EPA/540/2-89/011
      SUPERFUNDTREATABILITY
            CLEARINGHOUSE
               Document Reference:
  Shirco Infrared Systems. "Final Report: On-Site Incineration of Shirco Infrared
Systems Portable Pilot Test Unit, Times Beach Dioxin Research Facility, Times Beach,
   Missouri." Technical report prepared for U.S. EPA. Approximately 200 pp.
                    November 1985.
              EPA LIBRARY NUMBER:

            Superfund Treatability Clearinghouse - EUTR

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               SUPERFUND TREATABILITT CLEARINGHOUSE ABSTRACT
Treatment Process:

Media:

Document Reference:
Document Type:

Contact:
Site Name:

Location of Test:
Thermal Treatment - Infrared Incineration

Soil/generic

Shirco Infrared Systems.  "Final Report:  On-Site
Incineration of Shirco Infrared Systems Portable
Pilot Test Unit, Times Beach Dioxin Research
Facility, Times Beach, Missouri."  Technical report
prepared for U.S. EPA.  approx. 200 pp.  November
1985.

Contractor/Vendor Treatability Study

U.S. EPA - Region VII
726 Minnesota Avenue
Kansas City, KS  66101
913-236-2800

Times Beach Dioxin Research Facility, MO (NPL)

Times Beach, MO
BACKGROUND;  During the period of July 8 - July 12, 1985, the Shirco
Infrared Systems Portable Pilot Test Unit was in operation at the Times
Beach Dioxin Research Facility to demonstrate the capability of Shirco's
infrared technology to decontaminate silty soil laden with 2,3,7,8-
tetrachlorodibenzo-p-dioxin (TCDD) at a concentration range of 156 to  306
ppb.  Emissions sampling and final analysis was performed by Environmental
Research & Technology, Inc. (ERT), while laboratory analysis of the
emissions and soil samples was performed by Roy F. Weston Inc. Shirco
Infrared Systems prepared the testing procedure protocol and operated  the
furnace system.
OPERATIONAL INFORMATION;  A singe 55 gallon drum of contaminated road  bed
soil which had been screened through 1/2 inch mesh and homogenized in  a
mixer was used.  Two primary furnace solid phase residence times were
evaluated: 30 minutes and 15 minutes.  Emissions and soil sample testing
accompanied both of these tests.   A consistent furnace feed rate averaging
47.7 Ib/hr at a 1 inch bed depth was maintained during the 30 minute
residence time test.  The feed rate during the 15 minute residence time
test averaged 48.1 Ib/hr with a 0.75 inch bed depth.
    An important process parameter during testing was chamber temperature,
in both the primary and secondary chambers.  Over the effective process
length of the primary chamber, temperature was controlled in two equal
length zones.  During the 30 minute residence time test, the feed end  zone
maintained a nominal temperature of 1560°F and the discharge end zone
maintained a nominal 1550°F.  For the 15 minute residence time test, the
respective temperatures were both 1490°F.  The secondary combustion chamber
was heated by a propane burner and its temperature was maintained above
2200 F during both tests.  The nominal secondary chamber temperatures were
3/89-6                                               Document Number:  EUTR
   NOTE:  Quality assurance of data may not be appropriate for all uses.

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 2250°F and 2235°F, respectively, for the 30 and 15 minute primary chamber
 residence time tests.
 PERFORMANCE!  For both tests, the soil discharge concentration of
 2,3,7,8-TCDD was less than 38 parts per trillion.   Based upon the expected
 detection limit of 50 picograms of 2,3,7,8-TCDD as measured by the Weston
 GC/MS system and the sampling volume capability of the ERT emissions test
 equipment, the feed rates were more than adequate to confirm the required
 99.9999% Destruction Removal Efficiency (DRE).   Particulate emissions were
 well below the standard of .08 gi/SCF @ 7% 02-   Laboratory QA/QC procedures
 are discussed in the report.

 CONTAMINANTS;

 Analytical data is provided in the treatability study report.   The
 breakdown of the contaminants by treatability group is:

 Treatability Group             CAS Number        Contaminants

 W02-Dioxins/Furans/PCBs        1746-01-6         Tetrachlorodibenzo-p-
                                                   dioxin (TCDD)
3/89-6                                                Document  Number:   EUTR

   NOTE:  Quality assurance of data may not be appropriate  for all uses.

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                   FINAL REPORT






           ON-SITE INCINERATION TESTING



                        OF



SHIRCO INFRARED SYSTEMS PORTABLE PILOT TEST UNIT






       TIMES BEACH DIOXIN RESEARCH FACILITY



              TIMES BEACH, MISSOURI
               REPORT NO. 815-85-2



                NOVEMBER 14, 1985

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 SUMMARY

 During the  period  of July  8  through July  12,  1985, the Shirco  Infrared Systems
 Portable  Pilot Test Unit was  in  operation  at  the Times Beach Dioxin Research
 Facility  to demonstrate the  capability  of  Shirco's infrared technology to suc-
 cessfully decontaminate soil  laden with 2,3,7,8 tetrachlorodibenzo-p-dioxin
 (TCDD).   Equipment set-up, preliminary  operation, test operation, decon-
 tamination, and  takedown were  performed during this period.  Operation of the
 furnace system to  decontaminate  the dtoxin-laden soil, and sampling of stack
 emissions,  feed, and discharge streams  were accomplished on July 10 and 11.
 The Missouri Department of Natural Resources  Environmental Division coordinated
 the site  preparation.  Emissions sampling  and final analysis was performed by
 Environmental Research & Technology,  Inc., (ERT) while laboratory analysis of
 the emissions and  soil samples was performed  by Roy F. Weston Co.  Shirco
 Infrared  Systems prepared  the  test protocol and operated the furnace system.

 The testing was  planned such  that adequate material quantity would be processed
 and adequate samples of emissions and soil would be taken to assure that maximum
 soil decontamination and destruction  efficiency levels would be demonstrated.
 Two (2) primary  furnace solid  phase residence times were evaluated: 30 minutes
 and 15 minutes.  Emissions and soil sample testing accompanied both residence
 time tests.  A consistent  furnace feedrate averaging 47.7 Ib/hr at a 1 inch bed
 depth was maintained during  the  30 minute  residence time exposure.  The feedrate
 during the  15 minute residence time test  averaged 48.1 Ib/hr with a 0.75 inch
 bed depth.  Based upon the expected detection limit of 50 picograms of
 2,3,7,8-TCDD as measured by  the  Weston  GC/MS/MS system and the sampling volume
 capability  of the ERT emissions  test  equipment, the feedrates were more than
 adequate  to confirm the required 99.9999 % destruction efficiency.

 An important process parameter during testing was chamber temperature, in both
 the primary and  secondary  chambers.   Over  the effective process length of the
 primary chamber, temperature was controlled in two equal length zones.  During
 the 30 minute residence time test, the  feed end zone maintained a nominal tem-
 perature  of 1560°F and the discharge  end zone maintained a nominal 1550°F.  For
 the 15 minute residence time test, the  respective temperatures were both 1490°F.
 The secondary combustion chamber was  heated by a propane burner and its tem-
 perature was maintained above  2200°F  during both tests.  The nominal secondary
 chamber temperatures were  2250°F and  2235  °F, respectively, for the 30 and 15
minute primary chamber residence time tests.  The temperature  of the exhaust  gas
 leaving the wet  gas scrubber and discharging  into the atmosphere was nominally
 165°F over  the entire test duration.

The emissions test sampling performed by ERT  was accomplished  using a modified
EPA Method  5 with XAD-2 resin  to capture  any  dioxin present in the exhaust
gases.  The procedures, results  and quality control for these  tests are
explained in the Appendix A  report submitted  by ERT.

The analysis of the emissions, feed soil,  and discharged soil  samples were per-
formed at the EPA-approved Weston laboratory  located at the Riedel Environmental
Services  Office in Chesterfield, Missouri.  The test procedures, results, and
quality control are presented  in their  report presented in Appendix B.

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 In  summary,  these  two  appendices  report:
Composite feed soil
2,3,7,8-TCDD concentration

Composite discharge soil
2,3,7,8-TCDD concentration

Participate emissions
at 7% 02

Gas Phase ORE of
2,3,7,8-TCDD
      EPA
   STANDARD

     N/A


    <1 ppb


0.08 gr/dscf


>99.9999%
 30 MINUTE
 RESIDENCE

  227 ppb
 Not detected
 at 38 ppt

0.001 gr/dscf
>99.999996%
 15 MINUTE
 RESIDENCE

  156 ppb
 Not detected
 at 33 ppt

0.0002 gr/dscf


>99.999989%
In conclusion, the testing performed by Shirco  Infrared Systems  using  the
Portable Pilot Test Unit has proven the process and  technology to  be a success-
ful method of decontaminating the dioxin-laden  soil  present  at Times Beach,
Missouri.  The following report discusses  the equipment,  feed material,  and  pro-
cedures used in the test program, and  results of  that  program.
The Appendix A and B reports present  in detail  the  emissions  sampling  and  sample
analysis results and procedures.                                          '

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                               TABLE OF CONTENTS
Summary

1.0  Introduction

2.0  Test Equipment

     2.1  General
     2.2  Material Feed
     2.3  Primary Chamber
     2.4  Secondary Chamber
     2.5  Combustion Air System
     2.6  Offgas Handling System
     2.7  Control System
     2.8  Data Acquisition System
     2.9  Heating Element Power Centers (HEPC's)

     Figure 2-1  Portable Pilot Test Unit
     Figure 2-2  Equipment Layout

3.0  Safety Procedures and Equipment

     3.1  General
     3.2  Protective Equipment
     3.3  Personnel Training
     3.4  Emergency Procedures
     3.5  Stress Monitoring and Breaks
     3.6  Protective Equipment Application and Decontamination
     3.7  Furnace Operating Safety
     3.8  Process and Testing Equipment Decontamination

4.0  Site and Test Material Description

     4.1  Site Description
     4.2  Test Material

5.0  Test Conduct and Procedures

     5.1  Operational History
     5.2  Equipment Set-Up
     5.3  System Heat-Up
     5.4  Contaminated Soil Feed
     5.5  Scrubbing System
     5.6  Operating Data Log
     5.7  Operating Conditions
          5.7.1  Test Condition Matrix
          5.7.2  Primary Chamber Temperature
          5.7.3  Primary Chamber Residence Time
          5.7.4  Secondary Chamber Temperature
          5.7.5  Primary and Secondary Chamber Combustion Air

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          5.7.6  Contaminated Soil Feed Rate
          5.7.7  Furnace Draft
     5.8  Emissions Testing
          5.8.1  General
          5.8.2  Sample Procedures
     5.9  Soil Sampling
     5.10 Soil and Emissions Sample Analysis

     Table 5-1  Test Condition Matrix

6.0  Test Results/Conclusions

     6.1  General
     6.2  Feed Material
          6.2.1  Material Properties
          6.2.2  Soil Feed Rate
     6.3  Soil Decontamination
     6.4  Stack Emissions/DRE
          6.4.1  2,3,7,8-TCDD Emissions
          6.4.2  Particulate Emissions
     6.5  Scrubber Effluent Analysis
     6.6  Equipment Operation
     6.7  Process Temperatures
     6.8  Power Usage

     Figure 6-1  Feed History - 30 Minute Residence Time
     Figure 6-2  Feed History - 15 Minute Residence Time
     Figure 6-3  Temperature Recorder Chart - July 9, 1985
     Figure 6-4  Temperature Recorder Chart - July 10, 1985
     Figure 6-5  Temperature Recorder Chart - July 11, 1985

     Table 6-1  Test Data Summary
     Table 6-2  Furnace Feed History - 30 Minute Residence Time
     Table 6-3  Furnace Feed History - 15 Minute Residence Time
     Table 6-4  Operating Power Consumption

7.0  References

Appendix A  ERT Emissions Sampling Report
Appendix B  Weston Laboratory Analysis Report
Appendix C  Site Safety Plan
Appendix D  Test Site Description
Appendix E  Operating Logs
Appendix F  UMC Laboratory Analysis Report
Appendix G  Personnel health Monitoring Data

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1.0  INTRODUCTION

     Dioxin  contamination  of  Times  Beach,  MO,  and  the  community's  subsequent
     evacuation,  closing,  and disincorporate have  been  well-documented  and
     publicized.   Today, an estimated  200,000  tons of  dioxin-contaminated soil
     exists  within the  city limits,  which  have been  sealed  off  to  unauthorized
     entry.

     The  Missouri  Department  of  Natural  Resources  (MDNR)  has set up  a  Dioxin
     Research  Facility  within the city.  MDNR's mission  is  to  investigate means
     of decontaminating the soil, including  thermal  destruction.   Concurrently,
     the  U.S.  EPA has extended the  Resource  Conservation  and Recovery  Act (RCRA)
     to require  incineration  of  dioxin-bearing materials  to achieve  a  destruc-
     tion and  removal efficiency (DRE) of  99.9999 percent of the dioxin.   During
     July, 1985,  Shirco Infrared Systems,  Inc.  (Shirco),  and its Portable Pilot
     Test Unit became the  focal  point  for  DNR's investigation of on-site  thermal
     destruction  of dioxin.

     Shirco  Infrared Systems  has perhaps the only mobile  pilot  waste thermal
     processing system  available.   This  system is  comprised of  a belted electri-
     cally powered primary furnace,  a  propane  fueled secondary  chamber, a com-
     bustion air  supply system,  a single venturi wet gas  scrubber, and a  process
     monitoring and control system.  During  the week of July 8, 1985,  tests were
     performed at  the Dioxin  Research  Facility  for the process  of  determining
     the  ability  of the Shirco Portable  Pilot  Test Unit to  meet the  EPA
     emissions and soil decontamination  standards  for  dioxin incineration.  The
     test program  consisted of three (3) days  of thermal  processing, of which
     two  (2) were.spent accumulating emissions  and soil samples.   The  remaining
     time was  devoted to equipment  set-up, decontamination  and  take-down.

     MDNR requested the incineration test  and  coordinated site  preparation.  The
     emissions and soils sampling was  performed by Environmental Research and
     Technology,  Inc. (ERT),  with subsequent laboratory analysis by  Roy F.
     Weston Co. (Weston).  Shirco provided the  portable incineration pilot
     system and coordinated the  test operations.   In order  to evaluate the test
     and  its results, presented  herein is  a  description of  the  portable pilot
     incineration  system,  safety procedures, test procedures, and  results.

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2.0  TEST EQUIPMENT

    2.1  General

          The Shirco Portable Pilot Test Unit (Figures  2-1,  2-2)  is  designed  to
          demonstrate the performance of the Shirco Infrared "Furnace in  a
          variety of thermal  processing applications.   The  system consists  of a
          feed metering conveyor,  infrared primary chamber,  gas-fired secondary
          chamber, offgas handling, data acquisition and  control  equipment, and
          heating element power centers (HEPC's).  The  system is  housed in a 45'
          van trailer.

     2.2  Material Feed

          Material to be processed is fed onto a metering conveyor located  at
          the feed end  of the furnace by manual  dumping.   The  metering belt  is
          synchronized  with the furnace conveyor to control  the  material  feed rate.
          A feed  hopper is mounted above the conveyor belt.   The conveyor  is
          shrouded and  equipped with rubber skirts to  minimize inleakage of  air
          or escape of  furnace gases.  An adjustable guillotine-type gate  is
          provided at the conveyor discharge.  The gate levels the material  and
          distributes it across the width of the metering belt.   The gate  and
          the material  behind it complete the furnace  sealing  feature.  Final
          feed area sealing is provided by an additional  adjustable  knife  gate
          in the  feed chute into the furnace.

