soil  Samples over Seventy-Two Hours of
       Lime  Treatment in Open Vessels	    19

 5.    Mean Percentage of Spiked PCBs Recovered at
       Increasing Treatment Intervals 	    21

 6.    Maximum Reaction Temperatures Observed During
       Lime  Slaking in Open Beaker Experiments	    22

 7.    PCB Congener Concentrations in Control Samples  	    24

 8.    PCB Dechlorination Products Found in Open
       Vessel, Treated Extracts 	    30

 9.    Percent Recovery of PCB Congeners from
       Closed Vessel  Treatments 	    32

10.    Analysis of PCBs in Stabilized Lagoon Sludge
       from  the Westville Emergency Response Site 	    37
                                  vm

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                        ABBREVIATIONS AND SYMBOLS
ABBREVIATIONS
jig/mL
ARARs
CERCLA

cm
cm/sec
DCBP
9
g/cm2
g/cm3
GC/ECD
GC/MS
h
HCBP
kelvin
L
m
M
min
ml
mL/min
mm
m/z
PCB
ppm
psig
RCRA
RPD
rpm
RSD
TCBP
TSCA

SYMBOLS

Al
Ca
                 relevant and appropriate requirements
                 Environmental Response, Compensation, and
-- degrees Celsius
-- microgram(s)
-- micrograms per gram solid
-- micrograms per milliliter
-- microliter(s)
-- micrometer
-- applicable or
-- Comprehensive
   Liability Act
-- centimeter(s)
-- centimeters per second
-- 3,5-dichlorobiphenyl
-- gram(s)
-- grams per square centimeter
-- grams per cubic centimeter
-- gas chromatography with electron capture detector
-- gas chromatography/mass spectrometry
-- hour(s)
-- 2,2',4,4',5,5'-hexachlorobiphenyl
-- degrees Kelvin
-- liter(s)
-- meter(s)
-- molar concentration
-- minute(s)
-- milliliter(s)
-- milliliters per minute
-- millimeter(s)
-- mass-to-charge ratio
-- polychlorinated biphenyl
-- parts per million
-- pounds per square inch, gauge
-- Resource Conservation and Recovery Act
-- relative percent difference
-- revolutions per minute
-- relative standard deviation
-- 3,3',5,5'-tetrachlorobiphenyl
-- Toxic Substances Control  Act
-- aluminum
-- calcium

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 CaCl2
 CaO
 Ca(OH)2
 Cr
 Cu
 Fe
 HC1
 K
 KOH
 MeOH
 MeCl2
 Mg
 Mn
 Na
 NaOH
 N1
 Zn
            calcium chloride
            calcium oxide
            calcium hydroxide
            chromium
            copper
            iron
            hydrochloric acid
            potassium
            potassium hydroxide
            methanol
            methylene chloride
            magnesium
            manganese
            sodium
            sodium hydroxide
            nickel
            zinc
C
D
€
H
area; also constant for
temperature-dependent vapor
pressure calculation
constant for temperature-
dependent vapor pressure
calculation
concentration
diffusivity
porosity
height
K     transport coefficient
M     molecular weight; also mass
P*     pure-component vapor pressure
R     gas constant
p     vapor density
S     solvent mass
t     time
T     temperature
V     volume

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                             ACKNOWLEDGMENT

This report is the product of the efforts of many individuals and
several organizations.  Valuable direction on research priorities at the
inception and throughout the course of this project was provided by
Subhas Sikdar, Carl Brunner, John Ireland, Don Sanning, Guy Simes, John
Convery, and Tim Oppelt of EPA's Risk Reduction Engineering Laboratory
(RREL).  Similar direction from the analytical perspective was given by
Tom Bellar and Ann Alford-Stevens of EPA's Environmental Monitoring
Systems Laboratory—Cincinnati.  Robert Banner and Joseph Burkart of
RREL prepared the project safety plan and assisted in its
implementation.  Diana Kirk, RREL, contributed to the quality assurance
plan and provided logistical support for experimental work.  Louis
Thibodeaux of Louisiana State University lent his expertise in modelling
PCB volatilization under conditions specific to this study.  Leo
Weitzmann performed an extensive literature review of topics pertinent
to this report.  Battelle Columbus provided technical assistance in the
identification and measurement of PCB dechlorination products by GC/MS.
Stephen Winslow of Technology Applications, Inc. (TAI) performed
numerous sample extractions and cleanups, and assisted in lime
treatments.  Joan Van Dyne, Sharon Mullen, and Tracy Sawyers, also of
TAI, provided word processing support.   A number of independent
investigators participated in a review session and provided peer review
comments on the draft report:  Mitchell  Erickson of Argonne National
Laboratory; Art Friedman and Richard Ayen of Chemical Waste Management;
John Verbicky and Dan Olsen of General  Electric; Barbara Taylor of META
Environmental; Joseph Marinaccio and John Tyskewicz of Northeast
Utilities;  Gregory Felling and Sheila Scott of Reynolds Metals
Manufacturing; Dwayne Koszalka of Trinity Environmental; Robert Swank of
EPA-ERL-Athens; John Napier of Oak Ridge National  Laboratory; Edo
Pellizzari  of Research Triangle Institute; and Joan Bursey of Radian
Corporation.   To all  of these persons and organizations — our thanks.

                                   xi

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                              INTRODUCTION

Polychlorinated biphenyl (PCB) contamination is a significant problem at
Superfund sites, affecting 13% of such sites scheduled for a Record of
Decision in fiscal year 1991  (1).  In addition to Superfund sites,
wastes from active operations must meet disposal regulations authorized
under the Toxic Substances Control Act (TSCA) and/or the Resource
Conservation and Recovery Act (RCRA).  Carcinogenic activity is a major
concern in remediation of PCB contaminated sites (2).

Regulations allow PCB remediation, in various instances, by
incineration, burning in a high-efficiency boiler,  disposal in a
chemical waste landfill, or alternate methods (3).   Incineration and
landfill disposal have been used most widely to date at Superfund sites.
Both methods can be very costly when applied to large volumes of
contaminated soil or waste.  Alternative processes, such as
dechlorination by alkaline polyethylene glycol treatment, are attractive
if costs associated with material handling and treatment can be reduced.

At several field sites during the past two years, EPA Regional staff
have made observations that suggested an inexpensive alternative
treatment for PCBs might have been found.  After interim treatment of
PCB wastes with quicklime (CaO-containing materials) to stabilize the
material prior to remediation, large decreases in PCB content appeared
to occur.   Precise monitoring of the treatment and  statistical sampling
were not performed, since the treatment was not intended or expected to
destroy PCBs.  When decreases in PCBs, on the order of 90%, were
reported,  it was hypothesized that the alkaline material combined with
heat generated by quicklime slaking (conversion of calcium oxide to
calcium hydroxide) may have caused PCB decomposition.  Publicity about
these observations has led to premature interest in field application of

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quicklime treatment.

As a consequence of reports that quicklime might destroy PCBs, EPA
entered into a cooperative agreement with RMC Environmental and
Analytical Laboratories (RMC) to investigate the hypothesis in the
laboratory.  RMC's draft final report (Appendix A) showed a loss of PCBs
from synthetic soils spiked with three PCB congeners and treated with
quicklime and water.  However, the relatively small  project did not
include all the experiments needed to prove chemical decomposition of
PCBs as the major effect of quicklime treatment.  Alternative
explanations for apparent PCB losses include volatilization by
evaporation or steam stripping upon lime slaking --  an undesirable
outcome in open field application — and real or "analytical"
solidification.  Real solidification of PCBs may have a role in site
remediation; solidification has, in fact, been used  at Superfund sites
where PCBs and metals were found.  "Analytical" solidification — another
undesirable outcome--means that the extraction procedures which separate
PCBs from typical soil and waste matrices are not effective in
recovering PCBs from highly alkaline, lime-containing, or pozzolanic
matrices.

An in-house project was designed to answer some of the questions about
quicklime treatment of PCBs.  The work was conducted by Technology
Applications Inc., EPA's on-site contractor at the Cincinnati Research
Center, under the direction of the Risk Reduction Engineering Laboratory
(RREL) and the Environmental Monitoring Systems Laboratory.  The project
flowchart, shown in Figure 1, was designed to address uncertainties in
previous laboratory and field observations.  This report includes data
from the first phase of the project.

The first objective of the in-house project was to reproduce the
experiment designed by RMC and verify the loss of pure PCB congeners
from open reaction vessels.  Assuming that significant losses would be

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    I	3. RE-EVALUATE
    !       PREVIOUS LA8 STUDY
        t. RE-EVALUATE FIELD
           SAMPLES OR DATA
        5.  EVALUATE
          SOLIDIFICATION
                                                                UNTREATED
                                                                PCS-SOIL
                                                ACIDIFY, EXTRACT, __
                                                   CC/MS
                                                    YES
                                                     1.  EXAMINE
                                                        VOLATILIZATION
                                                     2. EXAMINE
                                                        DECOMPOSITION
                                                                                1
    1. VOLATILIZATION - SELECT 0= MOST PCS LOSS OCCURRED IK FIRST RVE HOURS,
    z DECOMPOSITION - SELECT IF ORGANIC PRODUCTS ARE NUMEROUS OR HIGH CONCENTRATION.
    a LAB STUOT -  TEST OUTDO. ACIDIFICATION. 6XTRACTIOM TO OGTERMB6 PROBLEM STEP.
    1 FIELD OBSERVATIONS - ANALYZE EXISTING DATA. NEW SAMPLES
    i SOLIDIFICATION - EXAMINE IF PCB« PRESENT BUT HARD TO EXTRACT.
Figure 1.   Project flowchart


observed,  the  second  objective of the project  was to measure PCB
migration  to the vapor phase via  evaporation or steam stripping  in
closed reactors.
In  both cases,  any potential  reaction products  would be  identified by
gas  chromatographic separation and mass  spectral matching.   In  the case
of  the closed reactors,  a mass balance would  be calculated  to
demonstrate that  reaction products and residual reactants  accounted  for
the  amount  of PCB present prior to reaction.  Closed vessel  tests were
designed to include commercial quicklime as well as  cement  kiln dust,  a
CaO-containing  material  that  had  been used in field  applications.

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The final objective of work completed to date was to investigate the
apparent loss of PCBs observed in the field.   Specifically,  a field
sample was analyzed using a vigorous extraction procedure to determine
if the PCBs were merely solidified during the sludge bulking process.
Further objectives, refined by results to date, are presented at the
conclusion of this report.

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                               BACKGROUND

PCB Regulation (3)

PCB use, storage and disposal are regulated under the Toxic Substance
Control Act (TSCA).  In addition, uncontrolled PCB disposal sites can be
subject to the Comprehensive Environmental Response, Compensation, and
Liability Act (CERCLA, Superfund) and the Resource Conservation and
Recovery Act (RCRA).  For active operations regulated under TSCA,
disposal requirements vary depending on PCB concentration.  Wastes at
levels above 500 ppm must be disposed by destruction of the PCBs.  At
levels between 50 and 500 ppm, disposal in a secure landfill is
acceptable.  Remediation requirements at CERCLA and emergency response
sites are risk-based, but include consideration of the above
restrictions as part of applicable or relevant and appropriate
requirements (ARARs).

PCB Destruction

PCB destruction is generally accomplished by incineration, the high-
temperature destruction of polychlorinated biphenyls.  The level of
performance accepted for incineration or alternate treatment is less
than 2 ppm PCBs in treatment residuals.

Chemical destruction is also used.  Numerous patented processes exist
for chemical decomposition of PCBs.   The most widely known
dechlorination methods are collectively called alkaline polyethylene
glycol (APEG)  treatment.   In the potassium (KPEG) process (4),  potassium
hydroxide (KOH)  reacts with PEG to form a potassium glycolate.   The
glycolate reacts with PCBs by nucleophilic substitution to yield a
lesser-chlorinated,  glycolate-substituted PCB.  Further reaction with

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KOH can yield hydroxy substitution as well.  The literature does not
indicate any evidence of phenyl-phenyl bond cleavage by APEG treatment.
Higher-chlorinated congeners are more reactive toward KPEG treatment
than lower-chlorinated congeners; sodium hydroxide (NaOH) can be
substituted for KOH with reduced reaction rates.  Calcium hydroxide
[Ca(OH)2]  has  not  been reported  as  an alkaline  reagent  for APEG
treatment, perhaps because of its limited solubility compared to NaOH
and KOH.

Numerous other PCB destruction processes have been reported in the
literature or patented, including reactive metal-organic reagent
processes (5-7), photolysis (8-9),  hydrogenation,  and biodegradation.
These methods have seen little or no application to PCB-contaminated
soils; methods including the reactive metals (such as elemental  sodium)
could not be applied safely to moist soils.  Recent patents or patent
applications include EPA's base-catalyzed decomposition (BCD) process
(10) and the Boelsing process developed in Germany (11).  The latter
process employs hydrophobitized quicklime as a dispersing agent  to
enhance the availability of PCBs to dechlorinating agents.

Alternatives to PCB Destruction

The destruction of hazardous compounds is not always required,
particularly at CERCLA and emergency response sites.  In such cases, the
risks of adverse effects on human health and environment are weighed
against the efficacy, cost and permanence of remediation alternatives to
select the appropriate cleanup strategy.

Solidification/stabilization is a common alternative to destroying
hazardous contaminants in soil or waste, or disposing the material in a
secure landfill.  Although most commonly applied to immobilized  metals,
solidification/stabilization has also been applied to immobilize organic
contaminants.   Organophilic binders are available that are intended

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specifically to immobilize organic compounds (12, 13).  PCB-containing
wastes were stabilized at two field tests with such materials but,
unfortunately, the waste properties did not allow a firm conclusion that
significant stabilization occurred (14, 15).  In the first case (14),
where the TCLP test was used to measure effectiveness, PCBs were below
the detection limit of 1 ppm in TCLP leachates of both treated and
untreated material.  It should be noted that PCBs were not the major
target contaminants in this study.  In the second case (15), where
reductions in PCB concentrations were reported, effects of treatment
could not be separated from the effects of dilution by mixing and
addition of treatment agent.

Lime-Based Processes

A search revealed two U.S. patents that refer to Ca(OH)2,  the slaking
product of quicklime, for PCB destruction in transformer oils or other
hydrocarbon liquids.  Thyagarajan (16) patented the use of hydroxides of
alkali or alkaline earth metals with any of several solvents to destroy
PCBs.  Thyagarajan specifically cited dechlorination of a decachloro-
congener by hydroxyl substitution for two of the chlorine atoms.
Wilwerding (17) patented the use of a Lewis acid, such as A1C13  or
FeCl3,  with  an alkali  metal  or  alkaline earth metal  hydroxide to
chemically alter PCBs.  Manchak (18) patented an apparatus and approach
to solidifying organic sludges with CaO.  While PCBs are not
specifically cited in the text of the patent,  the claims may include
stabilization of many organic compounds.

The impetus for this project derived from observations by EPA Regional
staff that suggested PCB losses following waste treatment with CaO-
containing materials.  PCB levels measured before and after such
materials were used to "bulk up" the wastes for handling prior to
remediation suggested significant losses,  on the order of 90%.  Regional
staff who brought the observations to RREL's attention correctly

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suggested alternative reasons for the apparent losses:   PCB dilution by
mixing with less contaminated waste or added materials,  concentration of
pre-treatment samples in "hot spots", analytical  problems,  etc., as well
as the possibility of PCB destruction.  Because the addition of CaO-
containing materials was not designed for PCB remediation,  the careful
measurements needed to document treatment effectiveness  had not been
performed.  Consequently, it was not possible to  evaluate existing data
to elucidate the mechanism of PCB loss.

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                          METHODS AND MATERIALS

Quicklime Treatment

The treatment procedure was performed in accordance with experiments
described by Soundararajan (Appendix A).  After 50 g of synthetic soil
and 120 g of calcined quicklime were combined and thoroughly stirred  in
a 1000 mL pyrex glass beaker, 50 ml of reagent water were added with
vigorous stirring.  Temperature was monitored during the stirring
process by thermocouple.  After a temperature spike was achieved (>175°C)
the mixture was covered with a watch glass and set aside for cooling.
The cooled reaction mixture (<100°C) was converted to a thick slurry  by
addition of more reagent water (about 200 ml).  The slurry was covered
with a watch glass and maintained at a temperature between 80°C and 90°C
for 3 h using a laboratory hot plate.  Afterward the treated mixture was
stored at ambient conditions in a fume hood while awaiting extraction
and GC/MS analysis.

Open Vessel Experiments

A 50 g aliquot of synthetic soil was distributed into each of seventeen
1000 ml beakers.  Each of fifteen aliquots was fortified with 50.0 ml of
a spiking solution containing the PCB congeners 3,5-dichlorobiphenyl
(DCBP), S.a'.S.B'-tetrachlorobiphenyl  (TCBP) and 2,2/,4,4/,5,5/-
hexachlorobiphenyl (HCBP).  Two aliquots were spiked with solvent only
(30% methylene chloride/70% methanol) and subsequently served as reagent
blanks.  After solvent evaporation 5 of these fortified soils were
reserved as untreated control samples.  The 10 remaining fortified
samples plus the reagent blanks were then processed through the
quicklime treatment procedure.   The 10 slaked samples were grouped into
5 sets of duplicate samples.   Each set was reserved for a holding time

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of 5, 12, 24, 48 or 72 h.  At the designated times, duplicate samples
were treated with 7.2 M HCl(aq).  The acid was added slowly with
frequent mixing until stable, mildly acidic conditions were achieved
(pH=3.5).  The resultant matrix consisted of the original synthetic soil
residue and approximately 600 ml of aqueous supernatant (CaClz[aq]).
The timing of this neutralization step was taken as the endpoint of the
treatment process.  Extraction of the resulting binary matrix typically
occurred within 24 h of the neutralization step.

The experimental regimen for the five untreated samples mimiced the
procedures followed for the treated samples, although without lime and
HC1 addition.  Slurries were prepared by water addition, and heated to
80-90°C for 3 h on a hot plate.  To each untreated soil sample, 600 ml
of water were added to simulate the binary matrix resulting from the
lime neutralization procedure performed on the treated samples.  The
latter step was performed on one untreated sample concurrently with the
neutralization of duplicate treated samples at 5, 12, 24, 48 and 72 h.

Closed Vessel Experiments

The apparatus consisted of a standard, 1000 ml pyrex glass, resin
reactor and accessory equipment illustrated in Figure 2.  The same mass
proportions of spiked synthetic soil and calcined quicklime employed in
open vessel experiments were placed in the resin reactor.  Slaking water
(50 ml) was added via a standard taper funnel  attachment with the high
torque mixer motor ON.  The mixer itself consisted of a household pastry
whisk.

To prevent the escape of volatilized materials around the mixer shaft, a
vacuum assist was employed to capture them in  a cold-trap and an
entrained bubbler containing methylene chloride.  Airflow through the
bubbler was moderate (200 mL/min) and only sufficient to eliminate
excursion losses.  This approach had the added benefit of allowing a
study of a contained reaction under otherwise  ambient conditions.
                                   10

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        Separatory Funnel
              A
                  Motor
   Thermocouple
   Heating
   Mantle -
A=LC

1

O1
i
Stirrer

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a 60% duty cycle for 5 minutes and centrifuged at 3000 rpm for
approximately 3 min.  After the methanol was decanted into the
separatory funnel containing the original aqueous supernatant, 100 ml of
a 50% methanol/50% methylene chloride solution were added to the soil
residue.  Sonication, centrifugation and decantation were carried out as
described above.  These procedures, beginning with the soil sonication
step, were repeated once more using 100 ml of methylene chloride.  The
separatory funnel contents were shaken vigorously for 2 min with
frequent venting.  After phase separation the methylene chloride layer
was drained through a sodium sulfate drying column into a 500-mL
volumetric flask.  The soil residue was then washed (without sonication)
with two additional 100 ml aliquots of methylene chloride.  The washings
were each centrifuged, decanted into the separatory funnel, shaken,
dried and collected as above. The combined extract was diluted to the
mark with methylene chloride and transferred to an amber bottle with a
teflon-lined screwcap to await analysis.  Because of the magnitude of
the original spiking level (-1000 ppm per PCS congener) no extract
concentration step was required.

Analysis of synthetic soil extracts by GC/MS utilized chromatographic
and MS conditions itemized in Table 1.  Quantitation of each PCB
congener was attained by a 5-point calibration curve of total ion
current relative response versus concentration.  Phenanthrene-d10 served
as the internal standard for calibration of DCBP and TCBP, while
chrysene-d12 was the  internal standard for HCBP.  Peak  identification
was confirmed by visual comparison of mass spectra obtained from sample
extracts with reference mass spectra for DCBP, TCBP and HCBP generated
in-house from the pure materials.  Chromatographic peaks other than the
spiked congeners (potential PCB breakdown products) were identified by
National Institute of Standards and Testing (NIST) library spectral
matching.

The performance of the described method in terms of precision and
accuracy was evaluated through the analysis of triplicate, spiked
                                   12

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synthetic soils at each of three concentration levels.  The method
performance data (Table 2) demonstrated a grand mean recovery of 90%,
with acceptable precision, at concentrations ranging from 1333 to 525
ppm.
  TABLE 1.   ANALYTICAL CONDITIONS FOR MEASUREMENT OF CONGENERS BY GC/MS
      Column:

      Carrier Gas:
      Injector Temp:
      Column Temp:
      Injector Vol:
      Scan Delay:
      Scan Range:
DB-5 Fused Silica Capillary,
30m x 0.25 mm(ID), 0.25 jim film thickness
He @ 30 cm/sec.
250 °C
120°C to 288 °C @ 6°C/min.
1.0  jiL, splitless (1 min.)
3.4 min.
35-450 m/z
      TABLE 2.  RECOVERY OF PCB CONGENERS IN SPIKED SYNTHETIC SOIL
SAMPLE1
Al
A2
A3
Bl
B2
B3
Cl
C2
C3
MEAN
S.D.
DCBP, %
86.5
85.3
86.2
86.4
87.6
87.9
89.7
88.4
87.8
87.3
1.3
TCBP, %
94.8
94.7
94.5
94.4
93.0
92.3
93.4
90.5
90.8
93.1
1.6
HCBP, %
88.7
86.5
88.0
91.4
88.1
88.0
92.6
90.6
89.7
89.3
1.8
'Samples  designated  A were spiked with  1333   jig/g of DCBP and HCBP,  1050
lig/g TCBP.  Samples designated B and C were spiked at 75% and 50% of
these concentrations, respectively.  Numbers following the letter
designation indicate replicate sample preparation and analyses.
                                   13

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Analysis of Aroclors in Site Sample

A solidified field sample archived during an emergency response cleanup
conducted in 1987 was analyzed for PCBs.  The purpose of this analysis
was to confirm the absence of PCBs, purportedly a consequence of in-situ
lime treatment.  A 5.00 g sample of the solidified sludge was acidified
to pH 2 with 7.2 M HC1 (aq).  Following the addition of 50 ml of
methanol, the mixture was sonicated for 5 min and centrifuged at 3000
rpm for approximately 3 min.  The supernatant was decanted into a 250 ml
separatory funnel.  Sonication and centrifugation steps were repeated
using 50 ml of methanol/methylene chloride (50%/50%, v/v).  This
supernatant was also transferred to the 250 ml separatory funnel which
was then shaken for 2 min.  After phase separation,  the methylene
chloride layer was drained through a sodium sulfate  drying column and
collected in a 500 ml volumetric flask.  These procedures (sonication,
centrifugation, separatory funnel liquid-liquid extraction,  drying and
collection of the extract) were repeated using three successive 100 ml
portions of methylene chloride.  The final extract volume was adjusted
to 500 ml_.

The oil content of these sludge extracts necessitated both florisil and
gel permeation chromatography (GPC) cleanups.  A 100 ml portion of the
methylene chloride extract was concentrated by Kuderna-Danish to 10 mL
and solvent exchanged to hexane.  The hexane extract was loaded on a 21-
g florisil column and eluted with 200 ml of 6% ethyl ether in hexane.
The eluate was concentrated nearly to dryness and reconstituted with 10
ml of methylene chloride.

GPC conditions consisted of a methylene chloride mobile phase set at a
flow rate of 5 mL/min (5 psig) and a column packed with 70 g of S-X3
Biobeads".   Retention  times  bounding  the collection  fraction  were
determined by injection of a calibration solution composed of a mixture
of Aroclors 1016 and 1260.  The column eluate was monitored  with an in-
line UV detector.  5 ml of the methylene chloride extract derived from
                                   14

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the florisil cleanup were loaded into the GPC loop injector and
processed through the above-stated cleanup conditions.  The collection
fraction (53 mL) was concentrated then solvent exchanged to hexane with
Kuderna-Danish apparatus yielding a final extract volume of 5.0 ml,

Identification and measurement of Aroclors was accomplished by gas
chromatography with election-capture-detection (GC/ECD) under analytical
conditions itemized in Table 3.  Quantitation of PCBs was accomplished
by means of an external  standard calibration procedure using standards
composed of mixed Aroclors.  More details of the PCB quantitation
procedure are presented in the Results and Discussion section of this
report.

  TABLE 3.   ANALYTICAL CONDITIONS  FOR  MEASUREMENT OF  AROCLORS  BY  GC/ECD
          Column:

          Carrier Gas:
          Detector:
          Make-up Gas:
          Injector Temp:
          Column Temp:
DB-5 fused silica capillary,
30m x 0.25 mm(ID), 0.25 ^m film thickness
He @ 30 cm/sec
Electron capture, Ni63, 350°C
5% methane/argon at 66 mL/min
250 °C
180 °C to 300 °C (? 15°C/min,
hold 6 300°C for 15 min
          Injection Volume:    1.0  nL,  splitless (1 min)
                                   15

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Instrumentation

GC/MS System - A Hewlett-Packard Model 5995 gas chromatograph/mass
spectrometer and RTE/6 data system were used to identify and measure
PCBs in all synthetic soil studies.  The system was equipped with a
Hewlett-Packard Model 7673A autosampler (robotic arm and injection
tower).  Separations were accomplished with a 30m x 0.25 mm (ID) DB-5
fused silica capillary column (J&W Scientific, Folsom, CA).

GC/ECD System - Analysis of Aroclors in stabilized sludges employed a
Hewlett-Packard Model 5890 gas chromatograph equipped with an electron
capture detector and a Model 7673A autosampler.  A PE/Nelson 760 Series
analytical interface and Nelson 2600 software were used to process
chromatographic data.  These separations were also accomplished with a
30m x 0.25 mm (ID) DB-5 fused silica capillary column.

GPC System - Cleanups were performed with a GPC Autoprep Model 1002A
(Analytical Biochemistry Laboratories, Inc., Columbia, MO).   An ISCO
Model UA5 absorbance/fluorescence detector with a biochemical flow cell
(10 mm path length, 100 \il volume) was fitted in-line to monitor GPC
column eluate.  The gel stationary phase consisted of 70 g of SX-3 Bio-
Beads (Bio-Rad, Richmond, CA) packed in a 2.5 x 50 cm glass column.  The
mobile phase was methylene chloride.

Apparatus

Reaction Vessel - For closed-vessel experiments.  Pyrex" organic
reaction vessel (1000 ml) with four-port lid, connecting "U" tube, and
24/40 standard taper joints.  (Fisher Scientific, Pittsburgh, PA)

Centrifuge - Model K, International Equipment Co.
                                   16

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Sonicator - Sonic Dismembrator, Model 300, (Fisher Scientific,
Pittsburgh, PA).  Used on 60% duty cycle.

Analytical Balance - Sartorius, Model 2405, microbalance, 30-g capacity
(Brinkman Instruments, Inc., Westbury, NY).

Hotplate - Thermolyne, Model HPA2235M, extra capacity hotplate (Fisher
Scientific, Pittsburgh, PA).

Other Specialty Glassware - Centrifuge bottles, 200 ml, with teflon
lined screw-caps; pre-cleaned amber glass reagent bottles, 500 ml, with
teflon-lined screw caps; injection vials, 1 ml, with teflon-lined septa
and crimp top lids; Kuderna-Danish (K-D) flask, 500 ml with 10 ml
concentration tube and 2-ball and 3-ball Snyder columns; microsyringes,
5 pi to 100 |iL (Hamilton).

Reagents, Standards and Testing Materials

Solvents - Pesticide-grade methylene chloride and hexane; HPLC-grade
methanol and ethyl ether.  (Burdick and Jackson, Muskegon, MI).

Sodium Sulfate - Anhydrous (J.T. Baker, Phillipsburg, NO).  Heated at
400°C for 1 h.

Florisil - Pesticide grade (Supelco, Bellefonte, PA).

Analytical Standards - 3,5-dichlorobiphenyl (AccuStandard, New Haven,
CT);  3,3/,5,5/-tetrachlorobiphenyl and 2,2/,4,4/,5,5/-hexachlorobiphenyl
(Ultra Scientific, North Kingstown, RI); Aroclor 1242 and Aroclor 1254
(USEPA Repository of Toxic and Hazardous Martials, Research Triangle
Park, NC); acenaphthene-d10, phenanthrene-d10  and chrysene-d12 (Supelco,
Bellefonte, PA).
                                   17

-------
PCB Stock Solution - 2.7564 g of 3,5-dichlorobiphenyl (DCBP) and 3.0004
g of 2,2/,4,4/,5,5/-hexachlorobiphenyl (HCBP) were each dissolved in a
30% methylene chloride/70% methanol (v/v) solution then diluted to 690
ml and 750 ml, respectively.  A 3.0016 g mass of 3,3',5,5'-
tetrachlorobiphenyl (TCBP) was dissolved in a 45% methylene chloride/55%
methanol solution and diluted to 950 mL.  A higher proportion of
methylene chloride was required to completely dissolve the TCBP congener
in the stock.  Resultant stock solution concentrations of DCBP, TCBP and
HCBP were 4000 jig/ml, 3160 ^g/mL, and 4000 pg/mL, respectively.

Primary Dilution Standard - Equal volumes of stock solutions were
combined.  The resultant solution served as both primary dilution
standard for GC/MS calibration and spiking solution for synthetic soils.
Concentrations of DCBP, TCBP and HCBP in this solution were 1333, 1053
and 1333 yg/mL, respectively.

Testing Materials - Quicklime was supplied by Austin White Lime Company
(Austin, Texas) and Chemical Lime Company (Clifton, Texas), the same
commercial vendors who supplied materials for RMC's studies.  Austin
White Lime, with a lot analysis of 94% CaO, was used almost exclusively
in this study.  Unless otherwise noted, the quicklime was heated in a
muffle furnace at 900°C for at least 3 h to drive off any absorbed
moisture and C02 and  cooled  prior to  use.   Following  heating,  the Austin
quicklime was analyzed in our laboratory and found to contain 65.3% Ca
(equivalent to 91.4% CaO), 0.4% Mg, 0.2% Al, and 0.1% Fe; Cr, Cu, K, Mn,
Na, Ni, and Zn were found at less than 500 ppm each.

Synthetic soil was prepared by mixing equal weight parts of diatomaceous
earth (Fisher Scientific, cat. no. 122-3), silicon dioxide (Fisher
Scientific, cat. no.  S150-3), and acid-washed Ottawa sand (U.S. Silica
Co., Ottawa, IL).  Prior to use, the Ottawa sand was washed with
hydrochloric acid, tap water, and distilled water, then air dried.
                                   18

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                         RESULTS AND DISCUSSION

Open Vessel Experiments

Analysis of synthetic soil samples following lime treatment in open
beakers evidenced pronounced losses of PCBs.  Table 4 lists PCB congener
concentrations (ng/g) obtained by GC/MS analyses of samples after 5, 12,
24, 48 ad 72 h of lime treatment.  The concentration of each congener as
a function of time of treatment is depicted graphically in Figure 3.
The data demonstrated that most PCB loss occurred during, or soon after,
the initial lime slaking process.  DCBP, TCBP and HCBP averaged 75%, 60%
and 85% reductions, respectively, in the 5 h samples, while losses in
subsequent treatment intervals (12 to 72 h) were small, but apparent,
for each congener.  The apparent increase in DCBP concentration at 72 h
is probably an artifact of experimental conditions as discussed later.
These results, while generally confirming the loss of PCBs in synthetic
soil following quicklime treatment reported by RMC, differ significantly
with regard to kinetics.

    TABLE 4.  PCB CONGENER CONCENTRATIONS IN SYNTHETIC SOIL SAMPLES1
        OVER SEVENTY-TWO HOURS OF LIME TREATMENT IN OPEN VESSELS
TIME
HOURS
5
12
24
48
72
DCBP (uq/crt
REP. 1
439
405
172
136
238
REP. 2
315
217
167
90
309
RPD2
16
30
1.5
20
13
TCBP (iia/crt
REP 1.
535
248
257
207
200
REP 2.
333
429
277
241
183
RPD
23
27
3
7
4



.7
.6
.4
HCBP (uq/q)
REP 1.
260
130
155
128
69
REP 2.
177
309
187
130
76
RPD
19
41
9
0
4



.4
.8
.8
'Soil  samples  were  spiked  at  1330,  1050  and  1330  jig/g  of DCBP,  TCBP  and
 HCBP respectively.
2RPD  = Relative  percent  difference
                                   19

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       120
           CONGENER REMAINING, %
                           DCBP
   40
 TIME, h

^-TCBP
HCBP
Figure 3.  Percentage of PCB congeners remaining  in  synthetic
           soil over 72 hours of lime treatment in open vessels.
Treatment times, (i.e., the intervals between the slaking procedure and
neutralization of lime) were chosen to characterize as  explicitly as
possible the incremental losses of PCBs during the early stages of
treatment (0-24 h).  The data thus obtained differed significantly from
the PCB decay profiles reported by RMC (Table 5).   In this study the
bulk of PCB losses were observed in the 5 h samples in  contrast to RMC
data which did not achieve comparable losses until the  48 h samples.
The RMC data discount the contribution of the slaking process alone to
the loss of PCBs and suggest rather that slaking must set up reaction
conditions which result in attenuated decomposition of  PCBs over time.
By implication, the loss of PCBs as a result of volatilization or steam
stripping is similarly discounted, since these effects  would be most
pronounced during the slaking process.  The concentration versus time
curves presented in Figure 3, on the other hand, invest far more
importance in the slaking process and its attending exothermic effects.
                                   20

-------
Further, gross observation of the open beaker slaking process  (conducted
in a glove box) certainly argues in favor of volatilization and steam
stripping contributing to PCB loss.  Copious volumes of steam  and dust
were evident when the slaking temperature reached about 105°C  and
continued for several minutes until the maximum temperature (175-195°C)
was reached.  Dust which accumulated on the floor and other interior
surfaces of the glove box contained DCBP, TCBP and HCBP at levels of 70,
77 and 79 [ig/g, respectively, after 10 samples were treated with lime.

    TABLE 5.  MEAN PERCENTAGE OF SPIKED PCBs RECOVERED AT INCREASING
           TREATMENT  LEVELS.   COMPARISON  OF  RREL  AND  RMC  DATA.
TIME
HOURS
5
12
24
48
72
DCBP (%)
RREL RMC
28.4
23.4
12.7 53.6
8.5 10.5
20.6
TCBP (%)
RREL RMC
41.3
32.3
25.5 68.8
21.3 1.0
18.2
HCBP (%)
RREL RMC
15.9
17.8
12.9 45.4
9.6 25.2
5.5
This investigation employed a higher proportion (2.4:1) of calcined
quicklime to soil compared to that recommended by RMC (2:1).  The
additional lime was necessary to ensure that a slaking temperature
greater that 175°C was achieved.  Informal communications with RMC had
indicated that RMC considered this threshold temperature to be critical
to the efficacy of the treatment process.  Table 6 lists the maximum
temperatures recorded by a thermocouple immersed in each soil-lime
matrix during slaking.  With the exception of one 5-h sample, all
samples achieved threshold temperature.
                                   21

-------
       TABLE  6.   MAXIMUM  TEMPERATURES  RECORDED DURING  LIME SLAKING
                         OPEN  BEAKER EXPERIMENTS
SAMPLE1
DESIGNATION
5-1
5-2
12-1
12-2
24-1
24-2
48-1
48-2
72-1
72-2

TEMPERATURES f°C)
171
185
186
177
188
185
189
185
182
182
Sample designation is  treatment  time  (h)  -  replicate  number.

A protocol requiring treatment and analysis of discrete 50 g soil
aliquots was adopted in this experiment as opposed to a single large
scale treatment with analysis of subsamples.  The former approach was
favored due to concerns about obtaining representative subsamples from a
slurry composed of suspended particulates with varying densities and
surface characteristics (e.g., sand versus diatomaceous earth versus
Ca(OH)2).   The sampling procedure employed by  RMC  was  not  explicitly
described (Appendix A).  It was surmised, given the number of replicate
samples reported per treatment interval, that the laboratory employed
some kind of subsampling procedure.

While the use of discrete samples eliminated potential errors associated
with subsampling, the data indicated that the former procedure had its
own intrinsic variability.  For example, at the inception of the slaking
procedure, the fortified soils were still somewhat damp with residual
spiking solution solvent (70% methanol/30% methylene chloride) that had
not evaporated after overnight drying.  The fortified soils were heated
on a warm hotplate (80°C) to remove this residual  solvent prior to lime
                                   22

-------
treatment.  Because preheating could possibly cause PCB evaporation,
several samples were not preheated in order that they could serve as ad
hoc controls.  The samples withheld from preheating included:  5 h,
replicate 1; 12 h, replicate 2; and, 72 h, replicates 1 and 2.  The
sample data (Table 4) indicate that preheating had a moderate effect on
post-treatment levels of the PCB congeners, with unheated samples
tending to display higher concentrations than their preheated
counterparts.  This effect, however, is augmented by another variable --
the maximum slaking temperature of each sample.

Variability in replicate samples was high in certain cases (Table 4).
The relative percent difference (RPD) in sample pairs ranged from 1.5 to
30% for DCBP, from 3.7 to 27% for TCBP and from 0.78 to 41% for HCBP.
Method validation studies (Table 2) showed very low variability induced
by spiking, extraction and analysis of untreated samples.  Accordingly,
high RPD in treated samples can be associated with the non-analytical
factors described above.