          The metering  conveyor drive is interlocked with the  secondary chamber
          temperature monitoring system.  If the secondary chamber temperature
          should  fall below a preset value, feed to the primary  chamber is  auto-
          matically shut off.

     2.3  Primary Chamber

          The primary chamber consists of a rectangular cross  section "box"
          fabricated from carbon steel and lined with layers of  ceramic fiber
          blanket mounted on stainless steel studs, and retained with ceramic
          fasteners.  The material to be processed is  conveyed through the  fur-
          nace on a woven wire belt which is supported on high-temperature alloy
          rollers.  The rollers are, in turn, supported by external  flange-mount
          bearings.  A  friction drive system is used to pull the belt through
          the furnace.   When the processed material reaches the  discharge end of
          the furnace it drops off of the belt through a chute and into an
          enclosed hopper.  The hopper contains a  residue sampling drawer and
          seal gate for collection of "grab" samples of ash during processing.
          Infrared energy is provided by transversely-mounted heating elements.
          The elements  are silicon carbide rods, with external electrical  con-
          nections at both ends.  Access to the connections is gained by
          removing sheet metal wireway covers.  The elements are grouped into
          two (2) control zones, with each zone being powered by a heating ele-
          ment power center (HEPC).

          The primary chamber has nominal external dimensions of 2.5 ft wide  x
          9.0 ft  long x 7.0 ft high, and an installed weight of 3000 pounds.
          Its process capabilities include 500 - 1850°F process temperature,
          with material residence time variable between ten and one  hundred
          eighty  minutes (10 - 180 min).  Oxidizing, reducing, or neutral
          atmospheres can be provided.

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     For the test conducted at the Times Beach facility, the primary
     chamber was operated in the incineration mode.

2.4  Secondary Chamber

     The secondary chamber is similar in construction to" the primary
     chamber and also uses ceramic fiber blanket insulation.  A propane-
     fired burner is used to ignite combustible gases present in the
     exhaust, and burn them at a predetermined temperature.  Propane is
     supplied from a gas bottle located outside the system trailer.  The
     chamber is sized to provide the required combustion residence time for
     the gases at setpoint temperature (typically 1.5 to 2.2 seconds).  It
     has external dimensions of 3.0 ft wide x 9.0 ft long x 3.0 ft high, a
     weight of 1,500 pounds, and process capabilities of 2300°F, 2.2
     seconds gas residence time, and 0-100% excess air.  The burner is
     mounted in the chamber end plate, with the flame pattern intercepting
     incoming primary chamber exhaust gases at a 90° angle.  A pilot and
     electronic flame monitoring are provided as safety measures.  Chamber
     operating temperature is controlled by adjusting the manual gas valve
     and air registers.  Temperature is measured by a thermocouple located
     at approximately 1/3 of the chamber length from the burner outlet.

     The secondary chamber served as a gas-fired afterburner in this test.
     It was used to raise the primary chamber exhaust to a minimum 2200°F
     temperature before discharging those gases to the scrubbing system.

2.5  Combustion Air System

     Combustion air for the primary and secondary chambers is supplied by a
     blower with manual adjustment of airflow rate and distribution.  A
     splitter manifold with dampers at the blower outlet allows control of
     airflow to both chambers.

     In the primary chamber, air is injected at various points along the
     length of the chamber through a manifold system.  Adjustment of the
     flow  to an  injection point is by means of manually-adjusted blast gate
     valves.

     In the secondary chamber, air is injected through  the chamber top and
     sides directed at  the  interface of the burner flame pattern and
     exhaust gas  inlet  flow.  Adjustment of flowrate  is by means of a blast
     gate  valve  and the burner air registers.

2.6  Offgas Handling System

     Exhaust  gases  from the  secondary chamber pass through  a venturi
     scrubber  section  containing water  sprays, and a  separator  tower.  A
     manually-adjustable  cone-type damper  located  in  the venturi  section  is
     used  to  control  scrubber  pressure  drop.

     The  sprays  in  the  venturi  inject  a fine  water mist into the  exhaust
     stream.   The water droplets  are  sized  to  "capture" particulate  grains
     by having the  grains impact  the  droplets  as  they pass  through  the
     sprays.   The larger  and heavier  water-covered particulate  grains  are
     then  removed from the  air stream in  the  separator tower by gravity,
     centrifugal  force, and additional  water sprays.   In addition  to
      removing particulate,  the scrubber cools  the gases from their  incoming

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     temperature (1000°F - 2200° depending on system configuration)  to
     saturation temperature, usually about 180°F.   Subcooling  to  a  lower
     temperature can be performed if required, but consumes  substantially
     more water than cooling to saturation temperature.

     A sump tank with recirculation system is uncluded in the  scrubbing
     system.  The sump has a nominal 30 gallon capacity  with provisions for
     water makeup, system blowdown, and water sample acquisition.  The
     recirculation system was used during the Times Beach test to minimize
     total scrubber water discharge.

     An induced draft exhaust blower is located on the discharge  side of
     the scrubber.  The blower is capable of exhausting  the  primary and
     secondary chambers, producing a slight (typically 0.01  in. WC) draft
     on the system, while overcoming the 10.0 in.  WC pressure drop of the
     scrubber.  A butterfly damper is located on the outlet  side  of the
     blower.  The damper provides a means of manually adjusting the induced
     draft gas flow.

     A removable exhaust stack is installed through the  trailer roof.  The
     stack extends 10 feet above the trailer roof, and is equipped with two
     (2) standard sampling ports.  Access to the sampling ports is provided
     by scaffolding or a lift platform installed alongside the trailer.

2.7  Control System

     A master control panel contains the following control devices:

             Primary chamber zone temperature controllers
             Alarm Lights
             Hand-Off-Auto switches for mechanical components

     Alarm lights are provided for the following mechanical  and process
     conditions:

             Furnace temperature high
             Wireway cover open
             SCC temperature high
             SCC temperature low
             SCC purge
             High stack temperature
             Low scrubber water pressure

2.8  Data Acquisition System

     The control panel contains the following devices for process  data
     recording and monitoring:

             Multi-point temperaure recorder  (6 points)
             Digital thermocouple  reading  display  (12 points)
             Furnace running time  totalizer
             Primary chamber zone/secondary  chamber power
              consumption  totalizers and  indicators

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          In addition, operating parameters  can  be  monitored  at  the  following
          system components:

                  Scrubber (pressure drop)
                  Scrubber venturi  (water flowrate  and  pressure)
                  Scrubber separator (water  flowrate and  pressure)
                  Primary chamber exhaust (draft)
                  Secondary chamber exhaust  (draft  and  residual  oxygen)

2.9  Heating Element Power Centers  (HEPC's)

     Heating elements in the  two primary chamber zones  are  powered  by  a  10  KVA
     heating element power center to control  the flow of  electricity to  the
     heating elements.  Primary power input  required for  each power  center  is  3
     phase, 60 Hz, 480 volts  at 12  KVA.   A similiar HEPC  will be  installed  for
     the secondary chamber at a later date.   Each power center consists  of  a
     solid-state power controller driving the heating elements through a tapped
     step down transformer, mounted in a NEMA 3R (ventilated) enclosure.

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3.0  SAFETY PROCEDURES AND EQUIPMENT

     3.1   General

          Safety precautions  comensurate with this  operation were  taken  for  per-
          sonnel and equipment  protection.   Responsibility  for safety  was  shared
          so that  each company  or government agency involved provided  its  own
          equipment.  However,  the Missouri  DNR  Emergency Response Team  was
          responsible for assuring that all  safety  procedures  used complied  with
          the requirements of the Appendix  C safety plan and that  all  personnel
          protection equipment  was correctly worn and  maintained.   Riedel
          Environmental  Services  (RES), under contract to MDNR,  provided a
          safety briefing prior to the  start of  testing.  RES  also provided  a
          qualified  registered  nurse who monitored  each individual's vital
          signs  during rest breaks.

     3.2   Protective Equipment

          The guidelines  for  personnel  protection presented in the safety  plan
          were adhered to for this test program.  In summary,  the  personnel  pro-
          tection  equipment included:

          1.   All  equipment complied with NIOSH  Class  C specifications and
              requirements.                                              ,

          2.   Respiratory protection including a full  face  respirator  with orga-
              nic  vapor/acid  cartridges and  dust filters.

          3.   Dermal  protection including Tyvek  full body suit,  inner  light-
              weight PVC  or latex gloves, buna nitrile rubber  outer gloves,  and
              steel-toed, shanked neoprene  work  boots.

     3.3   Personnel  Training

          To  assure  correct use of the  protective equipment and  facilities,  mem-
          bers of  both the MDNR Emergency Response  Team and RES  presented  a
          safety briefing.   This briefing  included a  demonstration of the use
          and application of  the  protective  equipment, a description of  the  site
          including  the area  where safety equipment must be worn and the decon-
          tamination and  rest areas.

     3.4   Emergency  Procedures

          MDNR set up a minor injury first  aid station in the  rest area.  The
          nurse  in this area  was  capable of  providing  first aid  for minor
          injuries and the effects of minor  heat stress.  As noted in  Appendix
          C,  emergency phone  numbers were posted at the guard  gate entrance  to
          Times  Beach.

     3.5   Stress Monitoring and Breaks

          The stress monitoring procedures  presented in Appendix C were  strictly
          enforced.   The  registered nurse measured  and recorded  the ambient  Wet
          Bulb Globe Temperature  (WBGT) at  one hour intervals.  Prior  to
          entering and immediately upon exiting  the contaminated area, the nurse
          measured the worker's oral  temperature, blood pressure,  and  pulse
          rate.  Based upon the wet bulb temperatures, which ranged from 80  to

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     95°F, the nurse recommended that the person's time in the contaminated
     area be kept between 15 and 30 minutes.  Subsequent to each period a
     worker spent attired in the safety gear, a rest period was taken in
     accordance with the safety plan.

3.6  Protective Equipment Application and Decontamination

     The Missouri DNR marked the designated site areas where protective
     equipment was required, and where such protective equipment could be
     removed for rest breaks.  The designated contaminated zone was inside
     the fenced research area (see map in Appendix D).  The research area
     was a 50 foot by 60 foot fenced plot with a gravel ground cover.  The
     pilot trailer was located parallel to and 15 feet from the 50 foot
     fence.  In addition, MDNR set up an area for application, removal, and
     decontamination of the protective equipment.  The decontamination pro-
     cedures presented in the Appendix C safety plan were followed.

     The rest area was set-up outside the fence of the research area.  The
     rest area was located under trees to provide shade to allow personnel
     to cool off after work periods in the contaminated area.

     Before entering the contaminated area, a worker first put on a Tyvek
     suit.  Neoprene boots were then put on and tape applied to seal bet-
     ween the boots and the suit.  A latex inner glove was put on fallowed
     by a buna nitrile outer glove.  Tape was applied to seal the outer
     glove to the suit arms.  Finally, a full face respirator was put on
     and its seal checked.  The worker was then cleared to enter the con-
     taminated area.

     Two wash tubs were placed inside the contaminated area near its exit.
     When ready to exit the contaminated area, a worker stepped into the
     first tub which contained soapy water.  Using a scrub brush, the boots
     and outer gloves were washed.  Then the boots and gloves were rinsed
     by stepping into the second bucket and using the rinse scrub brush.
     The worker then removed the outer gloves and placed them on a table at
     the edge of the contaminated area to dry.

     Before removing the respirator the person would exit the contaminated
     area.  After removing and wiping off the respirator with clean paper
     towels, the inner gloves were removed.  However, prior to the removal
     of the gloves the person would tear off the Tyvek suit if it were
     dirty, or torn.  The inner gloves and suit were discarded in a special
     container located just  inside the contaminated area.  At this time,
     the worker  proceeded to the rest  area for a measurement of vital
     signs.

     While working  in the area designated for protection equipment person-
     nel  did not  remove  any  portion of his protective equipment.  As noted
     in Appendix C,  any  damage to that equipment  required the worker to
     pass  through the decontamination  area,  remove the damaged article,
     wash  accordingly, and  put on an  undamaged replacement before returning
     to  the contaminated area.

     During the  work day workers took  required rest breaks by  removing  only
     their respirators and  gloves  in  the decontaminating area.  When
     leaving the  area for an eating  break, equipment was  removed  and

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     a shower taken to prevent any possibility of ingesting the contaminated
     dirt or transporting it to an uncontaminated area.

     Precautions were taken during furnace operation to assure personnel in
     the vicinity were not subjected to any health danger.  The safety
     equipment discussed in preceeding sections was worn and kept in good
     condition at all times.  The organic vapor/acid cartridges and dust
     filters in the respirators were changed each operating day.  Used
     cartridges and filters turned over to the MDNR Emergency Response
     Team for proper disposal.

3.7  Furnace Operating Safety

     Procedures for obtaining transporting, and feeding the contaminated
     dirt to the furnace primary chamber minimized dust agitation.  When
     loading transport containers from the contaminated dirt storage drums
     personnel  located themselves upwind of the drum.  Dirt was removed
     from the drums using a shovel.  The dirt in the drums was not agitated
     or tossed, but removed and transported carefully.

     Considering the potential health hazards, the primary concern during
     operation was not to pollute the atmosphere.  This pollution could
     occur by allowing unburned gases to be released from the furnace or
     exhaust stack ifthe secondary chamber temperature were allowed to fall
     below approximately 2100°F.

     In order to prevent local atmospheric pollution, the operators con-
     tinuously monitored the secondary chamber temperature to assure it
     remained above 2100°F.  During the test program secondary chamber tem-
     perature did not fall  below 2100°F and the residual oxygen did not
     fall below pre-determined safe levels.

3.8  Process and Testing Equipment Decontamination

     For this decontamination, soap, water, hoses, and spray wand were
     supplied by MDNR.  Also, MDNR and RES supplied qualified persons to
     aid in the decontamination and serve as supervisors.

     At the completion of material processing, the primary chamber was
     baked out  at 1600°F in both control zones in order to volatilize any
     dioxin potentially remaining.  This bake-out was performed for four
     (4)  hours.  During bake-out the temperature near the feed module floor
     was  spot-mom'to red and recorded.  The secondary combustion chamber was
     operated at 2200°F during bake-out to assure no spread of dioxin to
     the  offgas handling system or atmosphere.  The system was then suf-
     ficiently  cooled overnight before the trailer was disconnected from
     utilities.

     At the conclusion of the bake-out a sample of insulation was removed
     through a  one-inch diameter port located in the coolest expected loca-
     tion in the material feed end of the furnace.  The sample was taken
     from this  location because any soil which may have fallen off the belt
     below the  feed chute would collect there.  If a subsequent analysis
     found excessive levels of dioxin (greater than 1 ppb) the feed half of
     the  furnace would have to be cleaned internally and the outer
     (exposed)  layer of insulation removed.  The sample was delivered to
     the  Weston TAGA Van, located at the RES office, for analysis.  An

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overnight analysis found no TCDD to a detection limit of 0.20 ppb.
Consequently, no decontamination of furnace internal surfaces or com-
ponents was required.