The 5 h sample pair differed in that replicate 2 was preheated while
replicate 1 was not; replicate 2 reached a maximum slaking temperature
14°C higher than that of replicate 1.  Both factors are consistent with
the higher PCB losses observed in replicate 2.  The 12 h sample pair
also differed in both factors:  the maximum temperature was 9°C higher
for replicate 1 but only replicate 2 was preheated.  In this case, the
preheating and higher maximum temperature produced different effects on
different congeners.  DCBP results showed higher loss in replicate 2,
the pre-heated sample.  In contrast, the other congeners showed higher
losses in replicate 1, the sample attaining a higher slaking
temperature.  It seems reasonable that DCBP should be more sensitive to
preheating than TCBP and HCBP since vapor pressure tends to decrease
with increasing chlorination of PCBs.  The greater losses of TCBP and
HCBP as a result of higher slaking temperature may be a consequence of a
significant vapor pressure gradient in this temperature range.  Data
from control samples, presented in the next section of this report, are
                                   23

-------
consistent with this interpretation.  The subject is discussed again
later in the report in conjunction with evaporation modeling.

The 24, 48 and 72 h sample pairs generally showed lower RPDs.  These
pairs were treated more equally:  both 24 and 48 h samples were
preheated, neither 72 h sample was preheated and maximum slaking
temperatures for each sample pair differed by no more than 4°C.

Further Evidence of Volatilization - As noted in the Methods and
Materials section, five spiked synthetic soil samples were reserved as
untreated controls.  These samples were excluded from lime addition and
the slaking procedure, but were otherwise processed identically to the
treated samples.  One untreated control was analyzed with each set of
duplicate treated samples at 5, 12, 24, 48 and 72 h.  Results of GC/MS
analysis of these untreated samples are presented in Table 7.  A plot of
percent recovery versus holding time is shown in Figure 4.


        TABLE 7.   PCB CONGENER CONCENTRATIONS1 IN CONTROL  SAMPLES
TIME2
HOURS
5
12
24
48
72

DCBP (uq/d)
577
515
420
241
629

TCBP (uq/d)
1011
978
975
893
863

HCBP (ua/q)
1346
1314
1257
994
1137
'Soil  samples  were spiked with  1333,  1053,  and  1333  jig/g  of DCBP,  TCBP
 and HCBP respectively.
212  and  24 h  samples  were preheated  to  remove spiking  solution  solvent.
                                   24

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       120
          CONGENER REMAINING, %
                                     40
                                   TIME, h
                          DCBP
HCBP
 Figure  4.   Percentage  of  PCB  congeners  remaining  in  untreated control
            samples.

 The  untreated  control  sample  held  for five hours  displayed a 57% loss of
 DCBP, while the congeners TCBP and HCBP were measured at practically
 100% of the original spiking  level.  Since DCBP is the most volatile of
 the  three congeners, the data suggest that this loss was due to
 evaporation, specifically during the 3  h heating  (80-90°C) of the sample
 slurries.  The untreated control samples contained no lime and consisted
 only of the synthetic  soil matrix and sufficient water to produce a
 slurry.  Arguably, had lime been present, as in the treated samples, the
 extent of DCBP volatilization during the heating process may have been
 mitigated by encapsulation.   But, by the same token,  the untreated
 controls did not undergo slaking, a process significantly more energetic
 (175-195°C)  than the comparatively innocuous heating  step.

Volatilization effects  for TCBP and HCBP were less pronounced.   Both
                                   25

-------
congeners displayed 10% to 15% losses over 72 h.   Heating of the
slurries for 3 h at 80-90°C seems to have had no  measurable impact on
the TCBP and HCBP congeners.   Rather, moderate losses appear to be an
effect more closely allied to time of exposure to open,  ambient
conditions, an effect consistent with materials having low vapor
pressure and distributed uniformly over a large surface  area.   It is
worth noting that the slopes  of the concentration versus time curves for
TCBP and HCBP (Figure 4) and  the slopes for these same congeners from 24
to 72 h treated samples (Figure 3) are quite similar.  This suggests
that evaporation is a plausible explanation for the losses of PCBs
evidenced over the second and third days of lime  treatment.

Evaporation Calculations - The losses of PCBs observed in open vessel
experiments were much higher  than could be accounted for by observed
decomposition products (discussed in a subsequent section).  The
evidence cited above, including significant losses of DCBP in untreated
control samples, suggested that evaporation and steam stripping were
responsible for PCB losses.

Calculations were made to estimate evaporation rates based on diffusive
transport and pure component  vapor pressures following the models
developed by Thibodeaux.  Detailed descriptions of the equations and
model results are given in Appendix C and summarized here.

The evaporation rate was assumed to be dependent  on evaporative surface
area and vapor phase PCB concentration modified by a transport
coefficient, K, cm/h:
                                 W = AKp                             (1)
where W is the evaporative loss rate, g/h, A is the surface area, cm,
and p is the PCB vapor concentration, g/cm3.   p is  calculated  from the
ideal gas law as:
                                 p = P^M                             (2)
                                     RT
                                   26

-------
where P* is the temperature-dependent pure component vapor pressure, mm
Hg, M is the molecular weight, g/mol, R is the gas constant  in  cm3 mm Hg
kelvin'WT1,  and  T is temperature,  kelvin.   P* was calculated as:

                             P* = exp(A+B/T)                         (3)

using literature values of P* at temperatures  in the range of 293°C  to
373°C kelvin to evaluate the empirical constants A and B.

The transport coefficient, K, cm/hr, was calculated according to:

                         K = 2D€1-33(l-e)   +       S                  (4)
                                   H            tAps

where D is diffusivity, cm2/hr,  e is matrix  porosity,  cm3/cm3, H is
material height, cm, S is solvent mass, g, t is time, h, A is surface
area, cm2,  and ps  is  the vapor density of  solvent,  g/cm3.  The ps term is
calculated from the  ideal gas law using the molecular weight of the
solvent.  The first  term of the transport coefficient equation  accounts
for evaporative losses while the second term represents losses  by steam
stripping.  D was calculated in several ways (see Appendix C).  The most
satisfactory agreement between observed and calculated losses was found
for
              Dpcb - 129.6/lV'5 /!_ + _L\-5/l_ + _1_\5         (5)
                         \298>  \M.1P   267/  \M.1P    Mp/

where Mpcb and Mair are the molecular weights of the appropriate congener
and air, respectively.  The exact value of D for a given congener and
temperature was calculated by ratio with a published diffusivity for
Aroclor 1242 (Mpcb = 267) of 129.6 cm/hr at 25°C:
The evaporation rates, W, were calculated and summed over the
temperature-time regime used in the open vessel experiments.  Results
                                   27

-------
are shown in Figure 5 for the calculated values that best match the
experimental data.  The data and calculated values agree well in a
qualitative sense; that is, the shapes of the observed and calculated
PCB loss-time curves are similar.  Thus, evaporation and steam stripping
loss mechanisms can account for the open-vessel test results.

The quantitative match between observed and calculated values is not
satisfactory.  Calculations showed that the model is sensitive to
changes in porosity, matrix height, and pure component vapor pressure
among other parameters.  Data from untreated, control samples showed
significant losses (Table 7), illustrating that PCB volatilization
occurs both at room temperature and at the 90°C temperature used for
slurry heating.  While the model also showed losses to the vapor phase
at room temperature (5-72 h), the magnitude of loss is too small to be
observed on Figure 5.  These data suggest that the pure-component vapor
pressure-temperature relationships used in the model underestimate
       120
          CONGENER REMAINING, percent
              DCBP, real
              DCBP, calc
        40
     TIME, hr

-*— TCBP, real
 +  TCBP, calc
                                                   60
-*-  HCBP, real
 *   HCBP, calc
                  80
Figure 5.  Comparison of observed PCB losses and modeled evaporative
           losses for open vessel, treated samples.
                                   28

-------
volatilization.  This finding is not unexpected because published values
are generally available only for Aroclors and there is conflicting data
for some Aroclors (See Appendix C).

Evidence of PCB Decomposition - Analysis of extracts from the open
beaker reactions revealed organic compounds not present in the PCB
spiking solution or matrix blank samples (Table 8).  Chromatograms and
mass spectra are provided in Appendix B.

All tentatively identified compounds are conceivable products of PCB
decomposition (19), with partially dechlorinated and hydroxy-substituted
biphenyls as the dominant products.  Product concentrations, assuming a
response factor equal to that of chrysene-d12, ranged from 1 to 76 ppm,
with a cumulative maximum of 5% decomposition of the starting materials
in any one sample.

Although these results indicate that PCB decomposition occurred upon
quicklime treatment, the extent of decomposition was too small to
consider as successful destruction of PCBs.  Further, there appeared to
be no trend of increasing product concentration as treatment time
increased.  Finally, in no case was any completely dechlorinated
biphenyl observed.

More products and higher product concentrations were observed in samples
that were not preheated to remove residual  solvent.  Moreover, methoxy
derivatives were found in samples that were not heated to remove the
spiking solvent, suggesting the possibility that methanol in the spiking
solvent may participate in the PCB reaction.  A similar result was
observed by Brunelle and Singleton (4) in their studies of KPEG
treatment; in the KPEG case, methanol  hindered the desired glycolate
substitution.  Nucleophilic substitution for chlorine by alkoxide is
also discussed by Hutzinger et al. (19).  There did not appear to be any
correlation between products formed and maximum reaction temperature in
this study, although the temperature range  examined was quite narrow.
                                   29

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             TABLE 8.   PCB DECHLORINATION PRODUCTS  FOUND IN OPEN VESSEL TREATED EXTRACTS
COMPOUND IDENTIFICATION1
monochloroblphenyl
hydroxymonochlorobiphenyl
dichlorobiphenyl'
trichlorobiphenyl
hydroxytrlchlorobiphenyl
methoxytrichlorobiphenyl
tetrachlorobiphenyl3
pentachlorobiphenyl
hydroxypentachlorobiphenyl
methoxypentachlorobiphenyl
tetrachlorodibenzofuran*
05-1*
4

1
11

4

10

16
2
05-2




3

1

13

6
12-1
29

23
66

7
14
34
7*
24
1
12-2








8

4
24-1






1

38

11
24-2






1

24

12
48-1




2

1

26

14
48-2




1

1

31

12
72-1
27
1*
16
53
4
9

24
70
12
5
72-2
32
1
16
50
3
4
4
25
76
14
4
GO
O
             Concentrations  are In |ig/g, assuming a response factor equal  to that of chrysene-d!2.   Identification
             of   specific  isomers of these compounds was generally not possible;  more than one  isomer was observed
             for  some  compounds.

             Samples are designated by time-replicate number.

             Di-and tetrachloro biphenyls shown on this table had different retention times than  the DCBP and TCBP
             isomers used  in spiking.

             Tetrachlorodibenzofuran was quantified based on a measured response  factor of 0.359  relative to
             chrysene-d!2.
              Indicates  a  more tentative identification than for most products.

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Observation of a tetrachlorodibenzofuran (TCDF) in several extracts is a
cause for concern because of the potential  toxicity of polychlorinated
dibenzofurans compounds.  A pure sample of 2,3,7,8-
tetrachlorodibenzofuran was analyzed by GC/MS to confirm the
identification.  The GC retention time of the pure compound agreed
almost exactly with that of the tentatively identified product (Appendix
B).  Selection of the HCBP congener chlorinated in the 2 and 21
positions for this study may have facilitated dibenzofuran formation:
chlorination adjacent to the biphenyl bond should lend itself to hydroxy
substitution and HC1 elimination.  Hutzinger et al. (19) reviewed a
number of pathways, including KOH fusion, that can yield substituted
dibenzofurans.  While formation of dibenzofurans was not reported for
the APEG process, studies with pure congeners did not include those that
would most readily allow their formation (4).  It should be noted that
the reaction products observed in this study would probably not have
been detected if Aroclors were used, owing to the complex chromatogram
of mixed PCB congeners.

Decomposition products observed in this open-beaker study do not agree
with compounds observed in RMC's study.  RMC reported a substituted
phenol and alkyl- and chloro-substituted cyclohexanes in extracts of
reaction mixtures (Appendix A), while we observed only compounds
containing the intact phenyl-phenyl structure.  Analysis of all extracts
from treated and control samples was performed in this study without
concentration.  However, in this study a matrix blank sample (synthetic
soil spiked only with methanol/methylene chloride solvent, then treated
with quicklime and water) yielded six small  chromatographic peaks when
extracted and concentrated 500-fold (See Appendix B).   Two peaks were
large enough to be tentatively identified as bis-(2-ethylhexyl)-
phthalate and 2,6-bis-(l,l-dimethylethyl)-4-methylphenol.   The latter
compound is the common antioxidant BHT; the former is a well-documented
contaminant associated with plastics.  BHT was one of several  compounds
identified in RMC's report as a PCB breakdown product.
                                   31

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Closed Vessel Experiments


Closed-vessel experiments were conducted to quantify PCBs and possible
decomposition products volatilized during lime slaking and subsequent
heating of the reaction mixture.  The results of four separate
experiments using quicklime are summarized in Table 9.

  TABLE 9.  PERCENT RECOVERY OF PCB CONGENERS FROM CLOSED-VESSEL TESTS
TREATMENT
Quicklime


Quicklime
(10% MeOH
in Water)
Kiln Dust


Kiln Dust +
Quicklime
(1:1)
SAMPLE1
EXTR-1
SOLV-1
TOTAL -1
EXTR-2
SOLV-2
TOTAL -2
EXTR-3
SOLV-3
TOTAL -3
EXTR-4
SOLV-4
TOTAL -4
DCBP
50.0
17.3
67.3
84.4
3.9
88.3
102
3.5
106
86.9
6.7
93.6
TCBP
75.1
2.0
77.1
88.7
1.3
90.0
110
1.0
111
102
1.0
103
HCBP
64.3
1.0
65.3
89.3
0.5
89.8
122
1.0
123
87.1
2.5
89.6
MONO2
ND
.02

1.2
.30

ND
ND

.04
.20

TRI2
ND
.01

.13
.19

ND
ND

.06
.10

'EXTR and  SOLV refer to  solids  extract  and  cold  trap/bubbler  solvent,
 respectively.

2MONO and  TRI  refer to  isomers  of  mono-  and trichlorobiphenyl.
Concentrations were calculated by assuming response factors for MONO and
TRI equal  to that of the nearest internal  standard.  Recovery of MONO
and TRI is given as the percent of total PCB spike (all  congeners)
by weight.


Recoveries of PCBs ranged from 67.3 to 106% for DCBP,  from 77.1 to 111%

for TCBP,  and 65.3 to 123% for HCBP.  Lower recoveries in the first

sample receiving quicklime treatment (TOTAL-1) may be due to

volatilization of PCBs during evaporation  of spiking solvent, losses in

transferring the spiked soil to the reaction vessel, or leaks in the
                                   32

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apparatus.  The unusually high recovery of HCBP (123%) in the closed
vessel experiment using only kiln dust (TOTAL-3) is probably an
analytical artifact because all three congeners evidenced a small to
moderate positive bias in this run.

Compared to open beaker experiments, the closed-vessel experiments
yielded higher overall recoveries of PCBs, as expected, but less
volatilization losses than expected.  At 24 h, open-beaker extract
recoveries of DCBP, TCBP, and HCBP averaged 13, 25 and 13% of starting
concentrations, respectively.  At the same reaction time, closed-vessel
extracts yielded average recoveries of 87, 94 and 91%, respectively.
The higher recoveries from the solid phase in closed vessels may be due
to altered air flow conditions.  In the open-vessel tests, the reacting .
material was directly exposed to a high-velocity air sweep in the glove
box; in each test a column of particulate-laden steam was observed
rising from the beaker toward the exhaust port of the glove box.  The
closed vessels were operated under a low-velocity air flow and with a
flow path constrained by the reaction vessel lid, access ports, and a
small-diameter u-tube connection to the cold trap (Figure 2).  Mobilized
particulates settled on the vessel lid and walls and on the vessel side
of the u-tube.  Therefore, much of the material lost in the beaker tests
would have been recovered with the solid phase in the closed-reactor
tests.  The cold trap and bubbler (Figure 2) yielded 3.5 to 17% of the
DCBP and 0.05 to 2.5% of the other congeners in the closed reactions.
Condensation was visible on the reaction vessel lid, but could not be
quantified separate from the reaction vessel contents.

Very small amounts of dechlorination products were observed in the
closed-vessel reactions.   Mono- and trichlorobiphenyl congeners were
observed at estimated concentrations totalling 1.5% or less of the
original total PCB spike.  The lower degree of decomposition observed in
the closed vessels relative to the open beakers may be due to lower
reaction temperature in the former.  Slaking temperature could not be
measured in the closed vessels, but a lower temperature may have
                                   33

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resulted from less efficient mixing by the mechanical stirrer.
Likewise, kiln dust, having a lower percentage of CaO than quicklime,
would not be expected to display as much exothermicity during slaking.

The closed vessel experiment where methanol was added to the slaking
water evidenced the highest percentage of dechlorination products (mono-
and trichlorobiphenyls), though the differences were not dramatic.  The
use of methanol to enhance PCB dechlorination was suggested by evidence
from open-vessel experiments as well as literature reports (4,19).

Analysis of Site Sample

During the course of this investigation the laboratory received an
archived field sample dating back to a 1987 emergency response cleanup
action at
-------
qualitatively  and quantitatively reproducible  patterns of Aroclors  1242
and 1254,  as depicted in Figure 6.  The  estimated average concentration
of total  PCBs  in the replicate samples  (Table  10) was 200 jig/g  (ppm).
Quantitation of total PCBs was referenced  to total  area counts  of the
chromatogram between retention times of  11  and 22 min.  Total peak  area
was converted  to extract concentration using a response factor  derived
from a  five point calibration curve.  Calibration standards consisted of
equal parts by mass of Aroclors 1242 and 1254  serially diluted  in
hexane.   Extract concentration was translated  into sample concentration
using the  following equation:
where Cs is the sample  concentration, ng/g, Cex  is  the extract
concentration,  ng/mL,  F1  is  a correction factor equalling  10,  Vex is the
final extract  volume,  ml, and Ms is the mass of the  sample,  g.

The PCB level  reported in Table 10 exceeds  the  value reported for this
site one year  after emergency response  remediation (<1 ng/g) by two
orders of magnitude.   The level even exceeds the maximum value reported
(157 ng/g)  in  the  initial TSCA investigation prior to any stabilization
and compositing of the lagoon sediments.  What  can account for these
discrepancies?

Analysis of PCBs  in contaminated soils, sludges and  sediments is not a
straightforward procedure.  Extreme care must be taken to ensure that
the PCBs are exhaustively extracted from the sample  matrix and that,
once extracted, levels of interferences such as oils,  sulfur and organic
contaminants are  sufficiently reduced by cleanup steps to allow for an
  F 1s a unitless, composite correction factor accounting for fraction of the Initial extract which was cleaned
up and analyzed (100 out of 500 ml), as well as for the loss of extract  (5 out of 10 mL) that results from
loading of the GPC loop Injector.
                                    35

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                                                   SAMPLE,  REP 1
                                                   SAMPLE,  REP 2
                                                   SAMPLE REP 3
                                                   SAMPLE REP 4
                                        STD - AROCLORS  1242 & 1254
                10     12     14     16     18     20    22     24    26

                            TIME, min
Figure 6.  GC/ECD chromatograms of replicate sample extracts of
           stabilized sludge from the Westville site and a standard
           of combined Aroclors 1242 and 1254.
                                   36

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unambiguous identification and accurate quantitation of characteristic
Aroclor chromatographic patterns.  Even with relatively clean samples,
established chromatographic methods for PCBs have historically evidenced
poor reproducibility in multilaboratory applications (20).

         TABLE 10.   ANALYSIS  OF  PCBs  IN  STABILIZED  LAGOON  SLUDGE
               FROM THE WESTVILLE EMERGENCY  RESPONSE  SITE
Replicate
Samples
1
2
3
4



Concentration
as Aroclors




mean
std. dev.
RSD (%)
of PCBs (ug/g)
1242 and 1254
202
197
190
210
199.8
8.4
4.2
In light of these circumstances the discrepancies in reported PCB levels
noted above are not surprising, particularly when one considers that the
samples in question are oil lagoon sludges replete with several types of
interferences (oil, sulfur, other semivolatile organics).  To illustrate
the magnitude of the analytical problem, consider a GC/MS chromatogram
of the identical lagoon sludge sample shown in Figure 8.  The sample was
processed through both florisil and GPC cleanups.  Gravimetric residue
analysis of the sample extract evidenced a 94% cleanup efficiency.
Nonetheless, the hopelessly intractable GC/MS chromatogram in Figure 8
was obtained.  An attempt to measure PCBs in this sample using approved
GC/MS methods (21) would more than likely have resulted in a reported
zero or "not detected" concentration, because aliphatic interferences
have completely obliterated the characteristic Aroclor peak patterns and
PCB mass spectra.
                                   37

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 o;
       i • i • i ' i * i • i • i—i—i—i—i—i ' i • i • i • i • i • i
                         16      20      24      28
Figure 7.  Total ion chromatogram of stabilized sludge extract.


These interference problems are not entirely obviated by application of
electron capture detection.  Characteristically high levels of sulfur in
these oil-bearing sludges can impair Aroclor pattern recognition just as
effectively as aliphatic interferences in GC/MS.   GPC cleanup, designed
to remove both organic constituents and sulfur, is not 100% effective,
particularly when levels of these interferences exceed the capacity of
the gel.  This laboratory, for example, has encountered municipal
sludges and marine sediments where the method-recommended sample size
had to be adjusted downward to accommodate GPC column capacity, or which
otherwise required an additional  extract cleanup  with activated copper.

Problems related to instrument selection, chromatographic interpretation
and extract cleanup notwithstanding, the difficulty of simply extracting
PCBs from porous soil and sediments has been well documented (22, 23).
The most plausible mechanism accounting for the poor extractability of
PCBs in soils by conventional techniques (as well as for the persistence
                                   38

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of PCBs in the environment) is encapsulation by water (24).  Several
analytical strategies have been routinely employed to recover PCBs from
moist porous soil matrices.  One approach is to use a hydrophilic
partitioning solvent, such as methanol, to mobilize the PCBs.  This
process can be enhanced by sonication.  The PCBs are thus made more
accessible to the extracting solvent, in this case, methylene chloride.
A second approach involves mineral acid digestion, where the focus is
more on breaking down the porous fabric of the matrix itself.  This
digestion can employ HC1, H2S04 or HF.  The latter, while quite
effective, is somewhat cumbersome and precludes the use of conventional
glassware.  Sulfuric acid digestion is contraindicated for stabilized
soils since this process results in the formation of insoluble calcium
sulfate (gypsum) which could also encapsulate the PCBs.

To determine whether the Westville lagoon sludge presented PCB
extraction problems which demanded use of the above procedures,  the
sample was reanalyzed using Soxhlet extraction without acid digestion.
All other method conditions, including cleanup, were identical to those
employed in the prior analysis (Table 10).  Soxhlet extraction was
performed in accordance with Method 3540 (25).  Each of two 20-g
portions of the sample homogenate was treated with sufficient anhydrous
sodium sulfate to dewater the matrix, placed in glass thimbles,  and
extracted for 24 h with methylene chloride.   The resultant extracts were
diluted to 500 ml.  A 10 ml portion of each extract was then processed
through florisil and GPC cleanups, solvent exchanged to hexane,  and
analyzed by GC/ECD.

Results of this analysis demonstrated total  PCB levels of 222 and 218
ng/g for the duplicates, as Aroclors 1242 and 1254.  This agrees within
10% with results reported in Table 10.  Thus, the lagoon sludge in
question did not impose any significant extraction problems because a
conventional,  routinely applied extraction procedure afforded a recovery
comparable to that of a more stringent technique.
                                   39

-------
The foregoing discussion offers several  analytical  scenarios to account
for the failure of laboratories participating in the Westville site
evaluation to adequately detect PCBs in  stabilized  oil  lagoon sludge.
One or more of these circumstances could explain the questionably low or
null findings for PCBs reported after the material  was  solidified.
Pinpointing the exact cause(s) of these  discrepancies,  however, is
problematical since documentation of sampling and analysis procedures
employed in these site evaluations has not been available.  In fact, it
is possible that either the archived sample available for our analysis
or samples furnished to laboratories who performed  the  original analyses
were not representative of the bulk material.  In spite of these open
questions, it appears likely that the incipient evidence supporting
claims of PCB dechlorination in the field by in-situ lime treatment is
based on erroneous data.
                                   40

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                               CONCLUSIONS

Treatment of PCB-fortified synthetic soil with quicklime in open vessels
resulted in large losses of all three PCB congeners.  The bulk of these
losses, 60 to 80% of starting concentration occurred in the first five
hours of treatment and immediately following lime slaking and sample
heating steps.  Subsequent losses of PCBs were less pronounced; about
10% to 30% of the original spiking levels over the balance of the 72 h
treatment period.  The copious excursion of steam and matrix
particulates during the slaking process, the evaporative losses of PCB
congeners over time evidenced in untreated samples, and the absence of
significant levels of PCB decomposition products all support the
hypothesis that volatilization, rather than decomposition, accounts for
the preponderance of PCB losses observed.  Furthermore, the
concentration versus time-of-treatment curves of the congeners agreed
reasonably well with Thibodeaux's model for PCB volatilization in soil,
when numerical constants, variables and assumptions consistent with
these experiments were used.

Minimal evidence of PCB dechlorination was observed.  Monochlorobi-
phenyl, trichlorobiphenyl, and hydroxy and methoxy-substituted
chlorobiphenyls, were found sporadically and in relatively small
abundance.   The presence of decomposition products did not appear to be
a function of maximum slaking temperature or treatment time.  No
products of phenyl-phenyl bond cleavage were observed.  Most of the
products were consistent with mono-substitution.

An archived field sample from the Westville, IN site analyzed during
this study did not support previous claims of PCB decomposition by in-
situ lime treatment.  The Westville sludge, which was reported to
contain post-remediation, PCB levels less than 1 ppm and which
                                   41

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accordingly provided a catalyst for this and other research into
lime-promoted destruction of PCBs, was found in this study to contain an
aggregate Aroclor 1242 and 1254 level  of 200 ppm.

The destruction of PCBs by application of quicklime to contaminated
soil, sediment or sludge has thus not  been demonstrated,  either by
controlled benchtop experiments or by  retrospective analysis of a sample
from a remediation site where the process was applied.  Evidence of PCB
volatilization suggests that use of reactive quicklime as an in-situ
treatment may even be contraindicated  due to the potential for migration
of PCBs as vapor or airborne particulates.

The presence of small amounts of partially dechlorinated  PCBs after
quicklime treatment may warrant further investigation to  obtain a better
understanding of PCB reactivity.  However, the low product yields
observed upon simple addition of quicklime and water suggest that any
process based on CaO will require other reagents,  catalysts, or more
extreme reaction conditions.  In-situ  treatment processes would be
constrained by PCB volatilization and  the possible formation of toxic
reaction products.

Further work is needed to determine the exact effects of  bulking
processes employed to temporarily stabilize PCB-containing wastes in the
field.  CaO-containing materials are often used to improve the handling
characteristics of such wastes.  We are currently constructing a pilot-
scale apparatus that will allow measurement of vapor and  particulate
phase losses of PCBs under conditions  likely to be encountered in field
applications.  The results of these studies will  determine the direction
of our future quicklime research.
                                   42

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                               REFERENCES
1.    U.S.EPA, Superfund Records of Decision Update.  Office of Solid
      Waste and Emergency Response, Intermittent Bulletin, vol. 6, no.l,
      Publication Number 9200.5-2161, 1990.

2.    Safe, S.,  Polychlorinated Biphenyls (PCBs):  Mutagenicity and
      Carcinogenicity.  Mutation Research, v. 220, pp. 31-47, 1989.

3.    U.S. EPA, Guidance on Remedial Actions for Superfund Sites with
      PCB Contamination.  EPA/540/G-90/007, Office of Emergency and
      Remedial Response, p.  144,1990.

4.    Brunelle, D. J., and Singleton, D. A., Chemical Reaction of
      Polychlorinated Biphenyls on Soils with Poly(Ethylene Glycol)/KOH.
      Chemosphere, 14, 173-181, 1985.

5.    Jordan, 0. D., System and Apparatus for the Continuous Destruction
      and Removal of Polychlorinated Biphenyls from Fluids.  U.S. Patent
      No. 4,4340,401, 1982.

6.    Brown, J. F., and Lynch, M. E., Method for Removing
      Polychlorinated Biphenyls from Transformer Oil.  U.S. Patent No.
      4,377,471, 1983.

7.    Norman, 0. L., and Handler, L. H., Method of Destruction of
      Polychlorinated Biphenyls.  U.S. Patent No. 4,379,746, 1983.

8.    Kitchens, J. F., Jones, W. E., Anspach, G. L., and Schubert, D.
      C., Light-Activated Reduction of Chemicals for Destruction of PCBs
      in Oil and Soil.  In Detoxification of Hazardous Waste, ed. by
      Exner, J. H., Ann Arbor Science, Ann Arbor, Michigan, 1981.

9.    Kalmaz, E. V., Craig,  R. B., and Zimmerman, G. W., Kinetics Model
      and Simulation of Concentration Variations of Species of PCBs
      Involved in Photochemical Transformation.  In Detoxification of
      Hazardous Waste, ed. by Exner, J.  H., Ann Arbor Science, Ann
      Arbor, Michigan, 1981.

10.   Kornel, A., Rogers,  C. J., and Sparks, H. L., Method for the
      Destruction of Halogenated Organic Compounds in a Contaminated
      Medium.  U.S. Patent Application No. 350,425, May 11, 1989.
                                   43

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11.   Payne, J., Boelsing, F., Habekost, A., Hirschfeld, G., and Birke,
      V., Complete Ambient-Temperature Dehalogenation of PCB in
      Comtaminated Soil Using Hydrophobic Lime and Other Reagents, EPRI
      1991 PCB Seminar, October 8-11, 1991, Baltimore, MA (in press).

12.   Boyd, S. A., Mortland, M. M., and Chiou, C. T., Sorption
      Characteristics of Organic Compounds on Hexadecyltrimethyl ammonium
      - Smectite, SoilSci, Soc. Am. J., vol.52, pp. 652-657, 1988.

13.   Boyd, S. A., Lee, J. F., and Mortland, M. M., Attenuating Organic
      Comtaminant Mobility by Soil Modification, Nature, vol. 333, pp.
      345-347, 1988.

14.   U.S. EPA, Technology Evaluation Report:  SITE Program
      Demonstration Test, HAZCON Solidification, Douglassville,
      Pennsylvania, Volume I.  Report No. EPA/540/5-89/001 a, EPA Center
      for Environmental Research Information, Cincinnati, Ohio, 45268,
      1989.

15.   U.S. EPA, Technology Evaluation Report:  SITE Program
      Demonstration Test International Waste Technologies In Site
      Stabilization/Solidification, Hialeah, Florida.  EPA Report No.
      EPA/540/5-89/004a, EPA Center for Environmental Research
      Information, Cincinnati, Ohio, 45268, 1989.

16.   Thyagarajan, B. S., Process for Treatment of Fluids Contaminated
      with Polychlorinated Biphenyls.  U.S. Patent No. 4,612,404, 1986.

17.   Wilwerding, C. M., Degradation of Polychlorinated Biphenyls.  U.S.
      Patent No. 4,931,167,  1990.

18.   Manchak, F., Methods of Transforming Sludge into Ecologically
      Acceptable Solid Material.  U.S. Patent No. 4,079,003, 1978.

19.   Hutzinger, 0., Safe, S., and Zitko, V., The Chemistry of PCBs.
      CRC Press, Cleveland,  Ohio, 269 p., 1974.

20.   Alford-Stevens, A. L., Eichelberger, J. W., and Budde, W. L.,
      "Multilaboratory Study of Automated Determinations of
      Polychlorinated Biphenyls and Chlorinated Pesticides in Water,
      Soil and Sediment By Gas Chromatography/Mass Spectrometry,"
      Analytical Chemistry.  22, 304, 1988.

21.   U.S. EPA, Methods for Organic Chemical Analysis of Municipal and
      Industrial Wastewater.  EPA 600/4-82-057, U.S. Environmental
      Protection Agency, Office of Research and Development,
      Environmental Monitoring and Support Laboratory, Cincinnati, Ohio,
      45268, 1982.
                                   44

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22.   Bellar, T. A., and Lichtenberg, J. J.  Some Factors Affecting the
      Recovery of Polychlorinated Biphenyls (PCBs) from Water and Bottom
      Samples.  In Water Quality Parameters; American Society for
      Testing and Materials:  Philadelphia, PA, 1975;  Special Technical
      Publications 573, pp. 206-219.

23.   Bellar, T. A., Lichtenberg, J. J., and Lonneman, S.  Recovery of
      Organic Compounds From Environmentally Contaminated Bottom
      Materials.  In Contaminants and Sediments; Ann Arbor Science:  Ann
      Arbor, MI, 1980; vol. 2, pp. 57-70.

24.   Weitzman, L., Pluhar, D., and Barth, R., "Solvent Washing of PCB-
      Contaminated Soil," Final Report on Research Pro.iect 1263-15,
      Electric Power Research Institute, April, 1988.

25.   U.S. EPA, SW-846.  Test Methods for Evaluating Solid Waste. Vol.
      IB, Third Edition, U.S. Environmental Protection Agency, Office of
      Solid Water and Emergency Response, November 1986.
                                   45

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            APPENDIX A:  DRAFT FINAL REPORT SUBMITTED TO EPA BY RMC
                FINAL  REPORT  ON  THE  "DISAPPEARING  PCBs"  PROJECT1
                             Dr. R. Soundararajan
                  RMC Environmental &  Analytical Laboratories
                              214 West Main Plaza
                            West Plains,  MO   65775
                                February 4, 1991
        The draft report presented in this appendix has been editted by EPA
staff for clarity.  Technical corrections are presented as footnotes so that
the content of the original draft report is preserved.
                                      46

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INTRODUCTION

       In response to a U.S. EPA Region V report from Mr. Robert J. Bowden,
Chief, Emergency and Enforcement Response Branch, to Mr. Timothy Oppelt,
Director, RREL, the following study was conducted to identify the processes
(chemical and physical) which may be involved in the apparent PCB
concentration changes reported at the General Refining Site and other
similar site locations.

BACKGROUND

      Oily soils at CERLA sites frequently contain PCBs with levels
typically between 200-300 ppm.  In an effort to stop the spreading or
migration of oily contamination and PCBs at those sites, lime and/or fly
ash is often added in an attempt to minimize this spreading or migration.
In several instances, it has been found subsequent to treatment, that PCB
concentration levels in the treated soils have been materially reduced.
The apparent reduction exceeds that explained by simple dilution.  A
possible explanation for these discrepancies could be poor analytical
testing or poor sampling at the site.

      Samples for this study were provided by Region V of Chicago.  All
pertinent information was provided by Region V,  Chicago.  Information
provided includes:  site description, sampling areas, site treatments, if
any, and chain of custody forms, etc.  RMC pursued a course of diligent
sample management and preparation as well as accurate analysis of all
samples.  Further, three known PCB individual isomers were spiked on a
synthetic soil matrix and were subjected to quicklime treatment under
controlled conditions in this lab.  The results  and the conclusions drawn
from them are presented in this final report.

EXPERIMENTAL DESIGN

      The experimental part of this project consisted of two major
sections.   The first section was the extraction  of site samples provided by
U.S. EPA Region V for the identification of any  PCB residues.   Fourier
Transform Infra-Red spectrometry (FTIR) and Differential Scanning

                                     47

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Calorimetry (DSC) were used for the characterization of the extract.
However, the GC/MS and FTIR studies revealed that there were no PCBs
present in the residue.  Extractions were carried out on 100 gram samples
with hexane and acetone and the final volume of the extract was reduced to
1 ml and was analyzed by  GC/MS.  FTIR of the extracts was run as KBr
pellets.