The portable pilot equipment decontamination and research area cleanup
was conducted with participating personnel in Class-C gear.  The
exhaust stack and all loose equipment were transported to the
designated decontamination area near research facility office.  Then
all trash (Tyvek suits, gloves, tape, sheet plastic, and paper towels)
were bagged, barreled, and correctly labeled as hazardous waste.
After the area was cleaned, the pilot trailer was moved to the decon-
tamination area.

The furnace feed metering conveyor was the only item which required
removal from the system for decontamination.  The conveyor was removed
and sufficiently disassembled to enable it to be thoroughly washed
with a high pressure water spray.  After decontamination of the
trailer, the conveyor was loaded for transport to Shirco's shop
facility where it was re-assembled and installed on the furnace.

The external surfaces of all equipment and the walls, ceiling, and
floor of the trailer were decontaminated next.  First the furnace
discharge chute and hopper internal surfaces were vacuumed with a
HEPA type vacuum cleaner.  Then the external surfaces of the primary
chamber, exhaust ducting, secondary chamber, control panel, scrubber,
and power distribution system were vacuumed.  After all surfaces were
vacuumed a fine spray wand was used to wash down the walls and floor
of the trailer.  Care was taken not to get the control panel and power
distribution systems wet.  The wand was then used to rinse the walls
and floor of the trailer.  After this was completed, the equipment and
inside of the trailer were considered decontaminated.

The fluorescent light bulbs in the trailer were removed next.  These
were carefully washed with soap and water and placed in their boxes.
While the vacuuming of the trailer was in process the loose equipment
such as tools, exhaust stack, portable stairs, ladder, drain hose,
etc., were washed with soap and the high pressure water spray.  All
auxiliary equipment was then placed back  in the trailer in preparation
for transport.

When all equipment was in the trailer, its doors were locked.  Then
the external surface  of the trailer was washed with water using the
spray wand.  Immediately  upon completion  of this washing the trailer
was removed  from  the  Times Beach site.

In addition  to  the Shirco equipment,  all  ERT emissions test equipment
used at  the  test  area was decontaminated  by washing with soap and
water  or methyl  chloride.

After  each  operating  day, the scrubber sump was drained and  refilled.
MDNR ground  disposal  facilities were  used  to dispose of the water.   A
scrubber water  sample analyzed  at  the conclusion  of testing  showed  no
dioxin  present,  to a  detection  limit  of 1  ppb.  Based on this analy-
sis, it  was  determined  that disassembly and cleaning of the  scrubber
were not  required.

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4.0  SITE AND TEST MATERIAL DESCRIPTION

     4.1  Site Description

          Times Beach is a city in St. Louis county,  Missouri.  A description of
          the location, history, and contamination is presented in Appendix D.
          The city made arrangements in 1972 to have  oil  spread on its dirt
          roads for dust control.  The used oil that  was  applied contained quan-
          tities of 2,3,7,8 Tetrachlorodibenzo-p-dioxin (TCDD) which was later
          found to be a hazardous material.  As a result, the city was eva-
          cuated, purchased by the U.S. EPA, and a research facility built to
          study means of decontaminating the area.

          The research area referred to in this report is a nominal  50 foot by
          60 foot plot parallel to the Laurel  Road research plots and approxima-
          tely 100 yards from Beach Drive (see map in Appendix D).  This plot is
          covered with gravel  and fenced on all sides.  For this test MDNR
          contracted to have electrical power run from the existing transformer
          in the research area to a breaker box.  This breaker box would supply
          480 volt/60 amp/3 phase power for system operation.  In addition, 120
          volts/60 Hz/1 phase receptacles were installed  for trailer lighting
          and emissions test equipment operation.  Water  to fill the system wet
          gas scrubber recycle tank was made available from a standard outdoor
          hydrant located just inside the research plot fence.  Outside the
          fenced research area is a gravel parking lot and drive leading to
          Main Road.

     4.2  Test Material

          The soil  used for the thermal process testing was acquired from the
          road beds in the city.  A description of the soils and geology of the
          city is presented in Appendix D.  A single  55 gallon drum of con-
          taminated soil  was used for this test program.   The soil had been
          acquired from one of the more highly contaminated roads in the city.
          The road bed soil  had earlier been screened with a lyfc inch mesh and
          homogenized in a mixer.

          The original  laboratory analysis to define  the  2,3,7,8-TCDD con-
          centration in the drum of soil  was performed by the Environmental
          Trace Substances Research Center at the University of Missouri
          -Columbia.  A concentration of 248 ppb was  found.  As a check, an ana-
          lysis was performed on July 8 at the Weston TAGA van located at the
          Spirit of St.  Louis Airport in Chesterfield, MO.  The sample analyzed
          was soil  from the top of the drum.  This analysis found a con-
          centration of  260 ppb.

          Although the soil  was not analyzed for moisture and combustible con-
          tent, estimates based upon visual inspection were that the moisture
          content ranged from 15 to 20 percent and the combustible content was
          approximately 5 percent on a dry basis.  Based  upon compaction in the
          full  drum, the density was estimated at between 90 and 100 lb/ft3.
          When removed from the drum and broken, the  soil density more nearly
          ranged from 60 to 70 Ib/ft^.  At the low moisture content, this soil
          was not clay-like but tended to crumble easily.

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5.0  TEST CONDUCT AND PROCEDURES

     5.1  Operational History

          The first day of material  processing was conducted on Tuesday, July 9.
          The heat-up of the unit began at 0600 hrs.  Prior to initiating feed a
          problem developed with a primary chamber zone 2 power control signal.
          This was successfully remedied and the first soil was fed to the fur-
          nace at 1245 hrs.  At this time the primary and secondary chamber tem-
          peratures were stable at 1600°F and 2300°F, respectively.  The test
          plan, based upon a conservative 2,3,7,8-TCDD laboratory detection
          limit estimate and the contaminant concentration in the feed soil, was
          to acquire an emissions sample over a seven (7) hour period.  This was
          to ensure that the required 99.9999 percent destruction efficiency of
          the 2,3,7,8-TCDD in the stack emissions could be demonstrated.

          The emissions sampling was initiated at approximately 1330 hrs.  All
          operation and sampling preceded well until 1500 hrs.  At this time a
          fuse blew at the site power source breaker.  While the problem was
          being investigated, adequate draft was maintained on the primary and
          secondary chambers to prevent the escape of emissions into the
          trailer.  The secondary chamber temperature remained high for over one
          primary chamber residence time, thus no atmospheric pollution was
          assumed to have occurred.  Because of the late sampling start and the
          electrical system upset, it was decided to restart the sampling the
          next day.

          The first of two (2) full days of test started on July 10, 1985.  The
          furnace heat-up began at 0300 hrs.  With the primary chamber and
          secondary chambers at operating temperature, soil feed began at 0720
          hrs.  The belt speed in the primary chamber was adjusted to a resi-
          dence time of 30 minutes.  As can be seen by reviewing the Appendix C
          operating logs and temperature charts the system operation remained
          steady throughout the day.  Because the wet gas scrubber system uti-
          lized recycled water the stack gas temperature was nominally 170°F.
          This temperature resulted in a 30% (by volume) moisture content which
          required some adjustment of heaters on the emissions sampling probes.
          By 1015 hrs the ERT crew had made the adustments needed for this
          operation and the emissions sampling began.  For the next seven hours
          until 1715 the system and emissions sampling ran consistently without
          need for adjustments.  System shutdown began at 1716 hrs with the
          stoppage feed dumping and start of equipment cool down 30 minutes
          later.  The data logs were maintained, material fed, feed and
          discharge samples taken, and the system operation monitored throughout
          the day as described in the following sections.

          On the second day of testing, the purpose was to obtain data for
          operation with a 15 minute material residence time in the primary
          chamber.  The system heat-up began this day at 0300 hrs.  The test
          options this day were to process either the 260 ppb-contaminated
          material that remained for a short duration, or the next highest con-
          tamination level material  (117 ppb) available for a longer duration.
          ERT's calculations showed  that, with the  260 ppb material, approxima-
          tely two hours of sampling was needed to  potentially capture enough
          dioxin to  verify a minimum 99.9999 % destruction efficiency.  Based
          upon a pre-test weighing of the barrel of 260 ppb-contaminated  soil,
          approximately 180 pounds  remained after the previous two days of

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     operation.   It was determined that the most viable option would
     include a change  in only the residence time variable.  Thus, the 260
     ppb contaminated  soil was used for the second day of testing.

     In order to establish the feed rate at the 15 minute residence time,
     the 117 ppb material was initially fed.  The feed depth was set 0.75
     inches, consistent with primary chamber process power capacity.
     However, at this  rate, some clogging of the feed gate was experienced
     due to rocks and  dirt chunks in the material.  This required more
     operator attention to prevent feed blockage. After one hour of feeding
     the 117 ppb material, feed of the 260 ppb material feed was initiated.
     The soil remaining in the barrel contained more moisture toward the
     bottom of the barrel.  Consequently, it had a tendency to aglomerate
     and clog at the gate somewhat like the 117 ppb material.  In order to
     provide a consistent feed to the furnace, an operator monitored and
     prepared the soil as required to prevent clogs during the entire
     emissions test period.  The emissions and soil sampling began at 1058
     hrs and continued until  the last 260 ppb material was fed at 1320
     hours.  After the sampling was completed the soil was given time to
     clear the furnace.

     At approximately  1400 hours the system decontamination bakeout was
     initiated, as described in Section 3 of this report.  The system was
     prepared for transport to Shirco's Dallas, TX, facility on the evening
     of July 12 and morning of July 13.

     Presented in the  following sections are more detailed descriptions of
     test and operating procedures and parameters for individual system
     components.

5.2  Equipment Set-Up

     The Portable Pilot Test Unit trailer arrived at the test site at 0830
     hrs on July  8, 1985, and was driven to and positioned in the research
     area by 1030 hrs.  The equipment and supplies stored in the trailer
     for transport were removed.  Spare parts and supplies not readily
     needed that  might be subject to rain damage were taken to the decon-
     tamination area and placed in the facility office trailer.  This
     trailer was  also used by the ERT emissions test personnel for sample
     train recovery and sample storage.

     All MDNR, ERT, RES, and Shirco personnel gathered at the site at 1400
     hrs to begin the equipment set-up.  Midway through the set-up a break
     was taken for all participants to receive a safety briefing presented
     by MDNR and  RES.  A total of nine (9) personnel were involved in the setup
     (and subsequent decontamination and teardown) of the test equipment.

     The ERT personnel set up their sampling equipment while the MDNR, RES,
     and Shirco personnel  mounted the exhaust stack above the trailer.  A
     scaffold was set up alongside the furnace trailer to provide access to
     the stack for emissions  sampling.

     The area designated for use of the class C safety gear was set-up by
     MDNR and RES.  RES also  connected wiring from the trailer to the
     breaker panels, and connected the scrubber water supply hose.  Shirco
     personnel  installed the  primary chamber heating elements, the secon-
     dary chamber baffles, the control panel instruments, the ash discharge

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     receiving barrel, the scrubber drain hose, and the trailer inside
     lights.  By 2000 hrs all equipment had been made operational.

     With pilot system and emissions test equipment set-up along with the
     contaminated, decontamination, and rest areas, the individual system
     components were operated as the final check point i-n the set-up proce-
     dure.  The system was then declared ready for operation the following
     day.

5.3  System Heat-Up

     Approximately four hours prior to initiating contaminated soil feed to
     the primary chamber, heatup was initiated.  Temperature setpoints of
     1600°F were used for both control zones.  After the primary chamber
     temperature reached 1000°F, the secondary chamber heat-up was ini-
     tiated.  The propane fuel flow rate was initially set at the maximum
     to minimize time required to reach operating tmepenature.

5.4  Contaminated Soil Feed

     Contaminated soil was transferred from the drum to the furnace feed
     conveyor in approximate 20 Ib increments.  The soil was shoveled from
     the drums to a 5 gallon plastic bucket.  Care was taken by the Shirco
     operator to minimize dust agitation.  The plastic bucket was weighed
     prior to filling, and the corresponding tare set on the scale.  After
     filling the 5 gallon bucket, it was weighed and the exact weight
     recorded.  Thus the recorded weight  included only the soil.  The time
     of depositing the weighed soil into the feed hopper was also recorded.
     The feed container was  then positioned on top of the feed conveyor
     hopper and approximately one-half of the  soil transferred to the
     hopper.  Approximately  15 minutes later the remaining contents of the
     bucket were dumped  into the hopper.  The  feed hopper cover remained in
     position except when depositing soil in the hopper.

5.5  Scrubbing System

     The wet  gas  scrubbing system was  adjusted to produce a nominal
     pressure  drop of 9  inches w.c.  The  venturi water flow was set to 1
     gpm while the venturi quench  and  seperator tower  sprays were adjusted
     to  produce a  nominal stack  temperature of 170°F.

     The  scrubber  liquid was a  recirculating water flow  from the  sump tank
     located  below the  venturi  tower.  The  operator  drained  and refilled
     the  reservior each  day  of  testing.   The 30 gallons  of wastewater were
     drained  onto  the  ground outside  the  research  area,  as directed  by
     MDNR.  During operation,  the  operator  regularly checked the  water
     level  in the sump  tank.  There was  no  need for  make-up  water.

 5.6  Operating Data  Log

     The Shirco operators maintained  the  operation log presented  in
     Appendix E.   Data was  recorded at one  hour  intervals.   Comments  rela-
     tive  to changes in the system operations,  interruptions, and per-
     tinent observations were recorded as they occurred.

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5.7  Operating Conditions

     5.7.1  Test Condition Matrix

            The test condition  matrix used  for  this  test-program  is  pre-
            sented  in Table 5-1.

     5.7.2  Primary Chamber Temperature

            The soil  contaminant  dioxin,  2,3,7,8-TCDD,  is known to volati-
            lize between  800°F  and  1000°F (Reference 1).   Also, it has  been
            found by testing in the U.S.  EPA's  mobile incinerator that
            acceptable processing of 2,3,7,8-TCDD-contaminated soil  is
            obtained at primary chamber temperatures between  1600°F  and
            1700°F  (Reference 2).

            For this test of the  Shirco system, the  primary chamber  Zone A,
            (drying and initial volatilization  zone) and  Zone B (high tem-
            perature volatilization and oxidation  zone) were  both
            controlled at a setpoint temperature of  1550°F.   These tem-
            peratures were maintained by  adjusting the  controller for each
            zone to that  setpoint value.  A thermocouple  probe extending
            into the process chamber at the mid-point of  the  control zone
            provided the  feedback signal  on which  the control was based.
            Electric power was  supplied by  the  individual  zone power center
            in response to the  controller output signal.

     5.7.3  Primary Chamber Residence Time

            Test condition #1 used  a primary chamber soil  residence  time of
            30 minutes.  The condition #2 residence  time  was  15 minutes.
            These residence times are based upon a furnace effective length
            of 66.5 inches.  The  residence  time was  set by adjusting the
            furnace belt  speed  control dial  on  the variable speed drive
            motor.   The rotational  speed  of the primary chamber end  drum
            was measured  by stop  watch.   The drive speed  was  then adjusted
            to produce the desired  rotational speed.

     5.7.4  Secondary Chamber Temperature

            EPA research  results  performed  prior to  this  test suggested
            that the complete destruction of dioxin  is  accomplished  at  a
            gas residence time  of 2.2 seconds and  a  temperature of 2200°F
            (Reference 2).  In  accordance with  these conditions and  other
            data acquired during  the EPA  mobile incineration  system  testing
            at Denney Farms, the  secondary  combusiton chamber temperature
            was maintained between  2100°F and 2250°F for  all  test con-
            ditions.

            The secondary chamber was heated by a  propane burner  with
            manual  control.  The  chamber  temperature was  set  during  heat-up
            at the  maximum fuel flow. The  adjustment was made  by a  hand
            valve upstream of the burner.  As the  chamber temperature
            approached the setpoint temperature the  operatior incrementally
            decreased the fuel  rate.  This  adjustment procedure covered
            nominally a 30 minute period  after  which the  chamber  tem-
            perature would remain constant  at a steady fuel flow  rate.

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       Upon Initiation of soil feed the operator would make minimal
       adjustments in the input fuel rate to maintain the setpoint
       temperature.  Due to the steady soil feed rate and consistent
       soil properties, very few fuel flow adjustments were required
       while processing soil.

5.7.5  Primary and Secondary Chamber Combustion Air

       The air injected into the primary chamber was supplied at a
       flow rate estimated to be adequate to oxidize any combustible
       material in the soil.  An air-to-fuel ratio of 8.0 Ib air/lb
       combustibles was used, along with a moisture content of 15% and
       combustible solids content of 5% (dry basis). Fifty percent
       excess air was supplied.

       Combustion air for the secondary chamber was set based upon the
       residual oxygen concentration measured in the secondary chamber
       exhaust stream.  The portable unit was designed to process a
       wide range of waste materials.  When processing a waste with
       low moisture and combusible content, waste gas velocity rather
       than residual oxygen content becomes the important air control
       parameter.  The combustion air blower damper was adjusted to
       produce a nominal residual oxygen content in the secondary
       chamber exhaust gases of 1%.  This value was based upon the
       volumetric flow rate of gas in the secondary chamber needed to
       produce adequate mixing.

5.7.6  Contaminated Soil Feed Rate

       The feed rate of contaminated soil to the primary furnace was
       controlled by the furnace belt speed setting and the gap
       opening of the feed conveyor guillotine gate.  The speed of the
       feed conveyor and furnace conveyor belts are synchronized.
       Both are driven by the same drive motor and are geared accor-
       dingly.  The guillotine to belt gap was 1.0 inch for test #1
       and 0.75 inches for test #2.  It is estimated that the bulk
       density of the contaminated soil was 70 Ib/ft^.  The resulting
       feed rates for the 30 and 15 minute residence times were 46 and
       70 pounds per hour, respectively.  However, the feed rate on
       the second day was limited to 48.1 Ib/hr to eliminate potential
       clogging of the feed inlet.

5.7.7  Furnace Draft

       Both the primary and secondary chambers were operated under a
       slight  negative pressure to prevent contaminants being emitted
       into the atmosphere through system pressurization.  The draft
       pressure in the primary chamber was maintained at approximately
       -0.015  inches w.c. above the processed soil discharge chute.
       The secondary chamber was adjusted to approximately -0.06
       inches  w.c.  These adjustments were made using the exhaust
       blower, scrubber venturi, and primary chamber exhaust duct  dam-
       pers.

       The procedure used is  based on opening the exhaust blower damper
       enough  to allow the desired primary and secondary chamber
       drafts  to be maintained while adjusting the scrubber venturi

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           damper to produce a scrubber pressure drop in excess of  -10
           inches w.c.

5.8  Emissions Testing

     5.8.1  General

            During both the 30 and 15 minute primary chamber residence
            time operations the stack gas was sampled for 2,3,7,8-TCDD  and
            particulates.  A modified U.S. EPA Method 5 sampling train  was
            used for the sampling.  Two sampling trains were used for each
            test condition.  This provided a duplicate back-up sample.

            The sampling test duration was based upon the concentration of
            2,3,7,8-TCDD in the soil  and the detection limit available  in
            the Weston laboratory.  The pre-test indication from Weston
            was that a 1 picogram/microliter detection limit of 2,3,7,8-
            TCDD was practical.  Since a 50 microliter sample was used  for
            gas chromatograph/mass spectrometer analysis, the stack
            sampling would have to be of a duration that could potentially
            catch 50 picograms.  Given the sampling volume flow rate and
            the estimated stack volumetric flow rate, a sampling duration
            was calculated for each residence time condition.  Because  the
            possibility existed that the sample analysis might have ,to  be
            performed by a laboratory with a detection limit of 250
            picograms, the final  sampling duration was based on that
            detection limit and calculated to be 7 hours.

            To provide some understanding of how the test duration was
            calculated, an example of calculations and other procedures
            used to  this duration for the 30 minute residence time test
            condition follows.

     5.8.2  Sample Procedures

            Estimated stack sampling rate :  40 scfh

            Calculated stack gas  flow rate:  6000 scfh

            Soil  dioxin concentration:       260 ppb

            Primary  chamber feed  rate:       46 Ib/hr (20,884 g/hr)

            Total  dioxin processed:

                Mdioxin   s  20,884 g/hr X 260 X 10'9 g/g

                          =  5.42984 X ID'3 g/hr

            Total  dioxin emitted  at 99.9999 % ORE

                ^emitted  =  5.42984 X 10-3 x (1 - 0.999999)

                          *  5.4298 X 10-9 g/nr

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            Stack dioxin concentration:

                            =  5.4298 X 1Q-9 g/hr

                                   6000 ft3/hr

                            =  9.04973333 X 10'13 g/ft3

            If laboratory detection limit is 250 X 10"12 grams for a 50
            microliter injection, the total sample volume required is:

                  ^sample   =      250 X 1Q-12 grams

                               9.04973333 X lO'*3 g/ft3

                            =  276.25 ft3

            At a sampling rate of 40 ft3/hr, the duration of sampling must
            be:

                  Sampling *   275.25 ft3

                                40 ft3/hr
                                                                   <
                            =  6.9 hrs

            Accordingly, a sampling duration of seven hours was used.

5.9  Soil Sampling

     Composite feed and discharged soil samples were taken during each
     test condition.  The soil sampling was performed over the entire
     emissions sampling duration.  Each composite had a volume of one (1)
     liter.  Each time material was fed to the feed hopper, approximately
     50 milliters was added to the sample jar.

     At approximately 30 minute intervals the discharge chute sampling
     tray was emptied into the sample jar.  For test #2 the amount of
     material added to the sample jar was doubled.

     Extreme care was taken to prevent contamination of the product soil
     sample.  The discharge chute sample drawer was sterilized in a 2000°F
     muffle furnace prior to being taken to the site.  Clean gloves were
     used to remove the sample drawer and deposite the sample into the
     container.  The sample drawer was not placed on potentially con-
     taminated surfaces during the transfer process.  A product sample was
     not acquired while a feed transfer was in process.  At the conclusion
     of each operating day the feed and discharge samples taken were tran-
     ferred to the office trailer in the decontamination area.  An ERT
     representative transferred the samples to the Weston laboratory at
     the end of  the two days of testing.

5.10 Soil and Emissions Sample Analysis

     The laboratory analysis of the feed soil, discharged soil, and
     emissions samples were performed  by Weston using their York/Weston
     REM-MS2 mobile GC/MS/MS laboratory.  This laboratory was located at

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the RES office in Chesterfield, Missouri, where it was condcting work
under another contract from the U.S. EPA.

In addition to the Weston analysis, the University of Missouri  at
Columbia laboratory analyzed a duplicate feed soil and discharged
soil  for MDNR in keeping with their policy of verifying the results
of a decontamination test.  Along with the soil samples the UMC
laboratory analyzed a scrubber effluent sample.  The specific test
procedures used by the two laboratories are presented in detail in
Appendices B and F for Weston and UMC, respectively.

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      TABLE 5-1



TEST CONDITION MATRIX
Condition
Number
1
2
Date
7/10
7/11
Primary
Chamber
Residence
Time (min)
30
15
Contaminated
Soil
Feed Rate
(Ib/hr)
46
70
Temperatures
Primary Chamber
Zone 1
1600
1600
Zone 2
1600
1600
Secondary
Chamber
2200
2200

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6.0  TEST RESULTS/CONCLUSIONS

     6.1  General

          The primary objectives  of  the  test  program were  to  confirm  the  ability
          of the Shirco Infrared  Systems process  to  decontaminate  dioxin-laden
          soil  and to incinerate  the dioxin  at a  verified  destruction and remo-
          val efficiency (ORE)  of 99.9999 %  or greater.

          The data from emissions and discharged  soil  sampling,  and subsequent
          analysis of that data,  form the basis for  determining  whether or not
          those objectives were met.  A  discussion of  the  data and analysis
          results  is  contained  in following  sections.   In  addition, the equip-
          ment  operating data is  of  interest  with respect  to  the conditions
          under which the decontamination results were obtained.

     6.2  Feed  Material

          6.2.1  Material Properties

                 Standard procedures for testing  performed by Shirco  Infrared
                 Systems include  having  the  feed  material  analyzed for moisture,
                 combustibles,  and contaminant content along  with  density and
                 calorific value. However,  the laboratories  used  to  measure  the
                 dioxin contamination concentrations were  not equipped to ana-
                 lyze for the other  properties.

                 Since the performance of the system with  respect  to  dioxin
                 destruction was  a main  purpose of the test program,  furnace
                 operating conditions were specifically adjusted to assure maxi-
                mum  destruction  efficiency.   A visual estimate  of the material
                properties provided the information needed to estimate furnace
                operation settings.  Therefore,  more  accurate material physical
                properties were  not necessary and were not determined.   The
                estimates presented in  Section 3.0  are the basis  for further
                evaluations of system performance.

                 Composite feed samples  taken during the 30 and  15 minute pri-
                mary chamber residence  time tests were analyzed by Weston
                 (Appendix B) and found  to contain 227 ppb and 156 ppb of
                2,3,7,8-TCDD,  respectively.   The UMC  (Appendix  F) analysis
                yielded a higher concentration of 306 ppb.

                 Since lower concentrations  would require smaller  quantities  of
                dioxin in offgas samples to confirm the 99.9999 % destruction
                efficiency, the  Weston  results were used  by  ERT to  calculate
                the  destruction  efficiencies.  Calculations  based on the UMC
                data would yield slightly higher DRE's than  those noted  in
                 Section 6.4.1.

          6.2.2  Soil Feed Rate

                The  feed rate history for the testing is noted  in the Appendix
                E operating logs, Tables 6-2 and 6-3, and Figures 6-1 and 6-2.
                For  both the 30  and 15  minute primary chamber residence  time
                 conditions, the  plots show a reasonably steady  feed  rate.  The

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            average feed rate for the two tests were 47.7 Ib/hr and 48.1
            Ib/hr, respectively.

6.3  Soil Decontamination

     Procedures and results for discharged soil sample analysis are con-
     tained in Appendix B, and the results  are summarized in Table 6-1.
     The Weston analysis found the samples from the 30 minute and 15 minute
     residence time tests to be free of residual dioxin, to detection
     limits of 38 and 33 parts per trillion (ppt), respectively.  The UMC
     confirmed these results, but to a less rigorous detection limit of 1
     ppb.

     Shirco has determined that disposal of residual material (soil, in
     this case) can be a significant area of operating cost for on-site
     incineration.  In order to minimize this  cost, it is important that
     the residual material be suitable for deli sting as  hazardous waste
     under U.S. EPA regulations 40 CFR 260.20  and 40 CFR 260.22, and for
     inclusion in Appendix XI of 40 CFR 261.

     A delisting petition for residual soil produced by  a similar operation
     was recently approved by U.S. EPA (Reference 3).  The detection limit
     for residual dioxin contained in this petition was  90 ppt, con-
     siderably higher than that used for the test of Shirco's equipment.
     This indicates that residual soil from on-site incineration of dioxin-
     laden soil  is suitable for delisting, provided suitable test data  is
     obtained and the incineration process is  properly maintained and moni-
     tored.   It  should be noted that approval  of  such delisting petitions
     may be denied based on the presence of other hazardous  components  such
     as  Teachable metals.

     These findings show that not only can the Shirco process effectively
     remove 2,3,7,8-TCDD from contaiminated soils,  but that  the  resulting
     residual material can be classified as non-hazardous with  respect  to
     dioxin.  This classification can  reduce the  overall operating  cost for
     on-site  incineration by  simplifying final disposition  of  the  residual
     soil.

 6.4 Stack Emissions/DRE

     6.4.1   2,3,7,8-TCDD

             Analysis  procedures and  results  of stack  emissions  testing  are
             reported  in  Appendices  A and B,  with results summarized in
             Table 6-1.

             The data  for 2,3,7,8-TCDD testing  shows that the required
             99.9999 % ORE was exceeded by an order of magnitude for the 30
             minute residence time test,  and comfortably exceeded for the 15
             minute test.  Actual  DRE's were >99.999996 %, and >99.999989 %,
             respectively.  In Weston's analysis of laboratory procedures
             used in determining expected dioxin quantities in the emissions
             samples,  calculations indicated that detection limits were 14
             picograms and 8.4 picograms.  These detection limits were used
             by ERT in calculating DRE's.

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             These  results  show  that the Shirco process is capable of
             exceeding  the  incinerator performance requirements (ORE) of
             U.S. EPA regulation 40 CFR 264.343(a), for dioxin-bearing
             materials.

      6.4.2   Particulate Emissions

             A  U.S. EPA Modified Method 5 sampling technique was used to
             determine  particulate emissions from the system.  The results
             of  this testing  and subsequent analysis are summarized  in Table
             6-1.

             For the 30 minute residence time test the particulate emissions
             were 0.001 grains/dry standard cubic ft (gr/dscf), and  0.0002
             gr/dscf for the  15  minute residence time test.  These rates are
             well below the 0.08 gr/dscf standard contained in U.S.  EPA
             regulation 40 CFR 264.343(c).

             The inherently low  particulate emissions of the Shirco  infrared
             furnace are graphically demonstrated by these results.  Compli-
             ance with particulate emissions standards has historically been
             a  problem for hazardous waste incinerators processing con-
             taminated soils.  Units using mechanical agitation or induced
             air turbulence to achieve adequate DRE's have significant dif-
             ficulty in complying with such standards.  The emissions levels
             measured during  this test indicate that particulate emissions
             from a Shirco incinerator processing contaminated soils are not
             a  source of concern.

             In addition to simplifying design, operation, and maintenance
             of pollution control equipment, lower particulate emissions
             will also result in significantly smaller amounts of scrubber
             solid residues for  disposal.  It should be noted that the
             delisting concerns  noted in Section 6.3 also apply to scrubber
             residues.

6.5  Scrubber Effluent Analysis

     MDNR secured a scrubber effluent sample during the 15 minute residence
     time emissions test, to determine its dioxin contamination level.  The
     procedures used in the  analysis are presented in the Appendix  B
     report.  The finding was that 2,3,7,8-TCDD was not present to  a detec-
     tion limit of 1 ppb.

     The Reference 2 delisting  petition for the U.S. EPA mobile incinerator
     operation showed that no 2,3,7,8-TCDD was found in scrubber effluent
     to a detection limit of 3.9 ppt, considerably lower than that  used in
     this test.  The ability to delist the scrubber effluent from any unit
     except  the EPA system has  not been demonstrated.  However, the failure
     to find TCDD in the effluent from this test suggests that dioxin is
     not present at a level which would prevent delisting of the effluent,
     with subsequent disposal as a non-hazardous waste.