      The second part of the experimental section consisted of preparing a
spiked matrix made up of sand:silicon dioxiderdiatomaceous earth in a 1:1:1
ratio.  Three individual  PCS isomers obtained  from Ultra  Scientific were
dissolved in methanol:methylene chloride solvent and spiked to yield a
concentration of 1333 ppm each.  Fifty grams of this mixture was thoroughly
mixed with pre-calcined commercial quicklime in the ratio  of 1:1 at first.
However, the rate of the reaction, the reproducibility of  results, and the
variation in the intermediate products warranted minor modification.  To
achieve concordant results, numerous experiments were conducted to
reproduce the site conditions.  It must be remembered that tons of high
calcium fly ash (CaO) were added at the site involving millions of
kilocalories of heat.  The heat would be sustained for an  extended period
of time since both soil and quicklime are insulators.  Hence, the mixing
was done during the final six sets of experiments as follows:

      1.    The spiked soil was mixed with quicklime in the ratio of 1:2.
      2.    Water was added slowly with vigorous stirring  until the
            temperature rose to a maximum.
      3.    The reaction vessel was set aside for an hour.  More water was
            then added and the temperature was  maintained  around 80-90
            degrees C for at least three hours  on a hot plate.
      4.    Another set of experiments (Steps 1 and 2) were done inside a
            glove bag.   The effluent gases were purged into a tenax column
            of an LSC II device and desorbed into a Finnigan 5100 GC/MS for
            identification and quantitation of  the effluents.
      5.    Samples were taken at 24, 48, 72, 96, 120, and 720 hours from
            the six sets of reaction vessels, dried in a desiccator over
            P2°5 extracted  with  acetone and/or other  suitable  solvents,
            reduced to 1 ml, and analyzed using a modification of EPA
            Method 680.  The PCB standards were used to create a five point
            calibration curve with auto quan methods using proper
      3,5-Dichlorobiphenyl,
      3,3',5,5'-Tetrachlorobiphenyl,
      2,2',4,4',5,5'-Hexachlorobiphenyl
                                     48

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            quantitation ions.  The analysis was done on a full scan basis.
            Whenever necessary, proper dilutions were carried out.
RESULTS
      Results of six different experiments are given in Tables 1-9; the
graphic representation is shown in Fig. 1.  These six sets of experiments
were conducted at different times.  There were other experiments where some
slight modifications were used such as keeping the reaction temperature
elevated for 48 hours, etc.  These experiments, of course, are not within
the scope of these investigations.  These experiments were used only to
confirm certain kinetic factors in the chemical reactions.  The overall
results may be presented as follows:

      1.    During the exothermic CaO + H20  reaction,  no  PCBs were found to
            volatilize.  No fragments of PCBs (chlorobenzenes) were seen,
            either.
      2.    The biphenyl structure was not preserved at the end of the
            reaction.  The C—C bond between the benzene rings was
            completely destroyed.
      3.    Only one substituted phenol was identified as one of the
            intermediate products.
      4.    Both alkyl- and chlorine-substituted cyclohexanes were found as
            intermediate products.
      5.    Saturation of the benzene ring,  cleavage of the aromatic ring,
            and subsequent oxidation of the terminal carbon atoms are
            strongly indicated.
      6.    Presence of inorganic chloride in the post-treated waste was
            confirmed.  There were no Cl ions in any of the reagents
            (except covalent Cl in PCBs) during this reaction.  This
            confirms the fact that the chlorine in the PCBs was removed.
      7.    The concentrations of all PCBs dropped after 24 hours, but
            after 48 hours the tetrachlorobiphenyl completely disappeared.
            The other two compounds (di and hexa) were also reduced
            substantially.  After 72 hours,  all of them disappeared.  Only
            traces (<5.0 ppm) of the hexachlorobiphenyl were seen.
      8.    In a related experiment (data not included in this report),
            pure CaO did not bring about this reaction.
      9.    When the reaction medium was kept at elevated temperatures
            ("95-100 degrees C) the reaction was much faster.  The entire
            destruction was completed within 36 hours.
                                     49

-------
 DISCUSSION

       Although  the  fact that PCBs are destroyed when treated with fly  ash
 in the presence of  water  is confirmed, we are left with a number of
 perplexing,  unanswered questions that need to be answered.  A methodical
 investigation into  the inner workings of this complex reaction is
 warranted.   The end products and the following postulates can only be
 considered as the "tip of the  iceberg."  In the following segments let us
 consider the possible chemical reactions that could yield the observed
 intermediates and end products.  These considerations are based on well
 established  concepts of both organic and inorganic chemistry.  The most
 conspicuous  reaction is the reaction between calcium oxide and water
 forming calcium hydroxide and  heat :

                          CaO + H2O 	> Ca(OH)2 + A H
                                AH = 235.68 k.cal/mole                    (1)
 This also results  in  several  secondary reactions such as

                    CxHyCl2   + CaO  	> CaC2  + CO2 +  CaCl2  + H2O            (2)

       It is worth  noting that one mole (56 grams of CaO) releases 235.68
 cals of heat.   In  a field  mixing situation, one ton of CaO can liberate
                                  /
 3.82 million kilocalories  of  heat ,  which can help  to sustain the reaction
 for several days.  The Ca(OH)2 formed in this reaction raises the pH to 13.
 Assuming that the AH  (heat of formation of Ca(OH)2) brings about a simple
 thermolysis (split by heat energy) we can see intermediates ranging from
 chlorobenzenes  to  hydrogen chloride, which of course will be neutralized
 immediately after  formation:
        The heat of formation cited for calcium hydroxide is correct for its
formation from constituent elements in standard state,  but not correct for its
formation as shown in the equation.  The heat of formation of calcium
hydroxide from calcium oxide and water is -15.6 kcal/mol.  Data for these
calculations were obtained from:  R. C. Weast, M.  J.  Astle, and W. H. Beyer,
CRC Handbook of Chemistry and Physics, CRC Press,  Boca Raton, Florida, pp.
D50-D93, 1986. —tech. ed.
     4
        Using -15.6 kcal/mol for the heat of formation  leads to evolution of
0.25 million kcal heat per ton of Ca(OH)2 formed from CaO and HpO.  —tech.  ed.

                                      50

-------
                                       A
	>   CXHV  +  C6H5C1
 Thermolysis   rn J.  rri  ,
    CaO        C0 +  C°2  4
                                                                         (3)
             Cl                Cl
      We do have  indirect  evidence  for this reaction.  One of the
 intermediate products  is a phenol.  The presence of the phenol can be
 explained by a  simple  3^2  reaction between the chlorobenzene and the
 Ca(OH)2.
                            Cl
                 'H
                                                                         (4)
                      chlorobenzene
However, the most intriguing aspect of the entire treatment is the presence
of cyclohexane derivatives, which are ring saturation products.  It appears
that after the initial thermolysis and SN2 substitution, the phenolic
compounds seem to undergo reduction.  During the simulated reactions in the
laboratory there was no source of hydrogen to bring about such reductions.
The possibility that water could have been split into H2 and O2 is  quite
slim unless there is a strong catalysis hitherto unknown involved.  It is
imperative to point out that in the commercial quicklime there are numerous
redox systems that could bring about every conceivable organic reaction.
An examination of the E values of these redox systems (in commercial
quicklime) confirms this view.  Hence, the formation of cyclohexane
derivatives may be visualized as follows:
                            Mn+l/Mn
                                                           + HC1
                                                                         (5)
Addition of certain additives such as slag powder would enhance this type
of chemical reaction.

      Yet another chemical factor to be considered here is steric
hindrance.  In heavily chlorinated PCBs, the bulk of chlorines would
prevent the approach of OH for substitution.  It appears that partial
breaking of C—Cl bonds is involved during the exothermic step (1) which
leaves the aromatic ring with only a few chlorines.
                                     51

-------
      One of the most significant end products is the ester of hexane dioic
acid.  The formation of this product very strongly suggests that following
the ring saturation there is ring cleavage and subsequent oxidation of the
terminal carbons to carboxylic acid functional groups.   It is also
interesting to note that no other dicarboxylic acid derivative was found.
The six member carbon chain is another indication that its precursor was a
six membered ring.  This oxidation phenomenon can be attributed to both
quicklime and dissolved oxygen in the water that is added during this
treatment process.

      It has been established that the organic chlorine in the PCBs has
become inorganic CaClj.   The Cl was measured with the aid of  ion selective
electrodes.  The original reaction medium (CaO,  sand, etc.) did not have
any chloride in it before the reaction began.  This evidence again supports
the idea that the chlorines were either removed by thermolysis or by a
simple nucleophilic substitution process.  It has also been established
that the reaction rates of this process are directly proportional to the
reaction temperature.  At elevated temperatures, the disappearance of PCBs
was faster.  During the investigations, we have found that the reaction
rates are directly proportional to the concentration of quicklime.  This
observation is in agreement with the law of mass action.   The site samples
were subjected to massive extraction procedures, but none of them had even
traces of PCBs.  This is not due to any stabilization,  encapsulation, or
masking, but due to the fact that the PCBs have been destroyed completely.

      Further, the total GC/MS analysis of the site samples showed
considerable amounts of long chain saturated hydrocarbons.  These compounds
during excessive heat release could have saturated the benzene rings in the
PCBs as the whole process resembles a closed system.  The entire phenomenon
can be speculated on, in light of experimental data, as follows:
                                     52

-------
                FLYASH-PCB REACTIONS   SCENARIO I
                           REACTION  1
              CaO + H20
     Ca(OH)2 + 235.68 kcal/mol
          thermolysis
          hydrolysis
            OH
          OH
substituted phenol
                                  (i.e., 235.68 kcal  per 56 grams;
                                   therefore, 3.82 million kcal  per
                                   ton of CaO)
                           REACTION  2
thermo-
 lysis

 A

 IHJ
    thermolysis, reduction,
   \hydrolysis
OH  \ A
                                                            +  HC1
                                                      CH3 4-methyl-
                                                           cyclohexanol
    thermolysis, reduction, ring
    cleavage, oxidation of
    terminal  carbons
           ROOC —(CH2)4~COOR
         hexane dioic acid ester
                                53

-------
       FLYASH-PCB  REACTIONS    SCENARIO II
                         HC1
                         A
CaCO,
           CaCl-
CaC,
                                              C02 + CO
       FLYASH-PCB  REACTIONS    SCENARIO III

                         AH
               CnH2n+2
    2 [H]
           [H]
        Cl
                        [H]
                        OH-
                                        OH
                         54

-------
CONCLUSIONS

      1.    The interaction between high calcium fly ash (CaO) and
            polychlorinated biphenyls  (PCBs) results in the total
            destruction of PCBs.
      2.    The reaction mechanism is  still unclear.  This would warrant
            thorough investigation where the reaction would be frozen at
            different time intervals and the intermediates would be
            analyzed and identified, possibly by GC/MS/MS.
      3.    The phenomenon of catalysis is very strongly indicated, but
            which catalyst brings about this destruction is yet to be
            determined.
      4.    The stoichiometry as well  as the upper organic threshold are
            yet to be determined to avoid fire/explosion and volatiles
            release into the atmosphere during site remediation.
      5.    The prospects for the application of this process for the
            destruction of other organic wastes appears to be bright, but
            systematic and thorough investigations are needed.

      In essence,  our investigations with limited scope, resources, and
time, indicate that this process needs to be evaluated properly since its
effectiveness and cost efficiency are phenomenal before full scale use in
the field.

REFERENCES
1.    Cotton, F.  Albert and Wilkinson, Geoffrey,  Advanced Inorganic
      Chemistry, 4th Edition, John Wiley & Sons, 1980.
2.    Morrison, R.T.  and Boyd,  R.N.,  Organic Chemistry. 2nd Edition, Allyn
      and Bacon, Inc. , Boston,  1958.
3.    Gibbons, J.J.  and Soundararajan, R.  , "The Nature of Chemical
      Bonding between Organic Wastes and Organophilic Binders, part 2",
      American Laboratory 21, (7)  70-79, 1989.
                                     55

-------
                                   TABLE 1
                    DICHLOROBIPHENYL CONCENTRATION  (ppm)
Zero Hours - (Baseline)
Sample #
Run 1
Run 2
Run 3
Average
1
1335
1329
1375
1346
2
1300
1346
1292
1313
3
1285
1340
1301
1309
4
1400
1395
1362
1386
5
1320
1304
1278
1301
6
1362
1286
1390
1346
Statistical Calculations:  mean   1333
                           standard deviation 32.08
                           relative standard deviation  2.41%
                                   TABLE 2
                    DICHLOROBIPHENYL CONCENTRATION (ppm)

Sample #
Run 1
Run 2
Run 3
Average

1
734
780
747
754

2
700
762
774
745
24 hours
3
689
645
670
668

4
710
690
704
701

5
781
761
772
771

6
660
620
678
653
Statistical Calculations:  mean  1333
                           standard deviation 32.08
                           relative standard deviation 2.41%
                                   TABLE  3
                    DICHLOROBIPHENYL CONCENTRATRION (PPItO

Sample #
Run 1
Run 2
Run 3
Average

1
138
140
140
139

2
135
140
132
125
48 hours
3
121
125
130
125

4
135
140
142
139

5
155
161
189
165

6
121
134
137
131
Statistical Calculations:  mean  1333
                           standard deviation 32.08
                           relative standard deviation 2.41%
                                     56

-------
                                   TABLE 4
                   TETRACHLOROBIPHENYL CONCENTRATION (ppnO

Sample #
Run 1
Run 2
Run 3
Average
Statistical



1
1216
1230
1290
1242
Calculations:


0 hours (baseline)
234
1210 1179 1221
1193 1201 1243
1225 1192 1300
1209 1191 1255
mean 1333
standard deviation 32.08
relative standard deviation 2.

5
1315
1302
1317
1311

41%
TABLE 5
TETRACHLOROBIPHENYL CONCENTRATION fppm)

Sample #
Run 1
Run 2
Run 3
Average
Statistical



1
837
880
855
857
Calculations :


24 hours
234
828 775 835
868 787 868
867 776 876
854 779 860
mean 1333
standard deviation 32.08
relative standard deviation 2.

5
925
936
920
927

41%
TABLE 6
TETRACHLOROBIPHENYL CONCENTRATION (ppm)

Sample #
Run 1
Run 2
Run 3

1
11.2
10.9
11.7
48 hours
234
10.1 9.3 11.1
11.4 10.1 10.6
9.8 8.9 11.4

5
12.3
11.8
12.0
                                                                         6
                                                                       1208
                                                                       1197
                                                                       1182
                                                                       1196
                                                                         6
                                                                        793
                                                                        810
                                                                        800
                                                                        801
                                                                         6
                                                                       9.6
                                                                       8.8
                                                                       9.5
Statistical Calculations:
mean  1333
standard deviation 32.08
relative standard deviation 2.41%
                                     57

-------
                                   TABLE  7
                   HEXACHLOROBIPHENYL CONCENTRATION (ppml
 Sample #1           2           3          4          5           6

 Run 1         1315       1310       1301       1316        1382       1300

 Run 2         1345       1352       1329       1329        1391       1298

 Run 3         1325       1328       1313       1350        1385       1302

 Average       1328       1330       1314       1332        1386       1300
Statistical Calculations:  mean  1333
                           standard deviation 32.08
                           relative standard deviation 2.41%

                                   TABLE 8
                   HEXACHLOROBIPHENYL CONCENTRATION (ppm)
                                 24 hours
Sample #
Run 1
Run 2
Run 3
Average
1
612
632
596
613
2
614
645
582
614
3
547
535
529
537
4
630
608
602
613
5
691
701
689
694
6
552
525
601
559
Statistical Calculations:  mean  1333
                           standard deviation 32.08
                           relative standard deviation 2.41%

                                   TABLE  9
                   HEXACHLOROBIPHENYL CONCENTRATION (ppm)
                                 48 hours
Sample #
Run 1
Run 2
Run 3
Average
1
334
341
327
334
2
327
357
302
329
3
302
307
300
303
4
329
333
341
334
5
408
393
389
397
6
321
317
302
313
Statistical Calculations:  mean  1333
                           standard deviation 32.08
                           relative standard deviation 2.41%
                                     58

-------
         1400
             CONGENER REMAINING, mg/kg
                          200
  400
TIME, h
   600
800
                             DCBP
  TCBP
HCBP
Figure 1.   Average loss  of PCB congeners  over time.
                                   59

-------
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              APPENDIX B - SELECTED  CHROMATOGRAMS, MASS  SPECTRA
                         AND COMPOUND  IDENTIFICATION

MATERIALS

      Stock solutions  and blank extracts were analyzed by GC/MS to identify
contaminants that could  affect experimental results.  Figures B-l through
B-3 show chromatograms of the individual PCB congener solutions prior to
mixing.  Figure B-4 is a chromatogram of the three internal standards used
for calculating relative retention times and response factors.  In each
case, the flat baseline  indicates the absence of contaminants that could
interfere with PCB and reaction product analyses.  The chromatogram of the
actual spiking solution  fortified with internal standards is shown in
Figure B-5.  Mass spectra obtained in this study are compared to reference
spectra for the three PCB congeners in Figures B-6 through B-8.

      Blank samples of synthetic soil were processed through lime
treatment, extraction and analysis to check for contaminants in solvents
and glassware used in the procedures.  These blanks were treated exactly
the same as experimental samples except that the spiking solution did not
contain the PCB congeners.  Six chromatographic peaks were detected (Fig.
B-9) at low concentrations  (compare ion counts in Fig. B-9 with Fig.  B-5).
The four peaks that could be matched to reference spectra were identified
as common laboratory contaminants (Figs. B-10 through B-15).

TENTATIVE PRODUCT IDENTIFICATION

      Aliquot samples of extracts produced in the open-vessel experiments
were sent to Battelle Columbus for identification of potential
decomposition products.  The values shown in Table 8 of the main body of
this report are from analyses performed by Battelle.   Selected data are
presented here to support the identification and semi-quantitation of
products.
                                     67

-------
Stock Solution and Solvent

      Chromatograms of methylene chloride solvent and the stock PCB
solution used to spike the synthetic soil are shown in Figures B-16 and B-
17, respectively.  The flat baseline of the solvent chromatogram indicates
that the compounds tentatively identified as reaction products are not
solvent contaminants.  The stock solution, at 50-fold dilution, shows one
peak in addition to the spiked congeners and internal standard at a
retention time of 32.56 minutes.  Mass spectra and peak identifications are
shown in Figs. B-18 through B-22.  The unknown compound was not
sufficiently resolved or concentrated for identification.

Open-Vessel Reaction, 72 hour sample-replicate 2

      The 72-hour, replicate-2 sample was selected to show compound
identifications since this sample contained all the products observed in
the open vessel reactions.  Figures B-23 through B-43 illustrate the
chromatogram, peak mass spectra, and tentative compound identifications for
the 72-hour sample.  Peaks numbered 2, 8, and 14 on the chromatogram (Fig
B-23) are the spiked PCB congeners, identified by relative retention time
and mass spectrum compared to pure PCB standards.  Peak 20 (Fig. B-23) is
the internal standard, chrysene-d^* used  to compute relative retention time
and to semi-quantify unknown peaks.  Unless otherwise indicated,
identification of unknown compounds was based on searches of the NIST data
base and manual interpretation.  The probability of each of several product
identifications being correct is shown under each mass spectrum, except for
peak 18 which yielded no interpretable spectrum.

      High-probability identifications were made for peaks 1,  3, 5, 6, 9
and 12 (Figs. B-24, B-26, B-28, B-29,  B-32 and B-35)  as mono- through
pentachloro biphenyls.  Isomer identifications could not be made from mass
spectral data.  Further identification would require GC/MS analysis of pure
samples of all the candidate congeners.  Peak 19 yielded a strong MS match
for a methoxypentachlorobiphenyl.

      Moderate-probability matches were found for peaks 4, 7,  10, 11 and 17
(Figs. B-27, B-30, B-33, B-34 and B-40) yielding tentative identifications
of hydroxymonobiphenyl, tetrachlorobiphenyl (not the starting TCBP
congener), pentachlorobiphenyl, methoxytrichlorobiphenyl, and
tetrachlorodibenzofuran, respectively.  The remaining peaks did not yield
good matches with library spectra; tentative identifications were
determined by manual interpretation.  Peak 15, eluting at a relative

                                     68

-------
retention time of 0.9495, may be a contaminant since the diluted stock
solution yielded an unidentified peak at a relative retention time of
0.9498 (Fig. B-17).