6.6  Equipment Operation

     The portable pilot set-up, dismantling, and decontamination were
     described in previous sections.  As noted, these activities proceeded

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     smoothly and in a timely manner.  Set-up was completed in six hours.
     The dismantling, decontamination and packing for transport were
     completed in twelve working hours.   With the exception of the blown
     main power breaker fuse, which occurred on July 9, all equipment
     operated without difficulty throughout the test cycle.

6.7  Process Temperatures

     Also presented in the Appendix E operating logs are temperatures in
     the portable pilot system recorded from the control panel digital
     display.  Presented on Figures 6-3, 6-4 and 6-5 are copies of the
     control panel temperature recorder chart for July 9, 10, and 11.  The
     temperatures in primary chamber zone thermocouples Aj and A2, primary
     chamber exhaust, and scrubber stack are recorded.  Errors in the
     signal to the recorder for the thermocouples in primary chamber Zone B
     and the secondary chamber were experienced during this program.  Thus,
     these two temperatures are not recorded; however, the digital readout
     signal was functioning, allowing the operator to make a written
     recording each hour.

     During the 30 minute residence time test performed on July 10 the pri-
     mary chamber was maintained at a nominal temperature of 1560°F in the
     drying/volatilization zone and 1550°F in the volatilization/bakeout
     zone.  The secondary chamber maintained a nominal 2250°F temperature.
     During the 15 minute residence time test on July 11 the primary
     chamber temperture was nominally 60°F lower.  A review of Figure 6-5
     shows the effect of the increasing moisture content of the feed soil
     as the soil  container was emptied.  However, during the emissions
     sampling period for this condition the primary chamber temperture was
     relatively stable at 1490°F in both control zones.  The nominal secon-
     dary chamber temperature was 2235°F.

     Thus, the soil decontamination was accomplished at primary chamber
     temperatures as low as 1490°F and  secondary chamber temperatures bet-
     ween 2200°F  and 2250°F.

6.8  Power Usage

     Input power  to  the  two temperature control  zones  in the  primary  fur-
     nace  chamber was measured  by  totalizers for each  zone.   The  totalizer
     readings were  recorded on  the Appendix E operating  log  at nominal  one
     hour  intervals.  Table 6-4 presents cumulative power  usage as  a  func-
     tion  of  time for each  of  the  three operating days.

     Process  power  consumed  includes  that  required  to  overcome heat  losses
     from  the  furnace  shell.   In  the  pilot  test  unit,  the  heat losses per
     unit  of  effective  belt  surface  area are  substantially greater than for
     a full  scale system,  as  shown in Figure 6-3.   Consequently,  the  speci-
     fic power consumption  data presented  here  for  the portable pilot unit
     should not  be  used  to  estimate  power  required  to  decontaminate  simi-
     liar  soil  in a full-scale system.   This  data  is  presented  here  for
     information purposes  only.

     During the  emissions  test period for  the  30 minute residence time  con-
     dition on July 10,  the primary  chamber power usage rate was  16.7  KW.
     Using the average  soil  feed  rate of  47.7  Ib/hr,  the specific power
     usage was 0.35 KW/lb feed.  During the 15  minute residence  time expo-

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sure, the average power usage rate was 16.9 KW.  For the 48.1 Ib/hr
soil feed rate during this test, the specific power usage  rate was
again 0.35 KW/lb feed.

Both of these test conditions required the use of the maximum power
available in the portable system, since the soil had very  little  heat
value and the feed rate, by design, was the maximum the unit could
process with the available power.

Since contaminated soil will likely have varied, site-specific charac-
teristics, a general estimate of operating power usage with a full-
scale system should not be made from the test data.

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                                          FIGURE 6-3




                          TEMPERATURE RECORDER CHART - JULY 9, 1985
IfOO
1300
0700

-------
                                    FIGURE 6-4
1160
1000
0100
TEMPERATURE RECORDER  CHART
                   0700
JULY 10, 1985
  0600          0500
OtOO

-------
0100
                   	RE
 TEMPERATURE RECORDER CHAR'i - JULY  11,  1985
0100         0700          OtOO          0500

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                                 TABLE 6-1
                             TEST DATA SUMMARY
Date
9/9/85
9/10/85
9/11/85
Test
Condition
1
1
2
Emissions
Test No.
1
2
3
Primary
Chamber
Residence
Time (min)
30
30
15
Average
Soil
Feedrate
(Ib/hr)
30(appr)
47.7
48.1
Nominal Test Temperature
Primary
Chamber
Zone A
1600
1560
1490
Zone 8
1580
1550
1490
Secondary
Chamber
2300
2250
2235
                              Table 6-1, Cont.
Emissions
Test No.
1
2
3
Average
Primary
Power Usage
(kw/lb feed)
-
0.35
0.35
Average
Secondary
Energy Usage
(BTU/lb feed
-
2850
2900
Feed Soil
Dioxin Level
(ppb)
N/A
227
156
Emissions
Destruction
Efficiency
(%)
N/A
99.999996
99.999989
Participate
Emissions
(gr/dscf)
N/A
0.001
0.0002
                               Table  6-1,  Cont.
Emissions
Test No.
1


2
Discharged Soil  Dioxin Level
   (parts per trillion)
                        N/A
                        <38
                        <33
                                           Scrubber Effluent Dioxin  Level
                                               (parts  per  billion)
                                            N/A
                                            N/A

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                                   TABLE 6-2

                              FURNACE FEED HISTORY

                            30 MINUTE RESIDENCE TIME

                                 July 10, 1985
Time
0720
0810
0932
1020
1053
1134
Unk
1248
1335
1412
1517
1559
1632
Weight Feed
(lb)
35
33.3
31
31.75
33.5
30
32.5
33.75
33.5
33.25
38
32.25
35.25
Cumulative Feed
(lb)
35
68.3
99.3
131.05
164.55
194.55
227.05
260.8
294.3
327.55
365.55
397.8
433.05
NOTE:  Based on this table and Figure 6-1, a total of 333.75 pounds of material
       were fed between 0932 hrs and shutdown at 1716 hrs.  The average feed
       rate during this period was 47.7 Ib/hr.  The emissions sampling tests
       were conducted between 1016 and 1720.

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                                   TABLE  6-3
                              FURNACE  FEED HISTORY
                            15 MINUTE  RESIDENCE  TIME
                                 July  11, 1985
Time
0904
1009
1055
1141
1231
Weight Feed
Mb)
55*
44.25**
37.75
37.15
39
Cumulative Feed
(lb)
55
99.25
137
174.15
213.15
NOTES:  *  Material  containing 117 ppb of 2,3,7,8-TCDD
        ** Material  containind 260 ppb of 2,3,7,8-TCDD (fed for remainder of
           testing)
           Emissions testing conducted between 1009 hrs and 1231 hrs.

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         TABLE 6-4





OPERATING POWER CONSUMPTION



        July 9, 1985
Time of Day

0900
1045
1145
1230
1315
1405
0610
0730
0810
8646
0940
1020
1100
1130
1230
1330
1440
1535
1630
1730
Cumulative Time
(hrs)

. 0
1.75
2.75
3.50
4.25
5.05
__-______-_._-_.. Inl v 1
0
1.33
2.00
2.60
3.50
4.17
4.83
5.33
6.33
7.33
8.50
9.42
10.34
11.34
Cumulative Power Usage
Zone A
Q 1QRR_._-_-
.0
14.9
24.0
28.3
33.8
40.3
01 QftR..-.-.
0
11.7
18.2
23.7
31.6
38.0
4.0
48.3
57.1
66.2
76.7
85.2
93.3
104.9
Zone B

0
14.5
22.6
27.0
33.2
40.1
0
10.2
15.9
20.7
27.5
33.0
38.2
41.9
49.6
57.4
6.55
73.8
80.8
90.9
Total

.0
29.4
46.6
55.3
67.0
80.4
0
21.9
34.1
44.4
59.1
71.0
82.2
90.2
106.7
123.6
143.2
159.0
174.1
195.8

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TABLE 6-4, CONTINUED
Time of Day

0810
0905
1030
1135
1205
1231
Cumulative Time
(hrs)

0
.92
2.33
3.42
3.92
4.3
Cumulative Power Usage
Zone A
Ul QRti_____
0
8.2
21.2
30.9
35.9
39.6
Zone B

0
7.2
18.6
26.7
31.1
34.3
Total

0
15.4
39.8
57.6
67.0
73.9

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7.0  REFERENCES

     1.  NIOSH Current Intelligence  Bulletin  40,  "2,3,7,8 Tetrachlorodibenzo-p-
         dioxin (TCDD, "dioxin")", U.S.  Department  of Health  and Human Services,
         January 23,  1984.

     2.  Federal Register,  Volume  50,  Number  108, pages  23721-23728, "Hazardous
         Waste Management System;  Identification  and Listing  of Hazardous
         Waste", U.S.  Government Printing  Office, June 5, 1985.

     3.  Federal Register,  Volume  50,  Number  143, pages  30271-30274, "Identifi-
         cation and Listing of  Hazardous Waste; Mobile Incineration System",
         U.S.  Government Printing  Office,  July 25,  1985.

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         APPENDIX  A
ERT EMISSIONS SAMPLING REPORT

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 Document C-S044
 January 1986
                 Final Report
      Thermal Destruction of
   Dioxin Contaminated Soils
 Employing a Shirco-Infrared
      Incinerator Pilot Unit -
   The Times Beach, Missouri
         Monitoring Program
EBT
A RESOURCE ENGINEERING COMPANY

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                            TABLE  OF  CONTENTS
                                                                Page
1.   INTRODUCTION                                               1-1
2.   SUMMARY OF RESULTS                                         2-1
3.   FIELD SAMPLING PROGRAM                                     3-1
4.   LABORATORY ANALYSIS                                        4-1
5.   QUALITY CONTROL PROTOCOLS                                  5-1

APPENDIX A       FIELD CALIBRATION DATA
APPENDIX B       ROY F. WESTON ANALYTICAL PROGRAM-
                 ANALYSIS OF COMBUSTION PRODUCTS FOR
                 2,3,7,8-TETRACHLORODIBENZODIOXIN (TCDD)
APPENDIX C       TECHNICAL WORK SCOPE FOR THE ANALYTICAL
                 PROGRAM PROVIDED TO ROY F. WESTON BY ERT
APPENDIX D       DRAFT ASME SAMPLING PROTOCOL

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                            1.   INTRODUCTION

     Environmental Research & Technology, Inc. (ERT) of Concord,
Massachusetts and Shirco Infrared Systems of Dallas, Texas jointly
sponsored an incineration test program at the Dioxin Research Facility
located in Times Beach, Missouri on July 10 and 11, 1985.  The test
program was conducted using a Shirco pilot mobile incinerator for the
thermal treatment of a dioxin contaminated soil feed.  The primary
objective of this test program was to provide a preliminary evaluation
of the Shirco Infrared Technology for use in the thermal
decontamination of dioxin contaminated soils.
     The actual demonstration program consisted of two test runs while
the pilot incinerator was treating Times Beach soil contaminated with
approximately 200 ppb of 2,3,7,8-tetrachlorodibenzo dioxin.  Sampling
of the requisite influent and effluent test streams was performed by
ERT personnel.  During each of the two test series, samples were
collected from each of four process streams as follows:  contaminated
soil feed, incinerator ash (treated soil), flue gas (combined
vapor/particulate) and scrubber slurry.  Laboratory analyses of the
requisite samples for 2,3,7,3-TCDD were performed by .Roy F. Weston of
Westchester, PA employing a tandem GC/MS/MS system situated in the
vicinity of the Times Beach site.
     The report to follow, which was prepared by ERT, addresses the
critical features of the incinerator monitoring program itself.  A
summary of the pertinent sampling and analysis procedures are
contained in Sections 3 and 4,  respectively.  Calibration data
pertinent to the field sampling activities are provided in
Appendix A.   The complete text of the analytical report provided to
ERT by Roy F.  Weston is provided in Appendix B.  These analyses were
conducted in accordance with technical specifications contained in the
ERT scope of work provided in Appendix C.  A summary of the quality
control features of the monitoring program are contained in
section 5.  A summary of results for each of the two test series
including the calculated destruction/removal efficiencies for
2,3,7,8-TCDD are provided in Section 6.
                                   1-1
6956P C-3044-A

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                         2.  SUMMARY OF RESULTS

     The presentation to follow contains a summary of-2,3,7,8-TCDD
test data provided to ERT by R.F. Weston and the University of
Missouri as well as pertinent field data collected during each of
ERT's field test series.
     Analytical test results for each of the requisite sample matrices
are provided in Table 2-1.  While results are provided for TCDD only,
it has been assumed for the purposes of this test program that all of
the TCDD is present as the 2,3,7,8-TCDD analogue.  As shown no
2,3,7,8-TCDD was detected in the treated soil from either test run at
levels ranging from 0.033 ppb to 0.038 ppb.  Similarly, no
2,3,7,8-TCDD was detected in the flue gas from either test series at
conci
Pg).
concentrations ranging from 0.002 ug/m  (14 pg)to 0.003 ug/m  (8.4
     These data in conjunction with pertinent waste feed and stack
flow rates were used to derive destruction and removal efficiency data
for each of the two test series.  These calculations, as shown in
Table 2-2, are in excess of the 99.9999% criteria stipulated by the
Environmental Protection Agency for the effective decontamination of
dioxin contaminated soils.
     A summary of physical and chemical parameters monitored during
each of the two test series are contained in Table 2-3.  These data
include critical physical features of the flue gas sampling system as
well as physical and chemical characteristics of the flue gas, itself.
     Particulate emissions data (grain loadings) for each of the two
test series are also provided in Table 2-3.  It should be noted that
the particulate emission results presented in this table represent
loadings from only the filter samples from each of the test runs.  Due
to an oversight, gravimetric determinations were not conducted on the
particulates rinses prior to organic extraction, rather each dried
probe rinse was submitted directly in combination with the
corresponding particulate filter for extraction and eventual TCDD
analyses.  We contend that the mass of particulate matter associated
with these sample would in no way be sufficient to effect the units
compliance status with the incinerator performance status of 0.08
gr/dscf
1429J C-3044                         2-1

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                                     TABLE  2-2
                        DESTRUCTION AND REMOVAL EFFICIENCY
                           CALCULATIONS FOR 2,3,7,8-TCDD
                                                             Test Series
     Parameter

Waste feed concentration
Waste feed rate
Mass rate in

Pollutant mass out
Flue gas concentration
Mass rate out

Destruction and removal efficiency
EPA Destruction and removal efficiency
Performance standard
Units
2A
3A
ug/kg
Ib/hr
ug/hr
P8
ug/m
ug/hr
percent
percent
227
47.67
4908
<14
<2xlO"6
<1.93xlO~4
>99. 999996
99.9999
156
48.12
3405
<8
<3xlO~6
<3.59xlO~4
>99. 999989
99.9999
                                          2-3

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                                         ,,            PHYSICAL A"° CHEMICAL CHARACTERISTICS
                                   THE FLUE GAS AND THE SAMPLE COLLECTION  SYSTEM
        RESULTS OF FLOWRATE AND  IBOKINETIC CALCULATION

        RUN NUMBER                                     «•*«••
        DATE OF RUN                                    *•»•••
        CLOCK TIMEt INITIAL                            **•»»»
        CLOCK TIMEl FINAL                              «•»»«*
K>
AVG. STACK TEMPERATURE
AVG. SQUARE DELTA P
NOZZLE DIAMETER
BAROMETRIC PRESSURE
SAMPLING TIME
SAMPLE VOLUME
AVG. METER TEMP.
AVG. DELTA H
DGM CALIB. FACTOR CY1
WATER COLLECTED
CO 2
O 2
CO
N 2
STACK AREA
STATIC PRESSURE
PI TOT COEFFICIENT
SAMPLE VOLUME DRY
WATER AT STD.
MOISTURE
MOLE FRACTION DRY GAS
MOLECULAR WT.DRY
EXCESS AIR
MOLECULAR WT. WET
STACK GAS PRESSURE
STACK VELOCITY
VOLUMETRIC FLOWRATE, DRY STD.
VOLUMETRIC FLOWRATE, ACTUAL
ISOKINETIC RATIO
  DEGREES F
  INCHES H2O
    INCHES
   IN. HG.
     MIN.
  CUBIC FEET
  DEGREES F
   IN. H20
    «••«•*
  MILLITERS
   PERCENT
   PERCENT
   PERCENT
   PERCENT
SQUARE INCHES
  INCHES WG.
    *••*••
     DSCF
     SCF
   PERCENT
    *»••**
  LB/LB MOLE
   PERCENT
  LB/LB MOLE
  INCHES HG.
     AFPM
    DSCFM
     ACFM
   PERCENT
    2A
IOJULBS
   1011
   1711

  167.0
    O.6
    0.3
   30.0
  3B9.O
  268.0
  116.0
    1.5
    1.0
 2871.O
    3.8
   14.4
    0.0
   81.8
    7.1
    0.4
    0.8
  249.5
  135.4
   35.2
    O. 6
   29.2
  200.1
   25.2
   30.0
 2129.5
   57.2
  IO4.6
  105.0
   3A
11JUL85
   1O59
   132O

  169.0
    0.7
    0.3
   29.9
  130.0
  114.5
  11O.O
    2.5
    1.0
 1263.4
    3.0
   1O.O
    O.O
   87. O
    7.1
    0.4
    O.8
  1O7.5
   59.6
   35.7
    O.6
   28.9
   77. 1
   25.0
   29.9
 2889.7
   76.5
  141.9
  101.2
        CALCULATIONS FOR BRAIN LOADING AND EMISSION RATES
        FRONT HALF TOTAL (Filter Only)
        PAR1'CUt-ATE
        • A    ULA1E AT 7 7. O2 
-------
                                TABLE 2-1
                   SUMMARY OF RESULTS - TCDDC  ANALYSES
Sample Stream                TCDD
Waste Feed (ng/g)a
     Run 2                   227
     Run 3                   156

Incinerator Ash/Treated
       Soil(ng/g)a
     Run 2                    <0.038
     Run 3                    <0.033
Scrubber Effluent (ug/1)
     Run 2
     Run 3
Flue Gas (Total pg)
     Run 2                   <14
     Run 3                    <8.4
Field Biased Blank           <22
 Analyses conducted by Roy F. Weston at their Times Beach laboratory
b
 Analyses conducted by the University of Missouri.
 Assumed to be the concentration of the 2,3,7,8-TCDD analogue
reported as total TCDD.
                                     2-2

-------
                       3.  FIELD SAMPLING PROGRAM

     As discussed previously samples were collected from each of four
incinerator influent/effluent streams during each of the two test
series.  These included the following types of samples:  flue
gas/waste feed, incinerator ash and scrubber effluent.  Additional
details pertinent to the collection of each of the four matrices are
provided below.

     Waste Feed

     Samples of the contaminated Times Beach soil were collected from
the feed hopper to the incinerator in conjunction with each of the
test runs.  Three to four grab samples were collected during each run
and composited to a single sample in a pre-cleaned 1000 ml amber glass
container for subsequent analysis.

     Incinerator Ash

     Samples of incinerator ash were collected during the course of
each test run by means of an access port located in the ash hopper.
Four to five grab samples were collected during each run and
composited to a single sample in a pre-cleaned 1000 ml amber glass
container for subsequent analysis.

     Scrubber Effluent

     Samples of the scrubber effluent water were collected at 30
minute intervals throughout each test run.  The samples from the
recirculating system were collected from the blowdown tank and
composited to provide a single, one liter sample for each run.
1375J C3044-A

-------
      Flue  Gas Sampling

      A modified U.S. EPA Method 5 sampling train was us.ed to quantify
particulate and semi-volatile emissions from the unit.  A schematic of
the sampling train used is presented in Figure 3-1.
      In accordance with the specifications of EPA Method 5 and the
ASME  dioxin protocol contained in Appendix D, flue gas samples were
collected  isokinetically using a single sampling point placed in the 3
inch  stack.  In addition full system leak checks of the sampling train
were  performed prior to and at the completion of each test series.
Stack velocity and cyclonic flow check measurements were also taken
just  prior to the commencement of each test series.
      The sample train consisted of a glass-lined heat-traced probe
with  a stainless steel button hook nozzle and attached thermocouple
and pitot tubes.  After the probe, the gas passed through a heated
glass fiber filter (Reeve Angel 934 AH filter paper).  Downstream of
the heated filter, the sample gas passed through a water-cooled
module, then through a sorbent module that contained approximately 25
grams of XAD-2 resin.  The XAD module was followed by a series of four
impingers.  The first impinger, acting as a condensate reservoir
connected to the outlet of the XAD module, was modified to have a
short stem so that sample gas would not bubble through the collected
condensate.  The second and third impingers each contained 100 ml of
1.0 NaOH water for the collection of HCl followed by a pump, dry gas
meter, and a calibrated orifice.
     At the conclusion of each of the test runs, the sample train was
removed to a designated clean area for sample recovery activities.
(This consisted of an organic free recovery trailer provided by the
Missouri Department of Natural Resources).
     The particulate filter was removed from its housing and
transferred to its original glass petri dish.  The container was
sealed with Teflon tape and labeled as: -M5/FF.  Run number precedes
all sample codes (e.g., 1-M5/PF).
     The front half of the sampling train was rinsed three times with
1:1 methylene chloride and acetone.  The rinse was recovered into an
amber glass container and labeled as: -M5/FH.
1375J C3044-A                      3_2

-------
                  Rccirculation Pump
                             Tharmomatart
 Tamparatura
  Probe
Ravarsa Type
 Pitot Tub*
                                                                            Vacuum Line
                              Dry Gas Matar
Air Tight
 Pump
                                                                 IMPINGERS
                                                                 1  CondartMta Trap (Empty)
                                                                 2 1NN«OH|100ml)
                                                                 3 INNaOHdOOml)
                                                                 4 Silica Gal
    *First impinger which serves  as condensate crap  has a very short
     stem that does not  extend  into the condensate.
     Figure  3-1  Schematic of the  Modified Method 5 Train Employed  for
                  Flue  Gas Sampling During the  Times Beach Demonstration
                  Program.
                                          3-3

-------
      The  volume  of  condensate collected in the first impinger was
measured  in  a pre-cleaned glass graduated cylinder and transferred to
an  amber  glass bottle.  The sample was then preserved by adding a
predetermined amount  of methylene chloride (30% of the total sample
volume).  A  methylene chloride rinse of the condensing coil and
impinger  were also  added to the sample which was then labeled as
-MS/CD.
      The  sorbent trap containing the XAD-2 resin was sealed using
ground glass fittings and labeled as: -M5/XR.  The volume of water
collected in the second and third impingers and weight gain of the
desiccant contained in the final impinger were determined and recorded.
      All  containers were inspected to ensure integrity of the samples
and logged on chain of custody tracking sheets.
      The  number and type of samples collected during the field program
are listed in Table 3-1.
      Copies  of all  calibration and field data sheets are presented in
Appendix  A.

      Combustion Gas Analysis - ORSAT Measurements

      Combustion gas measurements for CO., O  and CO were taken
during each  of the  two test series.  These measurements were conducted
in accordance with  EPA Method 3 employing an ORSAT.  (Federal Register
40 CFR Part  60 Appendix A July 1, 1985).
1375J C3044-A                      ,  .
                                   3-4

-------
                                                              TABLE  3-1
                                   SAMPLES COLLECTED DURING THE TIMES BEACH DEMONSTRATION PROGRAM
                             Sample Type
                               Source
                         Number
                       Collected
               Container Type
Modified Method 5 train
Particulate filter
Particulate rinses (Probe)
XAD-2 resin
Condensate catch
Impinger catch (IN NaOH)
Solvent rinses of train
(methylene chloride/acetone)
Train
Train - Front half rinse
XAD-2 tube
First impInger
Second/third impingers
Back-half rinse
2
2
2
2
2
2
2
Glass petri dish
500 mL amber glass
Glass sorbent trap
500 mL amber glass
500 mL amber glass
500 mL amber glass
500 mL amber glass
Method blanks
XAD-2 resin blank
Filter lot blank
Methylene chloride blank
Acetone blank
Impinger water blank

IN NaOH
XAD-2 lot
Filter lot
CH2C12 lot
Acetone lot
Organic- free
  laboratory water
NaOH lot
1
1
1
1
1
1
1
Glass sorbent trap
Glass petri dish
500 mL amber glass
500 mL amber glass
500 mL amber glass
500 mL amber glass
500 mL amber glass
Other
Contaminated soil feed
Incinerator Ash
Scrubber effluent
Waste feed hopper           6-8
Access Port-Ash Hopper      8-10
Slowdown tank               6
                                                                                                       1000 mL amber glass
                                                                                                       1000 mL amber glass
                                                                                                       1000 mL amber glass

-------
                         4.   LABORATORY ANALYSIS

     As discussed previously, samples from each of the two test series
were transferred to Weston's Times Beach Laboratory for the analysis
of 2,3,7,8-tetrachlorodibenzodioxin.  The requisite analyses were
performed using the rapid method developed by Weston employing a gas
chromatograph coupled with tandem mass spectrometry (GC/MS/MS).
     The analytical methodology employed by Weston has been accepted
by the EPA for use in performing TCDD analyses of Times Beach soil in
support of an existing contract at the site.  The current version of
the analytical protocol is presented as part of the Weston Report for
this test program which is provided in Appendix B.  Certain deviations
from the analytical protocol have been used in order to accommodate
the nature of the collected samples.  Sample preparative procedures
peculiar to this test program, and not contained in Appendix B, are
described 'below.

     Solid Samples

     The analytical methodology for the feed stock and ash samples is
as described in the EPA method.

     Flue Gas Samples

     The sampling train was received in the form of four different
samples consisting of a condensate sample, front half rinse, a
particulate filter, and an XAD-2 trap.  While we were interested in
determining the total amount of TCDD in the train, the four components
needed to be prepared separately.  The treatment of each is described
below.

     a.   Condensate Sample

     The condensate was placed in a separatory funnel and extracted
three times with 100 mL of dichloromethane by shaking the mixture and
allowing the phases to separate.  The dichloromethane phase from each
of the extractions was filtered through anhydrous sodium sulfate into

1377J C3044-A

-------
a beaker.  The combined condensate extract was evaporated gently on a
hot plate maintained at a low heat with a stream of nitrogen.  When
the volume of extract solution was approximately 10 mL", the beaker was
removed from the hot plate, and the solution retained until the
corresponding extracts from the same train were available.

     b.   Particulate Filter Sample

     Initial gravimetric determinations were conducted on the
particulate filters in accordance with the requirements of US EPA
Reference Method 5.
     The particulate filter was cut into pieces and placed in an
extraction jar.  Approximately 100 mL of acetonitrile-dichloromethane
(2:1 by volume) were added, and a magnetic stirring bar was placed in
the jar.  The sample was continuously stirred for about 2 hours.
     At the end of the extraction period, the solvent was passed
through a filter into a separatory funnel and 900 mL of distilled
water were added.  The mixture was shaken to transfer the acetonitrile
from the organic phase into the aqueous phase.  The layers were
allowed to separate, and the dichloromethane layer was passed through
anhydrous sodium sulfate into the same beaker containing the extracts
from the condensate and front half rinse samples.  The solution was
concentrated to a volume of about 10 mL.

     c.   Front Half Rinse Sample

     The front half rinse was added to a separatory funnel containing
approximately the same volume of water as the volume of the rinse.
The mixture was allowed to separate, and the lower phase removed.  The
aqueous upper phase was discarded.
     The process was repeated, taking the retained lower phase and
adding  it to water so that the water soluble portion of the solvent
could be removed.
 1377J  C3044-A                        4~2

-------
     The organic phase was passed through anhydrous sodium sulfate
into the same beaker containing the condensate extract.   The solvent
was evaporated on a hot plate with a stream of nitrogen, until the
final volume of solution was about 10 mL.

     d.   XAD-2 Trap Sample

     The resin was transferred into an Erlenmeyer flask and was spiked
with 10 uL of the spiking mixture containing 0.5 ng/uL of the internal
standard and 0.1 ng/uL of the surrogate compound.
     The spiked resin was treated with 100 mL toluene and placed on a
stirring hot plate.  The mixture was stirred and heated for two
hours.  At the end of the extraction time, the solution was filtered
while still hot into the beaker containing the extracts from the other
portions of the sampling train.  The mixture was gently evaporated to
dryness using heat and under a flow of nitrogen gas.              '
     The combined extract was redissolved in about 10 mL of
dichloromethane and the solution was transferred into a vial.  The
solvent was exchanged to cyclohexane following the procedures
described in Appendix B.  The extract was taken through both clean-up
steps described in the Appendix.  After the second clean-up step, the
extract was concentrated to a final volume of 100 uL.  Attempts to
concentrate it further proved unsuccessful, since the solution became
rather viscous.
     The extract was then ready for GC/MS/MS analysis as described in
the EPA methodology contained in Appendix B.

     Scrubber Effluent Samples

     The analysis of the scrubber effluent samples was conducted by
the University of Missouri.  Documentation pertinent to these analyses
is presented in the companion document to this report. Final Report.
On-site Incineration Testing of the Shirco Portable Pilot Test Unit.
Times Beach. Missouri. Shirco Report No. 815-85-2, Nov. 1A, 1985.
1377J C3044-A
                                   4-3

-------
                       5.  QUALITY CONTROL PROTOCOLS

       Quality control protocols  for  this program included a number of
  control elements common to  flue gas monitoring programs for trace
  organic constituents.   These  included quality control  measures
  associated with both the field  sample collection activities conducted
  by ERT, as well as the  analytical measurements performed by Roy F.  Weston.
  Further details on some of  the  more prominent features of the quality
  control program are provided  in the discussion to follow.

       Chain-of-Custody

       Samples were collected on  July 10 and  11, 1985  and transferred
  under Chain-of-Custody  to Roy F. Weston's Times Beach  laboratory on
  July 12, 1985.   A copy  of this  chain-of-custody documentation is
  provided in Appendix B  of this  report.

       Field Sampling Activities

       The sampling methodology and associated quality control protocols
v for the collection of the flue  gas  samples  were consistent with those
  contained in the ASME methodology entitled  Sampling  for the
  Determination of Chlorinated  Organic Compounds in Stack Emissions
  (Draft EPA 450/4-84-014c).
       This approach is presently in  use for  source sampling of Tier 4
  combustion sources in support of EPA's National Dioxin Study.  A copy
  of this protocol (Draft) is provided in Appendix D of  this report.
       Quality control measures prescribed in the ASME methodology and
  incorporated into ERT's field sampling program included but were not
  limited to the following:  replicate trains, field blanks, method
  blanks, XAD-2 sorbent pretreatment  and QC acceptance criteria, and
  sampling train leak check procedures.  For  example a complete sampling
  train was assembled and dismantled  in the field during the test
  program to serve as a field biased  blank.   The components of this
  sample train accompanied the  actual sample  set during  storage and
                                    5-1
  1433J-C3044-A

-------
 transport  to  Roy F. Weston's  laboratory.  The analytical results for
 this  field biased  blank  train are contained in Appendix B of this
 report.