      The tetrachlorodibenzofuran (TCDF) compound warranted further
examination because of possible toxicity of TCDFs.  A sample of 2,3,7,8-
TCDF available at Battelle was used to spike a d!2-chrysene-fortified PCB
calibration standard; the spiked sample was then analyzed by GC/MS.
2,3,7,8-TCDF eluted at a relative retention time of 0.9578 and exhibited a
response factor of 0.359 relative to d!2-chrysene.  Product compounds in
open-vessel extracts that were tentatively identified as TCDFs eluted at
relative retention times of 0.9570 to 0.9573 (see peak 17, Fig. B-23 for
example).  The relative retention time along with spectral matching support
the identification of TCDF.  Isomer identification is less certain, since
other TCDFs may have nearly identical retention times.   The total ion
current response factor measured for 2,3,7,8-TCDF was used to estimate TCDF
concentrations in all open-vessel extracts shown in Table 8.  Figure B-43
shows the chromatogram of the 72-h,  untreated control sample, indicating no
contamination that could be interpretted here as reaction products.
                                     69

-------
Fi le >BIPCB
4998889-
3699889-
329889CV-
2888898-
2498888-
2898889-
1688889-
1299880-
389990-
499998-
48.8-458.9 amu. 3>s DICHLOROBIPHEHYL





















-108
-?8
k*e
-70
-r.O
-50
-40
-38
^0
-10
4 6 8 19 12 14 16 18 28 22 24 26 28 39 32
Figure B-l.
Total ion chromatogram of 3,5-dichlorobiphenyl stock
solution.
File >TEPCB
1R88988-
1698999-
1499098-
1290999-
1808088-
889889-
689889-
488880-
280800-
nJ









4 '5 ' 8 ' 18 ' 12 ' 14 ' 16 ' 18 ' 28








22 24 26 28 38 3<
-188
-90
-SO
-7ft
-..9
-10
CO
-in
ki
Figure B-2,
Total ion chromatogram of 3,3',5,5'-tetrachlorobiphenyl
stock solution.
                                     70

-------
File >HXPCB
2209099-
2000000-
1899099-
1690998-
1499999-
1208809-
1999999-
-
888899-
608099-
499800-
299089-

IIC












p ' i ' T • r • i • i • i • i • r~-r- 7- • i • i • i • i 	 -|-' i • i • i •
4 6 8 10 12 14 16 18 29 22 24













1 	 • I • i
26 28 30 3^

-190
-*0
-89
.,„



-1H

-30
-2"
•18

Figure B-3.
Total ion chromatogram of 2,2',4,4',5,5'-
hexachlorobiphenyl stock solution.
Fil- >5UPLC
798000-
6S000B-
600098-
580080-
450980-
400009-
359880-
309909-
259880-
280000-
159009-
100000-
58809-
0-
49.8-4S0.0 »mu. SUPELCO STD



A







L. 	













c















4 f, 8 10 12 14 16 18 20 22 24 26 28 30 t-

-100
r?0

';7Q

^.0
!^«
^«

-Jro
-20
-19
^)
Figure B-4.
Total ion chromatogram of internal standard spiking
solution containing:  acenaphthene-d^g (A),  phenanthrene-
d10  (B),  and  chrysene-d12 (C).
                                     71

-------
File '.5TDOI 48.9-4S9.9 a*u . BI ,TETRR ,HEXfl- CHLOROB1PHEMYL
TIC P
2400000-
220000O-
20»0990-
1800000-
1600800-
1499909-
1 200000-
1009009-
399009-
699000-
400000-
290000-
0-




A


D
E


















F


l — •— i — •— r~ — r— • — r-* — r^ — r-1— i — •— l — ^T — "~~\ — ^~r^ — r^ — r~ — r— — T—^T — ^T — ^T — ^T — r~r^ — r-* — r-1 — i
4 6 8 10 12 14 16 18 20 23 24 26








' • i • i • i • i • i
23 30 S.
-100
^r,
-7'.'
,..
H

-10
•0
Figure B-5.
Total ion chromatogram of primary dilution standard with
internal standards:  acenaphthene-d1Q  (A),  3,5-
dichlorobiphenyl (B), phenanthrene-d1Q  (C),  3,3',5,5'-
tetrachlorobiphenyl (D), 2,2',4,4',5,5'-
hexachlorobiphenyl (E), and chrysene-d^
Fil» >STD88
Bpk flb 9999
18888-

8808-
6888-
488B-

2999-
9=





75

88






















^ "

File >BIGDB
Spk Ob 9999
10009-
8999-
6009-
4009-
2009-
0-


88

80












STD STB 88 US/ML Scan 682
128 168 288JL,0, 2<18 288 32a 36e 488 M'24 "ln'
-^
152




126
/
•-, ....J. ,r 	



186
	 | 	





2E5 231 329
, \ v 307 S 3S' 38S *z*
r^~. .. ^ . ? s f r . i
129 168 288 249 288 328 368 488
-198

-89
-69
-48

-29
-9
3,S-D1CHLOROBIPHEMYU Scan S2963
FIT 9.98 min
120 160 298 240 289 329 369 499
--
152
84 {
75
~~^






/





80
111
,S 186
f '

1 1, .



226


•188
-88
<0
-48
-28

128 ' 168 ' 288 ' 249 ' 288 ' 328 ' 368 ' 480 '
Figure B-6.
Mass spectrum of 3,5-dichlorobiphenyl compared to NIST
library reference spectrum.
                                     72

-------
Fil* >STD88
Bpk Ob 9999
18089-
8809-
6009-
4808-
2980-
8-
Fil* >BIGDB
Bpk Rb 9999
8899-
6909-
4899-
2099-
9-
STD
88 128 168 298


2
74 "9 icn
\ 92 X" ' '84
k ' 1 1 '
..i.r *_,.!...«. ij..,.lL 	 « 	 i.l....... • 	 Hi... 	 .
80 129 168 289
STD 80 UC/ML Scan 932
20.13 din.
290 C~
H
?•
L. x. 1. . 7 r 3r T
240 280 320 360 400 448
1 , 1 ' -Blph«nyl , tetrachloro- Scan
FLT 8.0(
80 120 168 289 248 280 320 368 400 446
	 i ... i 	 i ... i 	 oaf.\ 	
298 1
1
lie
92 S ise
/ r /
i L t /
I'M 1 i,
80 120 160 208
" 1— ^

248 280 328 368 408 448
-108
-80
•69
-(0
-20
-9
6327S
) nin.
-tee
-80
-68
-28
-9
Figure B-7.
Mass spectrum of 3,3 ', 5, 5 ' -tetrachlorobiphenyl compared
to closest matching spectrum in NIST library.   Isomeric
structure of reference spectrum not identified in
library.
File >STD88
Bpk flb 9999
18900-
8808-
6889-
4898-
2989-
0-

File >BIGDB
Bpk Pb 9999
10098-
8808-
6900-
4080-
0-

STB STD 88 UC/ML
88 129 160 288 240 288 320 3^

298
(
\\
.,..\,..Ij^, i 	 22.....i..A..!\l. i.
80 128 160 208 240 288 328 3<
1 ,1 --Biph*nyl , 2. 2', 4, 4', S. 5' -hexachloro-
FLT




298
/" / 3/5
88 ' 120 ' 160 ' 208 ' 249 ' 289 ' 329 ' 3<
Scar
23.7;
&.,,,.•!?!, ,,.,,
1



L T /2 .
9 489
Sc an
9.9t
'A , 4?B




366
>9 408
1133
min.
-199
•89
-60
-«9
-29
•8

69792
) nin.
-100
-89
-r,*
-40
-29

Figure B-8.
Mass spectrum of 2,2',4,4',5,5'-hexachlorobiphenyl
compared to NIST library reference spectrum.
                                     73

-------
Fil* > 1BLPN

LI
1990O-
.699*
14999-

12909-
19990-
a«90
"~
2000-

4S.0-4Se.0 ««u. SXIRftCT







A
\
Vs 	 	 	 ^

4 A 8 10
tl! 	 3THOT5T



B

C
1


1
' IftMhuA. t/n-> JMAfcJW^-j
^n*Wf\*'yWri**lMM"^Tv
12 14 1
PC8.S

D





E

.A^r*^ M^

> ie










Hi^^*awLM>'wWi'aw«^wVk'''*lv
^r Tiji/ifurMyvpifyv* ^ ™iTf B^P ! ^
29 22 24 26
F









^

^31

-too

-90
-«.o

-^'.'

-.0
'!"
-2..


                         A  - a,a-dimethyl benzyl alcohol
                         B  - no suitable match
                         C  - 2,6-bis(l,l-dimethylethyl)-4-methyl-phenol(BHT)
                         D  - l-(l-cyclohexen-l-yl)-4-methoxybenzene
                         E  - dibutylphthalate
                         F  - no suitable match

2«»99-
;;,,.,
„,,„>
l-.9>:'i>
12000-
l-.OOfVH


,0-v
29i]>0-

45.9-459.8 ...j. CXtRaCT
IIC


E



A
'
VL_,

4 * a 19
•t, UIMOUt


i



C

1
' WwV*«illrVlkt«Wl'
12 14 I
PCB.S f.
D




E



VllWfrW
> 18
tP 2 	









^i^Ws*yVwVfflWMOfl*rm T
29 ' 22 ' Z-t ' 26

F







^

2f


-?0
.9
-70
"

-10


-10

Figure  B-9.
Total  ion chromatogram of quicklime-treated soil  blank
duplicates.  Treated blanks  consisted  of synthetic soil
spiked with solvent only and processed through  quicklime
treatment,  heating steps and extraction.
                                         74

-------
Fi le > tPLBH
Bpk Ob 999?

10000-
8000-
6000-
4000-
2000-

77
"\
[
llllll. ll





JOS
1.1 :
ee
Fi 1» >BIGBB
Bpk flb 3741
4P00-
3000-
2000-
1000-
0-


77
.,




h
80
EXTRflCTED WIHOUT PCB.S tear, S4
4.46 IT. 1 n .
121 r









1S2 178 , s \ 308 33S "x 387 ,'
129 16B Zee 240 280 320 360 400
-100
-8'S
-60
-40
-28
-1BLOII EXTRRCTEB MIHOUT PCB.S Scan 402
Bpk- Pb ?99? 10.6> mil,.

1000O-
3009-
6000-
4000-
2000-
8-
164



S0 1




6f /'' 132 I 192 28s 23, 283 ^ 33 412
Jl. ,lL,Jlll 1 , , , \.,.lll!ll . \ ^ .-^ N . V f ! ! . f'''
80 ' ,20 ' 160 ' 200 ' 240 ' 280 ' 320 ' 360 ' 400

-1 no
-SO
-60
-40
-20
-0
File >BICDB Phenol, 2 ,5-dichloro- Scan 40071
Bpk Pb 9999 FLT 0.00 n, i n .
19009-
8000-
6?00-
200O-
0-
--


*? *> ,33
. 1 , i, \



,66
\
80 12B 166 299 240 289 329 360 400
-1 00
-80
-60
-10
Figure B-ll.
Best NIST library spectral match for Peak B (Fig. B-9)
Identification questionable,  with probability = 0.31.
                                     75

-------
Fi 1* > 1BLB1I
Bpk Bb 9999

10008-
8888-
6000-
4000J
2000-
0-



EXTRBCTED HIHOUT PCB.S Scan 419
10.93 Kin.
285 r



S7
•' 91 .., US 177
\ ' f f
,.il.i .1.1 .L j .in riv.ii.L, . , .1 i.
88 128



i 256 37-*
243 / 296 322 347 , 413
.1 ,' r . f , ' ' . .' !
168 280 248 288 328 368 400
-100
Uo
•48
-10
File >BIGFB Phenol, 2 ,6-bi 5< I , 1 -dime thylethyl ) -4-inethyl - tear. 4?7'i7
Bpk fib 9999 FLT 8.00 »tir,.

10000-
8000-
6000-
4000-
2000-



105 i
\ 119
1 1 '1 '<
88 128
285 r



*S 177



\™
168 280 248 288 320 368 400
-1 80
-80
•*«
-*
Figure B-12.
NIST library matching spectrum for Peak C (Fig. B-9).
Excellent match,  with probability = 0.96.  Compound is
commonly known as BHT (butylated hydroxytoluene),  a
common antioxidant.
Fil- >IBLfiH EXTRBCTED MIHOUT PCB.S Scan ril
Bpk Pb 9999 16.11 n.i n .

18800-
800O-
6000-
4000-
2000-
0-
• 188




8\ 94 '.60
i ' 139 1 1
i. .J ,il..al 	 	 . '. . . ill J




207 259 286 41*
s N. X 312 338 389
30 ' 129 ' 168 ' 288 ' 248 ' 288 ' 320 ' 360 ' 488 ' 44

-180
-90
-60
-10
-*<
8
Fiie >BIGDB Benzene, 1 - ( I -eye 1 ohexen- 1 -y 1) -4-m* thoxy- S<- 3n 46070
Bpl- Ob 9999 FLT 0.00 mir. .
10000-
388O-
6000-
4080-
2000-
0-
1

160
129
1
111 1 J ,.
88
f


189
80 128 168 288 248 288 328 360 400 44
100
-80
*:o
•40
-iO
-0
?
Figure B-13.
Best NIST library spectral match for Peak D (Fig. B-9)
Match somewhat uncertain, with probability = 0.52
                                     76

-------
File >1BLRN
Epk Ob 999?

10990-
8809-
6890-
4990-
2090-
8-

Fi le >E1GBB
Bpk flb 99?'?

18088-
8800-
608O-
4909-
2080-

9-



1




76 194
\ \ 121
I..I b I. .1 ft . .1
80 128
1 .2-
1




76 104
X N
.1, ..),,.. ,»., , , ,,,,
T f T '—'-r--f-*-* • ^^
80 120
EXTROCTED W1HOUT PC8.S ?c
13. S
49




,,, 287 326 37P
183 "J 248 x 388 / < 391 43ft
(..{.,{.? .*.:' / . "\ '. .
168 ' 200 ' 248 ' 239 328 ' 360 ' 408 ' 44'
Benzenedic arboxy 1 i c ac i d , dibutyl ester Scan
FUT 9.8'
49





223
, ,'
• i • • • i - i • - i • - - i - - • i • • • i • • • t - - - i • - - i • • ' 1 ' ' ' I ' ' ' I ' ' ' I • • • i
160 200 240 280 320 368 400 44r
in SC.S
1 nil..

-100
-90
-60
-10
-^

J
36477
1 mm.

-100
-fty
60
-40
T,



Figure B-14.
Best NIST library spectral match for Peak E (Fig. B-9)
F 1 1- 1 PLUM
Ppk Ob 99??

10000-
8000-
6999-
2990-
9-








186 129
... / 	 	 i. .01. .. .
89 128
Fil* >B1GDB 2-Propen-
Bpk Ob 9999

iceetv
398O-
6990-
4900-
2990-
0-



107
1




128
/'

88 128
EXTRPCIED WIHOUT PCB.S t- ,: an 1 I _">
248



297 .
1S6 194 /'
{.. 	 .' .U . Jl
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447
281 317 343 369 3 ?S
'..'./' f
169 ' 288 ' 248 ' 288 ' 328 ' 369 ' 499 440
-inn
-99
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1 -on« , 1 - (2-hydroxyph*ny 1 ) -3- ( 4-hydroxyph»ny It - Sc »n SS919
FLT n.OO «ln.
248



147
S 178 !
( I <( '• • i



242
;— - "
160 288 248 288 328 368 490 449
•100
-en
-60
-JO
-jft
-o
Figure B-15.
Best NIST library spectral match for Peak F (Fig. B-10)
Questionable match, with probability = 0.42.
                                     77

-------
        TOTflL ION CHROMfiTOGROM
         Fil«  >B7010   45.0-450.0  Amu. BLBNK MECL2
                                     TIC
                          400        800        1300
         400000-


         360000:


         320000-


         280000


         £40000^


         £00000-


         l6000'>


         1£OOOO


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          4000O
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Figure B-16.
                                      OMOLYST LHK D12-CHR

                                        1600        2000

                         •  1 '  1
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                 1  •  1 •
                    £0
                                           I  ' 1  ' 1
24
      £6
 1 '
3£
 1 •  1
36
                                                    40
Total ion  chromatogram of solvent  spiked with chrysene-d12

as internal  standard.
                                       78

-------
                        4*. 0-450 .0 ami*, DI 1,^'TEDS-TOCK 1 :50
                                      (tOC  TIC
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                                      T  LMK Dli-CHRYSEr

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               |i -e7'<':'  4? .0-4^.0.0  SMU, DiLUIED ETOOI'- 1:50  flNHLviT LHK Dlc-C'HRY; £N
                                      ^Di: TIC

Figure  B-17.
                 iO . v   31 .0  3£ . 0   ij: .C  i*t .C   35.0  3t". .0  37 . 0  36 .0  3* .0  40 , u
Total  ion  chromatogram  of  PCB  solution used to spike

open-vessel samples spiked with internal  standard.
                                              79

-------
        File >B7330 DILUTED STOCK  1:50   RNfiLYST LHK D12-CHRYSENE  $  £0  Scan 11331
Epk fib 9999.


-j
IS
40
Bpl< Pb 9999.

,
-i
J
•„' f ' 	 r-
40
File >B!6DB
Bpk Hb 9999.

SUE'.

1

63 '"'5 93 in l£6 135
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•' "'- , - "-• '• -•" 	 -- 1 	 7" r. r.l I ll'
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25.06 triin.
£££
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160 £00
1,1 ' - B i p h * n y ! , £ , 6 - d i c h 1 o r o - S c an 3 0 £ 0 6
0 .p.0_ min .

1

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1 ,1 '-Bipheny 1 , 4 , 4 ' -dichloro- Scan 80196


0.00 rn i n .
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1
63 ?5 93 HI ^ 136
16£ 136 Pn7
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1 r r-i
160 £00

ichloro- Scan 80198
0 . 00 mi n .
£'££
52 r"" i-
16 £ 186

                  ~^—[—r"1-)—i' T ;—r i "i "Y
Figure B-18.
Mass spectrum of first peak  in  spiking sample
chromatogram  (Fig. B-17).  Matches ranged in probability
from 0.88-0.96; library  did  not contain the DCBP congener
used in this study.
                                      80

-------
File >B7330 DILUTED STOCK 1:50
Bpk fib 9999.

j 50 74 92 110 12?
40 SO 120
1
le >BIGDB 1 ,l'-BiDhenvl
Bpk fib 9999.

T
j 74 92 11° 128
40 80 ISO
File >BI6DB 1 ,1 '-Bipheny 1 ,
Bpk fib 9999.

-j
50 ?4 92 110 123
ni { -X ,'.,,.' ,<,
u i i ' • • i ' • • i • • i • • • i
40 SO 120
File >BI6DB 1 ,1 '-Biphenvl ,
Bpk fib 9999.

1
40 3 w 12 0

flNfiLYST LHK D12-CHRYSENE 9
SUB

220
150 170 ^j34 ^ 2£5' 254
160 200 £40

, 2 ,3 ,4 ' , 6-tetrachloro-

220
150 M
160 £00 £40
2,2' ,6,6 '-tetrachloro-


220
150 ±70 ^184 ^ 225 255
it,|.i.|rjS|...[i..|..l^,
160 200 £40
£,£ ' ,3, 3 '-tetrachlc.ro-


159 1S9 £20 257
i * i i i i i i i i i i i i i \ i i j i i 1 j i
160 £00 £40

20 Scan 1393
29.67 rnin.
292

I, L
2SO

Scan 100720
0 .00 min .
£92
.--' ,_
1

280
Scan 100684
0 .00 min .
292
,--' ,
£S3
L_L

£30
Scan 100705
0.00 min.
292

")_
1 • | 1 1 1 | 1 -U
£SO

Figure B-19.
Mass spectrum of second peak in spiking sample
chromatogram (Fig. B-17).  Matches ranged in probability
from 0.59-0.79; library did not contain the TCBP congener
used in this study.
                                     81

-------
File
Bpk





\_
U
Bpk



File
Bpk



File
Bpk




>B7330
fib 9999
DILUTED STOCK 1
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fiNflLYST
LHK D12-CHRYSENE II 20 Scan
SUB
32
.42
1548
min
m
360
-\
1 «
J n>
40

>BI3DB
fib 9999

74 109127
7 / 	 (._„'_. r
80 120

3,4,5,3'

145

160

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132

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£18
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200


22£ £55
V"~~ _/
240

£90

|^ ^
280 320

5'-Hexachlorobip'henvl

3*7
~~


111
360


l_
C
I n


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0.00
min





9
,
360
H
n ' i

40
>BIGDB
fib 9999
1 . ^ --
•j ./. .». ,. .1 4 - r - C- ^
r ' 1 ' i T I ' l
80 120
145
s*

160
l.l'-Biphenyl, 2
.

130
/
T" '

218

£00
,£',4,4'


£22 254

£40
£90

280 3£0
,6,6'-hexachloro-


388

1

I


360
Scan 115160
0
.00
mm
,
360
b
40
>BI6DB
fib 9999
^>3 109 ]_27
T / ..... 4 riy: i'
r * i • i 'i 'i
80 130
0 0 S -3
"- , •- , " >
145
**•
160
4,4 '
130
/
't ' '
218
200
222 £53
£40
290
if 325
|L ^,-
i * i • i
£80 320
,5-Hexachlorobiphenyl
327
-^
i
I

1 ' 1 ""
360
Scan 115163
0 .00 min .
360
j
U 'l i
40

1 l I ' 1 l 1 ' I
80 120

r i
160





200

i • \ ' i '
£40

i ' i ' i
£30 3£0

i '
I
V '
I



360
Figure B-20.
Mass spectrum of third peak in spiking sample
chromatogram (Fig.  B-17).   Matches ranged in probability
from 0.91-0.94; library did not contain the HCBP congener
used in this study.
                                     82

-------
File
Bpk

-.
le
Bpk


File
Bpk

>B7330 DILUTED STOCK 1:50 RNRLYST
fib 9999.
1 «L 7 108 1
n 1 ,1 1 1 ^~~" 1
- V 1 " ' ' f""' 1 ' 1 '' 1 '
80 120
SUB flDD NRM
/5° 168 ^i 227

160 200 240
LHK D12-CHRYSENE BIGDB fi-CONIDEHDRIN DIMETHYLETHER
Qb 9999.
] 55 91 128 1
01..i<.TT./__. 	 /..r.

30 120
51 139225 233
i n^ T i r •" i
160 300 340
269
I 299 3£5
1 * T 'H ' 1 ' \
280 320
>BIGDB B-CONIDEMDRIM DIMETHYL ETHER
fib 9999.
_i

| 55 91 115 151 189225 238

File
Bpk
v ' i • i ' i • i • i
30 120
>BIGDB
fib 9999.
1 ' 1 • 1 • I ' t
160 200 240
269
1 299 325
••i \ i "i "i i i • i \
230 320

T
1 i ' i
360
32.56 min.
382
406C

400
Scan 117916
0.00 min.
384
353
' 1 ' 1
360
337 E

400
Scan 117915
0.00 min.
334

353
• i • i
360
Excel sinine



' i_
387 [
1 	 ~ rn
400
Scan 117342
0.00 min.
384


j 153 186 200
J
U i | i | i | i | i |
80 120

160 £00 £40
324

£80 320
353

360
335 F
i p i i i 0
400
Figure B-21.
Mass spectrum of fourth peak in spiking sample
chromatogram (Fig. B-17).  Matches insufficient for
identification (probability 0.11-0.12).
                                     83

-------
File
Bpk

>B7330
fib 9999

DILUTED STOCK 1

] 52 66 90 1'?6


"N
. le
Bpk



File
Bpk



File
Bpk





l-l 1 , , / ,


PR I POL
flb 9999

j 44
pii


>BIGDB
flb 9999

.1?

>BIGDB
fib 9999

1 t?
j-~
.-,il., . ..


/ "J"!
, . , MQ, . . , .

:50 RNflLYST
SUB

120 132 154
...^ .../ ^
r : | , 1 1 | 1 1
120

LHK D12-CHRYSENE (? 20 Scan 1653
34 .28 min .

156
s*^
160


180 194 212
/ / /
200

Chrysene d-12
.

66 90 1-96
' 1 '•' ' ' 1 ' ' ' ' ' 1 ' ''
30
Benzenamine ,
B

69 77
/ ^
\ ' ' • i • • • i •
SO
2-Propen-l-one ,

65 79 93
/ / .-'

\ I1 'l"l | 1 '!" 1 | 1
30


1?^ 132 154
• ' 1 • • • i • •
120


156
I ' *
160


184 194 203
^ / f .
i • • ' i • ' • i
200
4-<6-methyl-2-berizothiazolyl >-


118
/ 123
120



160
l-<2-hydroxyphenyl

1^ 123 147
l! """""^ i

r i ' I1 i • i i"'i i 	
180

162
f


160



j ... I ... |
200
240
232 t
.. .T/.l..ll, Frj
240

Scan 437
0 .00 min .
240
236 F

240
Scan 85422
0.00 min.
240
:L
240
)-3-<4-hydroxyp Scan 35532
0.00 min .

1?3 194 211
fit


200
240
2£3 || E
•^ (1 C
i -' rQ

240
Figure B-22.
Mass spectrum of fifth peak in spiking sample
chromatogram (Fig.  B-17).   Probability of 0.93 for match
with library spectrum of chrysene-d^-
                                     84

-------
Fil« >B
78000-
70000-
*BOOO-
60000-
55000
50000-
45000-
40000-
35000-
30000-
88000-
&0000-
1BOOO-
10000-
5000-
ec
Fii* >e
75000-
70000-
1 *ooo
60000
55000-
50000-
4500O
40000-
35000-
30000-
86000-
eoooo-
18000-
1000O-
8000-
0-
30
7314 45.0-449.0 UIU. T2-7S RNRLYST LHK D1Z-CHRYSEN
WC TIC
990 i 1000 t 1100 t 1200 § 1300 t 1400











1
I
1
.0 ei'.o ea'.o 23.0 24.0 ss
i



8





5
1
3
A ir
" r --'if- J ™
0 26.0 27.0 26.0 29'. 0 30.0
7314 45.0-449.0 MU. T8-72 OHflLYST LHK D12-CHRYSEM
ODC TIC
15(00 t 1600 f 1700 ( 1800 f 1900





2



14



7-1819
-M/^
0








'.0 31.0 32.0 33.0 34.0 35.0 36.0 37.0 38.0 39.0 40.0
Figure B-23.
Total ion chromatogram of 72-h,  replicate 2 sample.
                                     85

-------
File
Bpk



Q
Bpk




File
Bpk



File
Bpk



>B7314 T2-72
fib 9999.

1 50 63
ol ., 1
40 60
>BIGDB
fib 9999.

-j
j 51 63
Qi ^J, ^i
40 60
>BI6DB
flb 9999.

1 51 63
0 ~*~~pi -i'
40 60
>BI6DB
Rb 9999.

1 51 63
40 60
RNflLYST LHK D12-CHRYSENE 1? 20 Scan 996
SUB

•-_„ 77 94 102
80 100

126 127 151
120 140
1 ,1 '-Bipheny 1 , 2-chloro-



'-^ 77 94 102
80 100



126 127 1?^
"•^r-" y
120 140
1 ,1 '-Biphenyl , 2-chloro-


76
--^. 77 94 102
. | . 1 1 . | , . i . , . 1 . r , i . . , , ,
80 100


126 127 1?^
120 140
1 ,1 '-Bipheny 1 , 4-chloro-


7^ 77 94 113
80 100


126 127 15_^
120 140
22.63 win.
188
152 """
,r*t
160 180 200
Scan 65656
0 .00 min .
188
152 ^i i-
164 .--^ t
160 180 200
Scan 65655
0 .00 min .
188
•"" 164
i . r n
160 180 200
Scan 65625
0 .00 min .
188
152 ' -
173
't '
190 t
i 	 In
160 180 200
Figure B-24.
Mass spectral matching for peak 1 (Fig. B-23) indicated
0.94-0.99 probable agreement with isomers of
monochlorobiphenyl.
                                     86

-------
File >B7314 T2-72
Bpk fib 9999.


1 51 63
nl ...L. ,../...
40
.'e >BIGDB
Bpk fib 9999.


j
\j i i i i i i i
40
File >BI6DB
Bpk fib 9999.


^1 / /
40
File >BIGDB
Bpk fib 9999.

1 51 63
.-. 1 .. . u -.1
U '| i I1 i I1" i i
40
flNRLYST LHK D12-CHRYSENE P 20 Scan 1133
SUB £5


75 93 ±11 126
f, 	 ( „, ,^ , ,>
80 120
1 ,1 '-Biphenyl





80 120
1 ,1 '-Biphenyl ,



75 93 in 126
80 120
1 ,l'-Biphenyl


/ 9,3 HI 126
.11 ( .. >, V,
80 1£0

152
135 1 170 186196 220
160 200
.06 min .
222
^^^-
I , fo

, 2 ,6-dichloro- Scan 80806
0

152
' I
j. r 1

160 200
.00 min.
£££

I I


4,4'-dichloro- Scan 80196
0

152
136 1 162 186 207
/ ,,1. ^ / ^- 1
160 ' 200 '
.00 min.
222
r.
• ' n

, 3,4-dichloro- Scan 80199
0
152
135 161 186196 £09
/ |ll. — - .' / X- I
160 £00
.00 min.
222
1 , 1.

Figure B-25.
Mass spectral matching for peak 2 (Fig.  B-23) indicated
0.93-0.96 probable agreement with isomers of
dichlorobiphenyl.
                                     87

-------
File
Bpk




>B7314 T2-72 ONflLYST LHK D12-CHRYSENE 9 20 Scan 1163
Rb 9999. SUB
1
1 50 63 /5 93 111 126136
J / / i ..„{....(. f ' ii
60 ' 80 100 120 140
25.59 min.
222
53 j-**
168 186 1 f
/ f \\f Fc
160 180 200 220
e >BI6DB l,l'-Biphenyl , 2 ,6-dichloro- Scan 80206
Bpk
flb 9999.
0.00 min.
222
152 ^-


File
Bpk
1
0 i i | i i | i i • i • i • i ' I ' | ' i
60 80 100 120 140
ll f
• . M.i r n
'i | i | i | •' | i | i | i |"'l' | i1 O
160 180 200 220
>BI6DB l,l'-Biphenyl , 2 ,4-dichloro- Scan 80208
flb 9999.
0.00 min.
222
1 152 f -i-
j 51 63 75 93 m 126i35 \ 170 186196 220 I f
J / / / ,' 	 i. .ft .1. / t. / ^11- L

File
Bpk



W 	 r- [ i | i | • | • | • | • | • | • | • | • |
60 SO 100 120 140
• i • i • i • i • i • i • i • i • w
160 180 200 220
>BI6DB l,l'-Biphenyl , 4 ,4 '-dichloro- Scan 80852
flb 9999.
0.00 min.
152 ZSZ
1 70 /5 ^ "-1 126 139
' Vo' ' ' SO' 'lOO ' 'l20 ' 140
165 185 201 I F
i ('. ^ |-. / llljl. FQ
160 180 200 220
Figure B-26.
Mass spectral matching for peak 3 (Fig.  B-23) indicated
0.87-0.96 probable agreement with isomers of
diclorobiphenyl.   Relative retention time distinguishes
this isomer from that shown in Fig.  B-25.
                                     88

-------
File >B7314 T2-72 flNflLYST LHK D12-CHRYSENE 9 20 Scan 1277
Bpk fib 9999. SUB

J


47 68 69 97 3.15 141
f "Tir" i » "^i n

40 80 120 160
27.61 min.
204
/
236 F

200 240
.e >BIGDB 2-Hydroxy-5-chlorobiphenyl Scan 72861
Bpk flb 9999.

•j
rJ



51 63 75 89 115 126 ±/39 151 *-6i
^ / . / ../ ^j / LI **- r

40 80 120 160
0.00 min.
204
3 189 207 E
/ At— -— f0

200 240
File >BI6DB Cl ,1 '-Bipheny l]-4-ol , 4'-chloro- Scan 72880
Bpk flb 9999.

j

„ 11R 141 170
39 55 69 85 11^ 119 / 151 /
v- ,...,...,...,...,.., , , . , ,
40 80 120 160
File >BISDB 2-Chloro-4-bipheny lol
Bpk Ob 9999.

^
j

139
51 63^69 39 ng 126 ' 151 16J
40 80 120 160
0 .00 min .
204
184 210 E
' ' ' 200 ' ' ' ' ' 240 °
Scan 72902
0 .00 min .
204
/ i_
3 208 E
200 240
Figure B-27.
Mass spectral matching for peak 4 (Fig. B-23).
Identification as a hydroxymonochlorobiphenyl isomer with
probability 0.36-0.41.
                                     89

-------
File
Bpk

>B7314 T£-72 RNflLYST LHK D12-CHRYSENE 9 20 Scan 1284
flb 9999. SUB
"j 50 74 J? 93 111 129 «°
J f. ... !>J ... ,L^.. . .y^.....-^. Jl ... . ]. .
£7.73 min.
220 1 F
-" I,L F«
„'• | 1 1 1 | 1 1 1 | 1 1 1 | • • 1 1 ' • 1 | 1 1 > | 1 1 1 | 1 1 1 | 1 1 1 | 1 1 1 | 1 1 1 | 1 1 M
40 80 1£0 160 800 240
e
Bpk

>BIGDB 1, I'-Biphenyl , trichloro-
flb 9999.
'H 186
\ 50 74 JJ> 93 m ±29 150 -""
„{ if . ... ^il 	 i 	 it. '....r~^ .«. .
Scan 90258
0.00 min.
256
- f f
,- 11 F.
V | • • • | • • • | • • • | • •• • | • • • | • • • | • • • | . . | . . . | . • . | 	 	 V
40 80 120 160 200 240
File
Bpk



>BIGDB 1, I'-Biphenyl , 2 ' ,3 ,4-tr ichloro- Scan 90269
flb 9999.
186
1 ->* *s
j 50 74 	 75 JK 11± 12g U>Q 1?2

0.00 min.
256
_^^-
207 2£0 E
/ ^ 111 L
iii "i i i i i i i""i" i i1 u
40 30 120 160 200 £40
File
Bpk



>BIGDB 1, I'-Biphenyl , £ ,3 ' ,5-tr ichloro- Scan 90268
flb 9999.

_j 186
1 50 74 J.5 93 m 129 150 1?0 ^
nl .if „ if .. rT l.-^....-^ .1 , / 1,
0.00 min.
258
•^ 1
215 220 054 F
^^ ^ " -LI.. r«
40 SO 1£0 160 £00 £40
Figure B-28.
Mass spectral matching for peak 5  (Fig.  B-23).   Excellent
match as isomer of trichlorobiphenyl,  probability 0.96-
0.99.
                                     90

-------
File >B7314 T2-72
Bpk fib 9999.

] 50 92 1™1£?
j / --5 i /
nl j ki..i< i l i .1 >•
80 120
flNHLYST LHK D12-CHRYSENE BIGDB 1 ,1 '-Biphenyl , te trachloro-
Bpk fib 9999.
292
220 ,
1 50 9^ 1>° 146^ ^50 184 | 254J?5 it 29?
0 ' t '|* '•"lf'*f 1 * I •
80 120

160 200 240 280 320
File >BIGDB 1 ,1 '-Biphenyl , 3 ,3 ' ,5 ,5 '-te trachloro-
Bpk fib 9999.

1 9£ ^ 127
.-.I ji n .. .{

80 120
292
220 /
^° 184 l' || 296

160 200 240 280 320
File >BI8DB 1 ,1 '-Biphenyl , 2 ,3 ,4 ' ,6- te trachloro-
Bpk fib 9999.

1 92 11012E
,-,1 „ ^~; . f . /
U 1 | 1 | I1 1 f I I
80 120

?9?
220 f
I J.50 185 I || 296

160 £00 240 280 320
20 Scan 1301
£8.04 min.

37i
' '360' ' °
Scan 100686
0 .00 min .
I

360
Scan 100695
0 .00 min .

f

360
Scan 100720
0 .00 min .

I
1 i 1 ' 1 0
360
Figure B-29.
Mass spectral matching for peak 6 (Fig. B-23) indicated
0.87-0.95 probable agreement with isomers of
tetrachlorobiphenyl.
                                     91

-------
File >B7314
Bpk flb 9999.
3 w
.' '1 | V t
.e >BIGDB
Bpk flb 9999.
0' I1' '

File >BIGDB
Bpk flb 9999.
j

File >BI6DB
Bpk Pb 9999.

T2-72 RNPLYST LHK D12-CHRYSENE 1? 20 Scan 1308
SUB POO NRM NSP 28.16 min.
280 290
/ / ,
SB 111 150 255 i f
/ / 121 / 166 188 233 — ' j 300 322 t
80 ' ' f 120rtn 160 '
200 ' 240 ' 280 ' 320
TETRPCHLOROBIPHENYL Scan 100676
0 .00 min .
220 292
/ ,
98_ 110 123 / 185 ^£55 I 2g6 f
if, i .1 .|l ^"",, ,4 ^ i \ • ll. lilr^' hn
80 120 160
l,l'-Biphenyl , 2,2
149
110 123 f 184
80 1£0 160
1 ,1 '-Biphenyl
?2 ""is? S50 184
.{, j. ./ rf ^.
1 fill ' ' ' 1 ' ' 1 1 ' ' 1 1 ' ' 1 1 '
80 120 160
£00 240 280 320
',4,5'-tetrachloro- Scan 100710
0.00 min.
220 292
/ / .
1 255 I, £96 f
1, f \l\r-- F0
200 240 £80 320
, tetrachloro- Scan 100686
0 .00 min .
£20 2J2
' 255 || f7
194 £54 ^" . i £97 t
£00 ' £40 ' £80 ' 3£0
Figure B-30.
Mass spectral matching for peak 7 (Fig.  B-23).  Moderate
agreement with isomers of tetrachlorobiphenyl
(probability 0.52-0.79)
                                     92

-------
File >B7314 T2-72
Bpk Rb 9999.
1 5° ™
QJ ' .. it 	 .
40 80
.e >BI8DB 1
Bpk fib 9999.
1 „
n' i '1 L
U | i i i | i i 1 | i
40 80
File >BIGDB
Bpk fib 9999.
j 50 75^
n u i Jl

40 80
File >BIGDB 1
Bpk fib 9999.

_i
] 50 74
-\ ' ^,
u i i r i i i > 1 i i
40 80
flNRLYST LHK D18-CHRYSENE 9 20 Scan 1393

98 110 12?
{. .. h .{.
120
,1 '-Bipheny 1

92 1/0 128
120
SUB
£9.67 win.
292
220 r" h
150 17Q 184 -X 225 256 885 I, f
r( { .fT . ..L-< ./ -^ ill, F«
' 166 ' 266 ' '
• •• i i i i i i i i i i i i i i -
240 280
, 2,3' ,5,5'-tetrachloro- Scan 100714

0.00 min.
£92
220 \' h
150 184 x. 1 b
.( r (.. IL L
160 ' 200
240 ' 280 ' ' ~
l,l'-Biphenyl , tetrachloro- Scan 100687

92 110 128
t i, ,. ii. .( .

120
,l'-Biphenyl



820
150 184 ^

160 £00
0.00 min.
292
f |_
i, r 2,si L
•\ i i | i i i"| i i i | i i"i' | .' g
£40 £80
, 2,2',5,5'-tetrachloro- Scan 100700


0 .00 min .
292
£20 ^ L
92 110 123
i i i i 1 i i i i i
1£0
,7 ''" " 4 ^
160 £00
i 225 £/55 I E
(^ u, 11., F0
£40 280
Figure B-31.
Mass spectral matching for peak 8 (Fig.  B-23).  Excellent
agreement with isomers of tetrachlorobiphenyl
(probability 0.96-97).
                                     93

-------
File >B7314
Bpk flb 9999
h
nl , .
V 1 i l r
40
. .e >BIGDB
Bpk flb 9999
150
-/
1 ' '
40
File >BIGDB
Bpk fib 9999
j 50
40
File >BIODB
Bpk flb 9999
0-— n—r-
40
T2-72
74
1 /
80
74
SO
74
1 ' ' 'so
1
74
80
109 127
. ,r^ . L r
120
ONflLYST LHK D12-CHRYSENE 
-------
File >B7314 T2-72 RNRLYST LHK D12-CHRYSENE 9 20 Scan 1436
Bpk fib 9999.
1"
^ i f\
•J \ \ f'|
\
. .'e >BISDB
Bpk Rb 9999.
-i

• i • |
File >BI6DB
Bpk flb 9999.
J

File >BI6DB
Bpk fib 9999.