      Analytical Measurements

      Quality  control features of the analytical program were
 consistent with the EPA  dioxin methodology employed by Roy F. Weston
 at their Times Beach laboratory.  Actual QA/QC features of the
 analytical program were  implemented in accordance with the EPA
 methodology  contained in Appendix B of this report as well as
 requirements  of the ERT  Work  Scope provided to Roy F. Weston at the
 outset of  the program.   (A copy of these specifications are provided
 in Appendix C of this report).  These included but were not limited to
 the following types of quality control measures:  performance check
 samples, replicate analyses,  and the use of isotopically labeled
 surrogate  compounds placed in each program sample.
      Further  details on  each  of these quality control elements is
 provided in the discussion to follow.  This includes a summary and
 evaluation-of each data  category.  The data evaluation will also
 discuss any perceived anomalies in the quality of the reported data.

      Matrix Spikes

      Results  are provided for a single soil sample spiked with a 1 ppb
 spike of native TCOO (assumed to be 2,3.7,8 TCOD or 1,2,3,4 TCDD).  A
 recovery of 99.0%  (0.99  ppb)  was reported.  This value is consistent
with performance criteria contained in the EPA protocol.

     Replicate Analyses

     No results are provided  for replicate analyses of any of the
media.  It  can only be assumed that sample replicate analyses were not
performed  as part  of the quality assurance protocol.  It appears,
however, that mandatory  replicate analyses are not a provision of the
EPA TCDD protocol used by Weston in the analyses of the ERT/Shirco
samples.
                                  5-2
1433J-C3044-A

-------
     Surrogate Spikes

     Surrogate data contained in the Western report (Appendix B pg.  8)
satisfy all of the requisites specified in the Scope of Work provided
                                                             37
to them by ERT with two exceptions.  The % recovery data for   Cl
- 2,3,7,8 TCDD contained in the report for both the ash samples and
the flue gas samples are in compliance with the acceptance criteria
provided by EPA as part of their TCOD protocol.  Surrogate recovery
data for the two ash samples ranged from 92-109%, while recovery data
for the three flue gas samples ranged from 99-105%.  All of these data
are within the acceptance range provided by EPA as part of the TCDD
protocol (60-140%).
     Surrogate recovery data for the two soil feed samples, however,
were well beyond the upper acceptance limit specified in the
protocols.  Recovery values of 473.9% and 378% were reported (pg.8)
for Runs 2 and 3, respectively.  Despite the 4x (four times)
enhancement in the expected surrogate recoveries, in our judgement, we
do not feel that the native TCDD data for these samples has been
compromised.
     The apparent enhancement in recovery of the   Cl.  - 2,3,7,8
TCDD isomer was not actually caused by a 4x increase in the amount of
surrogate present, but rather by a signal enhancement for those ions
used to quantitate the surrogate species.  More simply, the presence
of elevated concentrations of native TCDD in the soil feed samples
(156-227 ng/g or ppb) has provided a positive interference to those
ions normally used to quantitate the isotopically labeled surrogate.
The EPA TCDD protocol employed by Weston in fact contains the
following excerpt pertinent to this issue:
     [Native 2,3,7,8-TCDD contains an innate quantity of 3 C14 -
2,3,7,8-TCDD.*  Except at high concentrations of native 2,3,7,8-TCDD,
this contribution  is too small to significantly affect the calculated
concentration of surrogate   Cl -2,3,7,8-TCDD.  The theoretical
correction  is calculable on the basis of isotope distribution and
^Naturally occurring elemental chlorine is comprised of both
  1?C135  (75.53%)  and 17C137  (24.47%).
                                   5-3
1433J-C3044-A

-------
 amounts to 1.08% of the m/z 257 peak.  (This correction should be
 checked at low resolution by analyzing about 200 pg/ul of unlabeled
 2,3, 7 ,8-TCDD. )  On this basis, the correction to the area count of the
 surrogate, is made as follows:]
     A263 = A263 - 0.0108
     Calculate the analytical percent recovery of the surrogate
     standard.
     Surrogate             amount measured (nanograms) x 100
     Analytical       =                   5 ng
     Percent Recovery

In any case, it should be emphasized that this anomaly has not
comprised the data reported for native TCDD in each of the two feed
samples.  In fact, TCDD values of 227 ppb and 150 ppb reported for
Runs 2 and 3, respectively  are corroborated by results provided by
the State of Missouri.  The latter analyses conducted on replicate
aliquots of the ERT incinerator feed samples were in fact somewhat
higher than the values reported by Weston in this report.  Hence, the
Weston data can be construed as providing a more conservative estimate
of the TCDD destruction efficiency (%) achieved by the Shirco Infrared
incinerator.

     Calibration Data (GC/MS/MS)

     As specified in the EPA TCDD protocol, results are provided for
both a daily calibration check sample (pg.9, Table 4) as well as a
3-point standing calibration curve (pg.  4, Table 1).  All of the
response factors provided here are within the prescribed acceptance
range of 1.630-1.993.  Furthermore, the instrument calibration checks,
as stipulated by the EPA dioxin methodology, were run within the
8-hour elapsed time criteria between actual samples and calibrant.
The samples themselves were run early in the morning of August 6 ,
1985, while the requisite system calibrants were run late on August 5.
                                   5-4
1433J-C3044-A

-------
     Additionally, copies of the computer derived quantitation reports
are provided in Appendix B.  Data pertinent to the generation of the
August 03 standing calibration curve including response factor data
are provided in Table 1 (pg.4) of the Weston report.  In general, the
calibration documentation are presented in accordance with the data
reporting requirements of the EPA protocol.  A copy of these data
reporting requirements are provided in Appendix B of this report.
     Further details including documentation pertinent to the above
categories of quality control data are contained in Roy F. Weston's
analytical report provided in Appendix B.  The reader is referred to
this document for other critical QC features of the TCDD analytical
program not addressed in the preceding discussion.
                                   5-5
 1433J-C3044-A

-------
                               APPENDIX A
                         FIELD CALIBRATION DATA

               1.  Run Data Forms - Particulate Test Field
                   Data Sheets
               2.  Temperature Sensor Calibration Form
               3.  Dry Gas Meter Calibration Data
               4.  Pitot Tube Calibration Data
1430J C3044-A

-------
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-------
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-------
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-------
           APPENDIX  B
WESTON LABORATORY ANALYSIS REPORT

-------
           7720 LORRAINE AVENUE
           SUITE »102
           STOCKTON. CA 95210
           PHONE (209) 957-3405
  ANALYSIS  OF COMBUSTION PRODUCTS FOR

2, 3, 7, 8-TETRACHLORODIBENZODIOXIN  (TCDD)

-------
ANALYSIS OF COMBUSTION PRODUCTS FOR 2,3,7,8-TETRACHLORCDIBENZODIOXIN (TCDD)


1.0   INTRODUCTION

      In support of Shirco Infrared Systarts, WESTON undertook to perform ana-
lyses of samples collected during a demonstration of a combustion system for
the destruction of 2,3,7,8-tetrachlorodibenzodioxin (TCDD).  The analyses
were performed using the rapid method developed by WESTON and which employs
gas chromatography coupled with tandem mass spectrcmetry.

      The analytical methodology has been accepted by the EPA and the current
version of the analytical protocol is presented in Appendix A.  Certain
deviations from the analytical protocol have been used in order to accommodate
the nature of the collected samples.  A discussion of the deviations will be
presented in Section 3.0.

      The results of the analyses for two runs are summarized below:

      Component                 	TCDD Found	
                                   Run 2           Run 3
      Feed                       227 ng/g        156 ng/g
      Sampling train  (Composite) <14 pg  (total) 
-------
       The sampling  train was received in the form of four different
 samples consisting  of a corelensate sample, front half rinse, a particulate
 filter, aid an XAD-2 trap.  While we were interested in determining the
 total amount of TCDD in the train, the four components needed to be
 treated separately.  The treatment of each is described below.

       a.    Condensate Sample

            The condensate was placed in a separatory funnel and extracted
 three times with  100 ml of dichloromethane by shaking the mixture and
 allowing the phases to separate.  The dichloromethane phase from each
 of  the extractions was filtered through anhydrous sodium sulfate into
 a beaker.'  The combined condensate extract was evaporated gently on a
 hot plate maintained at a low heat with a stream of nitrogen to help
 remove the vapors.  When the volume of extract solution was approximately
 10  mL,  the beaker was removed from the hot plate, and the solution retained
 until the other extracts from the same train were ready.

      b.    Front  Half Rinse Sample

            The front half rinse was added to a separatory funnel containing
 approximately  the same volume of water as the volume of the rinse.  The
 mixture was allowed to separate, and the lower phase removed.  The aqueous
 upper phase was disposed of.

            The process was repeated, taking the retained lower phase and
 adding *'it to water  so that the water soluble portion of the solvent could
 be  removed.

            The organic phase was passed through anhydrous sodium sulfate
 into  the  same  beaker containing the condensate extract.  The solvent was
 evaporated on  a hot plate with a stream of nitrogen, until  the final volume
 of  solution was about 10 mL.

      c.    Particulate Filter Sample

            The particulate filter was cut into pieces and placed in an
 extraction jar.   Approximately 100 mL of acetonitrile-dichloromethane
 (2:1 by volume) were added, and a magnetic stirring bar was placed in  the
 jar.  The sample  was continuously stirred for about 2 hours.

           At  the end of the extraction period, the solvent was passed
 through a filter  into a separatory funnel and 900 mL of distilled water
were added.  The  mixture was shaken to remove the acetonitrile from the
organic phase  into the aqueous phase.  The layerc were allowed to separate,
and the dichloromethane layer was passed through anhydrous  sodium sulfate
into the  same beaker containing the extracts from the condensate and front
half rinse samples.  The solution was concentrated to a volume of about
10 mL.

-------
      d.   XAD-2 Trap Sample

           The resin was transferred into an Erlenmeyer flask and was
spiked with 10 uL of the spiking mixture containing 0.5 ng/uL of the
internal standard and 0.1 ng/uL of the surrogate compound.  For soils
the amount of spiking mixture that is normally added is 50 uL; however,
it is known that the spiking mixture contains a small amount of native
TCDD.  Because of this, the volume of spiking mixture that was added
was reduced, so that its contribution to any native TCDD would be mini-
mized.

           The spiked resin was treated with 100 ml toluene and placed
on a stirring hot plate.  The mixture was stirred and heated for two
hours.  At the end of the extraction time, the solution was filtered
while still hot into the beaker containing the extracts from the other
portions of the sampling train.  The mixtrue was gently evaporated to
dryness using heat and under a flow of nitrogen gas.

      The combined extract was redissolved in about 10 mL of dichloro-
methane and the solution was transferred into a vial.  The solvent was
exchanged to cyclohexane following the procedures described in Appendix
A.  The extract was taken through both clean-up steps described in the
Appendix.  After the second clean-up step, the extract was concentrated
to a final volume of 100 uL.  Attempts to concentrate it further proved
unsuccessful, since the solution became rather viscous.

      The extract was then ready for GC/ttS/MS analysis as described in
Appendix A.


4.0   RESULTS

      a.   Calibration Curve

           The calibration curve was constructed using EPA supplied mixed
standards.  Each standard solution was prepared as described in the protocol
of Appendix A, then concentrated by a factor of 10.  Two uL injections were
made.  The initial calibration curve associated with these samples was
obtained on August 3, 1985.  The data are shown in Table 1.  The single ion
traces for the four monitored ions are shown in Appendix C.

           Based on the calibration curve, the ratio of the areas for the
ions of native TCDD will be acceptable if it falls in the range 0.861 -
1.053.  The response factor for the native TCDD, RFn, in the daily calib-
ration is acceptable in the range 1.630 - 1.993.

-------
                                               TABLE 1

                                       CALIBRATION CURVE DATA
Filename
AUG0324
AUG0325
AUG0326
Concentration, ng/L
Raw Area Counts
Ratio
RF_
RF0
AUG0327
AUG0328
AUG0329
AUG0330
AUG0331
AUG0332
Native
1
1
1
5
5
5
25
25
25
Surrogate
0.3
0.3
0.3
0.6
0.6
0.6
1.0
1.0
1.0
I.S.
5
5
5
5
5
5
5
5
5
A257
8
9
9


28
24
27


165
181
168


,967
,050
,169


,075
,515
,981


,402
,270
,035


A259
9,345
9,361
10,003
Mean
Standard
29,664
27,144
28,121
Mean
Standard
167,820
186,731
173,355
Mean
Standard
> A263 A268
6,
6,
6,

508 48
150 48
464 51

,865
,753
,300

Deviation
8,
1,
7,

648 33
610 30
233 29

,906
,019
,465

Deviation
16,
18,
16,

274 39
454 41
962 36

,185
,010
,898

Deviation
Overall Mean
Overall Std.
Deviation
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
.9596
.9668
.9166
.9477
.0271
.9464
.9031
.9950
.9482
.0460
.9856
.9708
.9693
.9752
.0090
.9570
.0303
1
1
1
1
0
1
1
1
1
0
1
1
1
1
0
1
0
.8737
.8882
.8686
.8768
.0102
.7029
.7209
.9040
.7759
.1113
.7008
.7947
.8505
.7820
.0757
.8116
.0834
2
2
2
2
0
2
2
1
2
0
1
2
2
2
0
2
0
.1922
.0746
.0733
.1134
.0683
.0634
.0513
.9744
.0297
.0483
.8866
.0510
.0936
.0104
.1093
.0512
.0836

-------
      b.   Blank Response

           The blank response is used to derive the detection limit (L.O.D.)
and the correction factor.  The blank consists of the same spiking mixture
used to introduce the surrogate and internal standard into the samples,  but
this mixture is simply prepared in solution to yield concentrations that
approximate the concentrations of these two compounds in the final extract.

           The need for the measurement of the blank response has arisen
due co the fact that the surrogate compound contains a small amount of
a component normally found as part of the native TCDD, specifically it is
that component which gives rise to the daughter ion of mass 259.  Since
the area of the daughter ion of mass 257 is hardly affected, the average
value of this area has been used in measuring the noise level.

           The raw data and the calculated parameters from the blank res-
ponse are shown in Table 2.  The single ion traces of these data are in
Appendix D.

           Based on the blank response data, the detection limit for a
five gram sample of solid material (soil or ash) is 0.038 ppb.  For samples
the weight of which is different than 5.0 g, the above value must be
multiplied by the factor 5.0/W where W is the actual weight of the sample.

           The calculation of the detection limit in absolute quantity,
needed for the evaluation of the quantity of TCDD in the sampling train,
is more complex.  This is so because the protocol itself is designed to
handle ratios of area counts to internal standard area count, but in
deriving an absolute detection limit, the real quantities injected must be
known.  The following assumptions were made in deriving the absolute
detection limit:

           1.   The instrumental response to 1 pg of native TCDD measured
                as the area of the daughter ion of mass 257 is the same
                as the instrumental response to 1 pg of the internal stan-
                dard measured as the area of the daughter ion of mass 268.