J

SUB
73 98 110 149i59
4 t J '1 '' /' f
80 120 160

l,l'-Biphenyl


74 109 127 145
80 120 160
l,l'-Biphenyl , 2,2'

109 127 135 163
Y •• "i -1 1" •
80 120 160
l,l'-Biphenyl , 2,3»


80 120 160
184
' 266'

256
219 \ 29°
(1. ")
240 280

, pentachloro-


184
/
200
,3, 4', 5

184 gj
/
\. . .
200

254
T (L ™
1 1 • • ' i • • ' i • • • i • ' •
240 280
'-pentachloro-

,1 2r 2*i
£40 280
,4,4' ,5-pentachloro-


£00

256
240 £80
30.43 min.
326
306 | f
\*\ 10
'••320 '

Scan 108107
0.00 min.
326
f h
,1,0
1 . . . 1 I'l i [ U
320
Scan 108115
0.00 min.
326
ft :o
'••320
Scan 108108
0.00 min.
326
1, t
320
Figure B-33.
Mass spectral matching for peak 10 (Fig. B-23)
agreement with isomers of pentachlorobiphenyl
(probability 0.36-0.58).
                                                                   Moderate
                                     95

-------
File >B7314
Bpk flb 9999

1 58
J ^


e >BI8DB
Bpk flb 9999

•
j

File >BIGDB
Bpk flb 9999


1
nl


File >B!SDB
Bpk flb 9999

T2-72 flNflLYST LHK D12-CHRYSENE 9
SUB

75 86 110 137 iJ3186
I,'!../ ^1 I L

80 120 160 £00
20 Scan
1451
30.70 min.

"" M /'
i i i i-i if
240
3-t1ethoxy-4,5)4'-trichlorobiphenyl
£86
i
i i i I i'"r i
280



Scan 99756
0 .00 rain .

173
100 111 13^ 143 { 186 207
~^r N/. .,. ,1. JT^i. .1,1 .1^ . '. ...f.
[ ' ' ' \ ' ' | * •!•••(••. |..f|l..|...[
80 120 160 200


243
221 f
240
3-nethoxy-2,£' ,5 '-trichlorobipheny 1
286
/
I
iii) i»'h •
280


=.

Scan 99782
0 .00 min .

173
100 110 13^ 15° \ 186 207
"^. 4- y.,.^.,1- H- ,- -,'4 .1^, (.. ',- -i.j.

80 120 160 200


236245
' „'"
i Vl-K

240
PHENYL-DI-D5-PHENYLPHOSPHIHE OXIDE


1 54 77 J32 W6 128 159 163 190 206

SO 120 160 £00
240
288

273 1
..' 11,1.
i i i 1 I'-'f i
280


•
^0

Scan 99203
0 .00 min .
286
...1.
£80



Figure B-34.
Mass spectral matching for peak 11 (Fig.  B-23).  Moderate
to poor agreement with isomers of
methoxytrichlorobiphenyl (probability 0.27-0.42).
                                     96

-------
File >B7314
Bpk fib 9999.

1"
J r,

. e >BI6DB
Bpk fib 9999.

H
J "


File >BIGDB
Bpk Ob 9999.
-\
0 ,?M-

File >BI6DB
Bpk fib 9999.

^
J ,

T2-72


73
f
SO

RNOLYST LHK D12-CHRYSENE @
SUB

105 12714Q 184 218 254
i r^ \ f f { \\
120 160 200 240 280
1 ,1 '-Biphenyl , pentachloro-
20 Scan 1516
31 .85 min .
326
ill
||]|
320

-
-0

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0 .00 min .


74
j ..

80


254
109 127 145 ^?4 218 / 291

120 160 200 240 280
1 .1 '-Biphenyl , pentachloro-
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326

74
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120 160 £00 £40 £80


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0 .00 min .
326
{

320


-n

Figure B-35.
Mass spectral matching for peak 12 (Fig.  B-23).
Identified as isomer of pentachlorobiphenyl (probability
= 0.83-0.86).
                                     97

-------
File >B7314 T2-72 flNRLYST LHK D12-CHRYSENE 9 20 Scan 1535
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272
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Figure B-36.
Mass spectral matching for peak 13 (Fig. B-23)
Identification uncertain.
                                     98

-------
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222 253 .' 325
240 280 320
2,2' ,3,4,4 ' ,5-Hexachlorobiphenyl
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80 ' 120 ' 160 ' 200
l,l'-Biphenyl , 2,2', 3, 4,
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360
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360
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0.00 min.


80 ' 120 ' 160 ' 200


240 280 320
360
, u
360
Figure B-37.
Mass spectral matching for peak 14 (Fig. B-23).
Excellent match with isomers of hexachlorobiphenyl
(probability = 0.86-0.95); moderate match (probability
0.50) with tetrachlorobiphenyl.
                                     99

-------
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80 120 160 200 240 280
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Mass spectral matching for peak 15  (Fig.  B-23).   Library
search yielded poor to moderate tentative identification
as methoxy derivative of brominated biphenyl.
                                     100

-------
File >B7314 T2-72 ONOLYST LHK D12-CHRYSENE (? 20
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342
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104 159 173 235 250 263 329 / fc

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342
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327342
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Mass spectral matching for peak 16 (Fig.  B-23).  Library
search yielded poor tentative identification as  methoxy
derivative of brominated biphenyl (probability = 0.25-
0.36) .
                                    101

-------
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!308 h
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-------
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-70
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Figure B-41.
Mass spectral matching for peak 18 (Fig. B-23).  Library
search yielded no matches.
                                    103

-------
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241 313
173 205 -^ 251 271 / 3
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356
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356
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339 f
f r Fo
360
Figure B-42.
Mass spectral matching for peak 19 (Fig.  B-23).   Library
search yielded good tentative identification as isomer of
methoxypentachlorobiphenyl (probability = 0.73-0.93)
                                     104

-------
File >B7314 T2-72
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20 ' 160 200 240 ' 280 ' 320
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242 E
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240
L^3 ^J 1/°7l/Cl "? 165 211 2f3 || 242 f
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search yielded good match (probability = 0.85) with
internal standard, chrysene-d^-
                                    105

-------
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V 	 f ^ t ^ . 	 --.!^ .1 >.ll.
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Total ion chromatogram of extract from untreated, 72 h
control sample.
                                     106

-------
                   APPENDIX C - VOLATILIZATION CALCULATIONS

INTRODUCTION

      Estimates of volatile emissions that could accompany quicklime treatment
of PCB-laden soils were made by Louis J. Thibodeaux of Louisiana State
University.  The equations were patterned after models he developed for Region
1 of EPA in relation to the New Bedford Harbor (Mass.) Superfund site .
Further calculations based on these equations were made by the authors to
improve the agreement between calculated and observed PCB losses in open-
vessel reactions and to examine the model's sensitivity to various parameters.

MODEL DEVELOPMENT

      For the conditions of the open-vessel experiments, it was assumed that
most of the volatile emissions would occur during heat evolution caused by
quicklime slaking.  It was further assumed that there was no resistance to PCB
transport (no buildup of PCB concentration) in the vapor phase since strong
ventilation was used in the glove box where the experiment was conducted.
Thus, volatile emissions would depend on diffusive transport of vapor-phase
PCB from a porous medium.

      The evaporation rate was calculated as:

                                    W = AK/3                                (1)

where W is the evaporative loss rate (g/h), A is the surface area (cm ),  K is
the transport coefficient (cm/h), and /o is the PCB congener vapor
concentration (g/cm ) .
        Thibodeaux,  L.  J.   Theoretical Models for Evaluation of Volatile
Emissions to Air During Dredged Material Disposal with Applications to New
Bedford Harbor, Massachusetts.  U.S. Army Corps of Engineers, Miscellaneous
Paper EL-89-3.  Prepared under Contract No. DACW39-87-M-2487, U.S. Army
Engineer Waterways Experiment Station, Vicksburg, MS,  39181.
                                      107

-------
      /"> is calculated from the ideal gas law as:

                                    f> = ZJi                                 (2)
                                        RT
       *
where P  is the temperature-dependent pure component vapor pressure (mm Hg) , M
is the molecular weight  (g/mol), R  is the gas constant (cm  mm Hg kelvin  mol
 ),  and T is temperature (kelvin).   We assumed that the experiment was
conducted at an atmospheric pressure of 760 mm Hg, although the glove box was
                                            *
actually under slightly  reduced pressure.  P  was calculated as:

                                 P* = exp(A+B/T)                             (3)

                            *
using literature values  of P  at various temperatures to evaluate the
empirical constants A and B.  Literature values were not found for the
                                                       *
specific congeners used  in this study.  Consequently, P  values for Aroclors
approximating the chlorine content  of DCBP, TCBP, and HCBP were used.

      The transport coefficient, K, cm/hr, was calculated according tot

                             K = De1-33(l-e) +  S                            (4)
                                      H

where D is diffusivity  (cm /h),  e is matrix porosity (cm /cm ) , H  is the
height of the solid matrix at 0 porosity (cm), S/t is the mass of solvent lost
over time (g/h) andyOsis the vapor  density of the solvent (g/cm ).   The  term
(1-e) effectively converts the solids height to total height  (bed depth) for
any porosity value.  The first term of the equation represents transport by
evaporation while the second term represents steam stripping.

      The diffusivity of PCB congeners has not been reported  in the
literature.  However, Thibodeaux used a value of 0.036 cm /s for Aroclor 1242
at 25 C.  Knowing this value and the relationship between diffusivity,
temperature and molecular weight allows calculation of estimated diffusivities
for pure PCB congeners.  According  to the Chapman-Enskog equation:

                         D 
-------
                        D oCT1'75 x  (1/Mp^ +  l/Ma1r)'5                        (6)
Given known molecular weights  and  a value of D for Aroclor  1242,  D  can be
estimated for any congener by  ratio of Daroclor1242 to D  .,  rearranging:

                  Dpcb =  129.6/jrV-5  (5.114)/_L_ +  _1_V5                 (7)
                              \ 298/          V  Ma1r   M^J

where the value  129.6 is Darociori242 in cm2/h, and 5.114 is the value for the
molecular weight term for Aroclor  1242.  Evaluating D  by  the Fuller-Schettler-
Giddings equation can be performed in the same manner.

CALCULATIONS

Constant and Variable Values

      The molecular weights of  DCBP, TCBP,  and HCBP are 223, 292, and  361
g/mol, respectively.  The molecular weight  of air was  approximated  at  29
g/mol.  Open vessel experiments were conducted in 9.93-cm diameter  beakers,
yielding a surface area of 77.4 cm .   The height of the spiked solid phase  (50
g silica matrix plus 120 g CaO) prior to water addition was measured at 2.9
cm.  Assuming a density of 2.65 g/cm  for the matrix and 2.2 g/cm  for
hydrated lime (120 g CaO = 159  g Ca(OH)2),  the solids volume would be 91.1
cm ,  with a solids height of 1.18 cm at 0 porosity.   Comparison of the solids
volume and measured volume yields  a porosity of 0.59.

      We did not measure the weight loss of either the spiking solvent or
excess water following the slaking step.  Consequently, it  is difficult to
estimate the contribution of steam stripping to the transport coefficient.
Assuming that steam stripping only occurred during slaking, when  steam
evolution was observed, the following estimate can be made.  Addition of  50 mL
water to 120 g quicklime yields a  2.8:2.1 mole ratio.  Thus, after  complete
slaking, 0.7 mol or 13 g water  available for evaporation.   Since  the sample
appeared nearly dry after the peak temperature was observed, most of this
water must have evaporated in the  short time the sample was heated  above
100°C.

      P  values  published for Aroclors 1232, 1248,  and 1260 were used to
                                           *
calculate the coefficients for  evaluating P  at experimental temperatures for
DCBP, TCBP, and HCBP, respectively.  The values used and  resultant  calculated
coefficients are presented in Table C-l.
                                      109

-------
                                   Table  C-l
                *                                  *
               P and Calculated Coefficients for P  = exp(A+B/T)
            Aroclor
              ID
  P
mm Hg
  T
kelvin
1232


1248


1260





4.06x10
2.2 xlO °
-4
4.94x10
5.3 xlO"1
->;
4.05x10
7.6 xlO 2
7.6 xlO 2
.5
9. xlO
1.5 xlO"1
298
373

298
373

298
693
6.73

293
373
                                             2.58x10
                                             2.71x10
                                             1.93x10
                                             1.99x10
                                             1.89x10
                                             2.53x10
                                             3.08x10
                                  -9.33x10
                                 -1.03x10
                                 -8.76x10
                                 -8.96x10
                                 -8.28x10
                                 -1.01x10
                                 -1.22x10
               Values of A and B for Aroclor 1260  are  calculated,
            in the order shown in the Table, from the  following
            data pairs:  298 and 693 kelvin, 298 and 673 kelvin,
            293 and 673 kelvin, 293 and 373 kelvin,  and 298 and
            373 kelvin.

Model Sensitivity

      Calculated evaporation rates are quite sensitive to several variables in
                *
the equation.  P ,  which is linearly related to/>, varies  widely with
                                       *       '
selection of the literature values of P  used to calculate the  temperature-
dependence coefficients.  Figure C-l shows vapor pressure-temperature curves
for Aroclor 1260 used in this exercise to approximate  HCBP.  The differences
increase greatly in the temperature range of interest  in this study (about 185
*C or 458 kelvin) .
                                      110

-------
          500
           400
           300
           200
           100
              VAPOR PRESSURE, mm Hg
                                                -83—EB—Si-
                        100
     200         300
TEMPERATURE, kelvin
400
                            500
                            293,673
293,373
                      298,373
Figure C-l.  Variation of vapor pressure with temperature depends strongly on
                                         *
             which literature values of P  are used to calculate constants
             for equation (3).

      The transport coefficient, K, is composed of an evaporation term and a
steam stripping term (eq. 4).  The former depends strongly on diffusivity, D,
and less strongly on porosity.  Diffusivity was estimated by two formulas, the
Chapman-Enskog and Fuller-Schettler-Giddings equations.  Figure C-2 shows the
variation of transport coefficient with porosity for both equations.   In both
cases, the transport coefficient reaches a maximum at approximately 60 percent
porosity (balance of increasing pore space with increasing diffusion path
length); values in the range of 40 to 80 percent porosity are within about 25
percent of the maximum value.  The assumed temperature dependence of
diffusivity has a much greater effect, with the transport coefficient
increasing more than 400 percent at a porosity of 0.6 as the exponent on the
temperature term is increased from 1.5 (Chapman-Enskog) to 1.75 (Fuller-
Schettler-Giddings) .
                                     Ill

-------
        120

        100

         80

         60

         40

         20 h

          0
            TRANSPORT COEFFICIENT, cm/h
           0
                    -a	B-
   0.2
                                 0.4         0.6
                                   POROSITY
                                     0.8
                         Chapman-Enskog
                            Fuller et al.
Figure C-2.
Effect of diffusivity estimation method on evaporation term
of transport coefficient,  as a function of porosity.Figure
C-2.
      The steam stripping term is equally sensitive to solvent evaporation
rate, surface area, arid solvent vapor density (eq.  4).  When the water loss by
steam stripping was estimated to be 7-11 g over 8 min, the steam stripping
term varied from 1373 - 2158 cm/h, and the associated loss of PCBs was in the
range of grams per hour.  Clearly, much less steam stripping occurred in the
open vessel experiments conducted in this study, because substantial fractions
of the PCB congener masses were still present at the end of the experiment.
Further modeling of steam stripping would require actual measurement of vapor
losses under the various temperature conditions used in the experiment.  It
might also require consideration of solvent and PCB interactions with the
matrix that could hinder PCB transport.  For these reasons, the steam
stripping term was generally set equal to zero for calculations of PCB loss by
volatilization.  The interesting point is that these limited calculations show
that steam stripping is capable of removing large quantities of PCBs from non-
interacting matrices.

Comparison of Calculated Evaporation Rates with Experimental Data

      Calculated versus observed PCB losses are shown in Figure 5 of the main
body of this report.  The calculated loss curves were constructed by
                                      112

-------
calculating evaporation rates at several temperatures and multiplying the
rate by the estimated time a sample was held within a temperature range
(Table C-2).  To obtain calculated values that bracketed observations,
measured values of  solids height and porosity were used with the Chapman-
Enskog equation for diffusivity and steam stripping was omitted.

                                 Table  C-2
               Calculated  PCB Losses  for Open-Vessel Reactions
                                    STEPWISE PCB LOSS   CUMULATIVE
                                    DCBP  TCBP  HCBP  REACTION TIME, h
ACTION*

Spike
Slake
Cool
Slurry
Cool
Ambient



TIME
min
2
60
180
50
420
720
1440
1440
TEMP
kelvin
453
383
358
323
298
298
298
298
                                     0.
                                   150.
                                    96.
                                    51.
                                     0.96
                                     0.57
                                     0.98
                                     1.96
                                     1.96
 0.
84.
36.
16.
 0.23
 0.10
 0.18
 0.36
 0.36
 0.
26.
12.
 5.7
 0.08
 0.04
 0.07
 0.14
 0.14
 5
12
24
48
72
         The time and temperature for each reaction phase are estimated
      from the range of measured values.

      Figure C-3 shows a set of calculated loss versus reaction time curves
for HCBP using other assumptions.  In all cases, varying the solids height
and porosity by ±10 percent had little effect on the loss curve.  Changing
                                            *
the temperture-dependence coefficients for P  had a greater effect,  in one
case yielding a prediction of essentially no HCBP loss.  The greatest
influence was exerted by the method of estimating diffusivity.  When the
Chapman-Enskog equation was replaced by the Fuller-Schettler-Giddings
equation, predicted HCBP losses for the 72-h open vessel reaction increased
from about 20 percent to 100 percent.

      The model used in this comparison, by omitting the steam stripping
term, is not completely appropriate since it is intended for estimating
evaporation from dry materials.  In our experiments, the materials were
briefly wet during quicklime slaking and were slurried with water for a 3-h
heating period.  The model can be extended to wet matrices, as shown in
equation (4) and as Thibodeaux did for the New Bedford Harbor sediments.
However, the uncertainty due to unknown diffusivities and vapor pressures
of pure PCB congeners, described above, would severely limit confidence in
                                    113

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predicted  losses.  Further work in this area must be preceded by
experiments  to generate vapor  pressure and diffusivity  data.
       120
          HCBP REMAINING, percent
        80
        60
        40
        20
         0
Figure  C-3.
                        20
                    40
                TIME, h
          60
          80
              baseline
              helght-10%
          poroslty+10%
          293,673
poroslty-10%
293,393
helght+10%
Fuller et al.
Variation of  calculated evaporative  losses as equation
parameters  are  altered.
                                       114

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