           2.   The detection limit is three times the noise level.

           In preparing to obtain the blank response, the spiked solution
was concentrated by a factor of thirty; hence, the concentration of the
internal standard was 450 pg/uL.  Each injection into the instrument was
of 2 uL; thus introducing  a total of 900 pg of the internal standard.
The mean area count for the ion of mass 268 was 150,000.  Therefore, the
instrumental response is 167 counts/pg.

           The average response for the native ion of mass 257 was 466,
and is assumed to be instrumental noise.  The detection limit is taken
as three times the detection limit, corresponding to an area count of
1398.  Hence, the absolute detection limit is 1398/167 = 8.4 pg.

-------
                                TABLE 2
                          BLANK RESPONSE DATA
Filename
AUG0303
AUG0304
AUG0305
AUG0306
AUG0307
AUG0308
AUG0309
AUG0310
AUG0311
AUG0312
AUG0313
AUG0314
AUG0315
AUG0316
AUG0317
AUG0318
AUG0319
AUG0320
AUG0321
AUG0322
                   Raw Area Counts
RF
B
A257 A259
332
424
518
1,454 1,
0
782 1,
565
0
523
287
244
272 1,
486
803
1,073 1,
354
795 1,
121
0
284
Mean
Standard
93
619
708
063
789
059
851
454
113
619
800
196
667
0
116
329
314
215
100
178

A263
36,480
77,740
63,393
68,709
72,333
75,769
66,324
67,378
70,517
63,532
67,932
61,605
58,429
59,874
62,743
.-61,855
'66,508
61,007
51,336
62,474

A268
81,602
183,842
155,264
166,342
172,757
176,403
161,669
166,685
172,301
154,263
165,791
150,693
148,475
142,669
154,739
151,378
165,254
157,302
123,048
149,615

Deviation
°
2.2352
2.1143
2.0415
2.0653
2.0935
2.1476
2.0512
2.0211
2.0463
2.0592
2.0487
2.0441
1.9676
2.0984
2.0274
2.0431
2.0123
1.9392
2.0860
2.0878
2.0615
0.0627

0.0052
0.0057
0.0079
0.0151
0.0046
0.0104
0.0088
0.0027
0.0037
0.0059
0.0063
0.0097
0.0078
0.0056
0.0141
0.0045
0.0128
0.0021
0.0008
0.0031
0.0068
0.0040

0.0144
0.0157
0.0218
0.0417
0.0127
0.0287
0.0243
0.0075
0.0102
0.0163
0.0174
0.0268
0.0215
0.0155
0.0389
0.0124
0.0353
0.0058
0.0022
0.0086
0.0189
0.0110
C.F.
L.O.D.
             0.0068

             0.0378 ng/g

-------
           In determining the absolute detection limit in each of the
analyzed sampling trains, the actual internal standard recovery must be
known.  It is expected that in the clean-up steps some loss could occur.
Since the extract from each of the trains contains a maximum of 50 pg/uL
of internal standard, and since 2uL are injected, the maximum area for
the ion of mass 268 is 16,700.  Hence, to obtain the detection limit in
each of the measurements, the factor 8.4 must be multiplied by the
ratio 16,700/^258•

      c.   Results of Sample Analysis

           The results of the sample analyses are shown in Table 3.  The
ion traces for the samples are found in Appendix E.

           The surrogate recovery for the feed stocks appears much higher
than is acceptable.  The reason for this phenomenon is that the native
TCDD, containing approximately 1% of the surrogate compound, as calculated
on the basis of isotope distribution in nature, overwhelms the amount
spiked.  Thus, a sample that contains 250 ppb native, when spiked with
1 ppb surrogate, would appear to contain 3.5 ppb surrogate, or 350%
surrogate recovery.  Hence, for high levels of native TCDD in the sample
the surrogate recovery as defined in the protocol is not applicable.

      d.   QA/QC Sample Analysis

           Table 4 shows the daily calibration run for the period of the
sample analysis on August 5-6, 1985.

           Table 5 lists the results for the method blank run for the
same period, and Table 6 shows the results for a 1 ppb spike of native
TCDD into uncontaminated soil.

           The initial traces for these runs are in Appendix F.

      e.   Miscellaneous Measurements

           For the sampling trains, volumes of condsate and weights of
particulate filters were obtained.

Sample Description             Sample No.      Sample Wt., g     Sample Vol., ml

Particulate Filter, Run 2A       E426            0.6712
   (TB-08)
Particulate Filter, Ron 3A       E434            0.6623
   (TB-10)
Particulate Filter, Blank        E437            0.6598
   (TB-09)
Condensate, Run 2A               E424               -                2,570
Condensate, Run 3A               E432               -                  930

-------
Filename
AUG0605
AUG0606
AUG0603
AUG0604
AUG0620
Sample I.D.
Feedstock
Feedstock
Ash Run 2
Ash Run 3
Run 2 (E439)
Run 3 (E440)
(E441)
(E442)
Sample
Wt., g
5.10
5.62
4.96
5.70
Sampling Train Run 2A
TABLE 3
RESULTS OF SAMPLE ANALYSES
Raw Area Counts
A257
2,190,010
2,031,298
277
0
0
A259
2,286,855
2,122,987
661
0
0
A
123
119
59
73
4
263
,131
,297
,262
,943
,166
A268
53,323
65,187
133,176
171,762
10,221
• TCDD
227
156
< 38
< 33
< 14
Units Ratio
ng/g 0.9581
ng/g 0.9568
pg/g
pg/g
pg
(S
Surrogate
Rec., %
473
378
109
92
99
           (E424 +  E425 + E426
           + E427)

AUG0621   Sampling Train Run 3A
           (E432 -I-  E433 + E434
           + E435)

AUG0617   Field Biased Blank
           (E436 +  E437 + E438)
7,093   17,090   <  8.4  pg
2,684    6,214   < 22
P9
                 101
                 105

-------
Filename      Concentration, ng/L
           Native   Surrogate   I.S.
AUG0502       1        0.3
                                              TABLE 4

                                        DAILY CALIBRATION
         Raw Area Counts
                          Ratio
RFV
RFV
 A257
A259     A263     A268
11,092    10,666    9,902   58,520   1.0399   1.8250   2.7917

-------
                                               TABLE 5




                                            METHOD BLANK
Filename

Sample I.D.

Sample
Wt., g


A257
Raw Area
A259
Counts
A263

A268
TCDD

Units

Ratio

Surrogate
Rec., %

AUG0508   Method Blank
5.0
901   1,323  50,142  110,289    <38   pg/g
                                                                                                  115

-------
                                                TABLE 6

                                             SPIKE RECOVERY

          Amount         Sample                                    TCDD           Spike           Surrogate
Filename  Spiked  Units  Wt., g  	Raw Area Counts	   Found  Units  Rec., %  Ratio    Rec.r %
                                  A257    A259    A263     A268

AUG0506    1.0     ppb    5.13   24,486  26,098  60,431  134,139   0.996   ppb    99.6    0.9382    107

-------
    APPENDIX A
ANALYTICAL PROTOCOL

-------
   APPENDIX B
CHAIN OF CUSTODY

-------
Field Sheet and Chain of Custody  Record
CToJJec tor's Name an
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No.
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-------
MISSOURI DEPARTMENT OF-JUOURAL RESOURCES
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Field Sheet and Chain  of Custody Record
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Sample
No.
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   Di vi»lon of-gitv-iT onrogiitaJUguaJi ty
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Description of Shipment No. of Samples &L3
No. of Container
Collected
Date







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AnaJyses Requested
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-------
      APPENDIX  C
CALIBRATION CURVE RAW DATA

-------
                                                              3.400      3.533

                                                                  322 MAX 1200
2.767
            2.980
                     3.888
          3.188
                                         3.288
                    3.380
                                                              3.480
                     3.533
8
                                                                 328 MAX 5480S
2.767
            2.980
3.000
3.100
                                         3.200
3.380     3.400      3.533

           332 MAX 129806
0H
«

SY
Gl
G2
63
Z.767
3-AJG-95
220
0.000
0.000
0.0000
SPF 8.8
DTV 8.880
2.

SE
IT
I_T
DT
GR
ST
T 	 • — • 	 •— •-
900 3.
17:49:27
0
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•ataiataiatak
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0.01
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DIV
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3.100
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0.080
-0.041
0.00
0.00
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IQ
DM1
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3.200
0.0500
1260

-5.00
0. 0080
75.00
-15.00
3.300 3
STEP
TH
MO

CGT
CG
R2
0.2588
158
-1.888

94.9
OFT
-55.88
i •
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PE
TT
FP
MU
DM3
RE3
R3
3.533
8. 88
8.75
-20.00
-3600.0
0QGtdCk
• OI0O0
85.80
-65.00
                                                                    17:49:27
      G2-37.5; DI —1.75; TT-. 75; CG-PR
      320              257
      322              259
      328              263
                       268

-------
        	1 MIMI	TCDD 11X5  C20 SHOT ZERO CflllBRflTTQrO	JQ
 SS        1  ES     176  BO        e  TO      lie  GR     U*F  SE       88
 ni   2S7.ee  re  259.ee  MB   263.ee  m   2&8.ee  SR       as  TI 00:03:06
 FI   32e.ee  FZ  322.ee  F3   328.ee  F4   332.ee  ER       ee  IN    73000
110"3           *            >   >        &2    3 209         3 '-CjS  -^^ MPX 1000
    •^^^^N^
   2.758        2.900     3.888     3.188     3.288     3.300     3.400    3.517
11B*                    2.992       J/Y^*3.186 3.243    3.341   322 Mf* 1088
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   2.75B       2.900     3.000     3. lee    ' 3.200 '  '  3.300  '  ' 3.400    3.517

                                                                328  MftX 37208
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   2.758       2.900     3.000    3.100     3.200     3.388     3.400    3.517
332 MRX 86992
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        328              257
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-------
flUGB318    1 MIMI	TCDD  IIXS  C20 SHOT ZERO CflLIBRflTIONI	^
SS1  ES162   BO        0TO      118  GRUHNP  SE       81
ni   257.ee  M2  25s.ee   MS    263.ee  cvt   26e.ee  SR       ei  TI ee:ez:5B
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2.650 2.900
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MAX 55400

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332 MftX 127792
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2.650 2.800
3-AUG-eS 17:39:53
SY Z20 SE 0
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      320              2S7
      322              259
      328              263
      332              268

-------
              Mini
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                                                                322 MRX 1200
   2.733
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             328 MPX 50406
   2.733

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  2.733
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108.1
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        G2-37.5; DI — 1.75; TT-. 75; CG-PR
        320              257
        322              259
        328              263
                        268
                            PE     0.00
                            TT     0.75
                            FP   -20.00
                            MU  -3600.0
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                            R3   -65.00

                               17:44:49

-------
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322 MAX 1200
                                                        3.300   3.400

                                                      332 MRX 109008
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-55.00
3.3
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130 3.400
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                                                          17:34:01
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    320            257
    322            259
    328            263
    332            268

-------
            1 MIMI _ TCDD  1 1X5  C2B SHOT ZERO CPLIBRflTION] _ IfJ
 SS        1  ES      174  BO        8  TO      110  GR     LNNP  SE       87
 ni   257.ee  M2  259.00  MS    263.ee  m   26e.ee  SR       87  TI 00:33:05
 Fl   32B.ee  F2  322.ee  F3    328.ee  F4   332.00  ER       87  IN    89616
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   2.750        2.900    3.000     3.100     3.200     3.300     3.400     3.517
110-1
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                                                                 328 MfiX 50886
   2.750        2.900    3.000     3.100     3.200     3.300     3.400    3.517
H0-,
                                                                332 MRX 118000
   2.750        2.900    3.000     3.100     3.200     3.300     3.400    3.517

    3-«JG-e5     17:27:48  OP      TVP  MTL  0.0500  STEP 0.25OO PE     O-OB
 SY      220  SE       0  C        10  MCL     126O  TH      ISO TT     O.75
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 G2    e.eee  LT  *«»*»*«  DIV  -0.044  IQ    -5.ee               MU   -3600.0
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                                                                     17:27:40
        G2-37.5;DI—1.75;TT-.75;CG-flR
        32B             257
        322             259
        328             263
        332             268

-------
 PUG0315
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110-j
      j Mlfll	TCDD IIXS  C20 «a-ttj  ?T W
     1  ES      162  BO        0  TO       110  GR
257.OO  M2   259.00  M3   263.00  M4   268.00  SR
320.00  F2   322.00  F3   328.00  F4   332.88  ER
                                                           IH
                                            LNNP  SE       81
                                              81  TI 80:02:58
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                                                   320 MAX
                                                            3.280           3.367
                                                                    322 MBX 1208
   2.650
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                                                    332 MRX  106000
   2.658

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        320              257
        322              259
        328              263
                         268
                                                                   PE     0.O0
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                                                                   FP   -20.00
                                                                   MU  -3600.0
                                                                   DM3  0.8008
                                                                   RE3   85.00
                                                                   R3   -65.00

                                                                       17:22:59

-------
PUGB314    1  Mini _ TCDD 11x5  £20 SHOT 7f"^fl Cft TBRQTION3
                                                            _
SS        1  E5      174  BO        0  TO      110  GR     Lt+f   SE       87
Ml   257.00  M2   259.00  M3   283.00  M4   268.00  SR       87   TI 00:03:06
Fl   320.00  F2   322.00  F3   328.00  F4   332.00  CR       87   IIS      600
                                ^        2-72-     3.303      320««xie

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                                                               328 MAX 44408
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                                                              332 MAX 109392
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                                                                  17:17:23
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      320              257
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      328              263
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-------
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-------
           1 MIHI	TCPP IT/*?  £20 SHOT ZERO CPLIBRflTION]	IB
SS        l  ES178BO        0  TO      110  GRLhT*9  SE89
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-------
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       320              257
       322              259
       328              263
       332              268

-------
            i mm
 SS        1  ES
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             SE       67
         67  TI 00:02:55
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                                                   320 MflK 1000
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                     2.800
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            332 MftX 126000
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             T^P   MTL
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                 1260

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                                                     TH      150
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CGT
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R2
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-55.00
        G2-37.5; DI— 1.75; TT- . 75sCG-PR
        320              257
                         259
                         263
        332              268
                                                  PC     0.00
                                                  TT     0.75
                                                  FP   -20.00
                                                  MU  -3600.0
                                                  DM3  0.0000
                                                  RE3   85.00
                                                  R3   -65.00

                                                     16:55:59

-------
 f*JG0309    1 MIMI
 SS        1  ES
 Ml   257.80  M2
 Fl   328.80  F2
118-3
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                                [QM1
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259.88
322.88
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332.88  ER
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                                  89  TI 88:83:05
                                  89  IN      888
                                       328 MPX 1288
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        320              257
        322              259
        328              263
                         268
                                                                     16:45:32

-------
 PLG030B    1 Mlfll
                          TCDD  11/5  C20 SHOT ZERO CflLIBRflTIONI
                                                                          -ID
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Ml   257.00
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            332 MAX 126688
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SY      220  SE
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                 2.900

                 16:39:10
                        0
          3.000

         OP
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        320              257
        322              259
        328              263
        332              268
                      3.400   3.500

                     PE     0.00
                     TT     0.75
                     FP   -20.00
                     MU  -3600.0
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                     RE3   85.OS
                     R3   -65.00

                        16:39:10

-------
                            TCDD II/*5  C20 SHOT ZERO CflLIBRQTTOm
                                                                           -IH
SS
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     1  ES
257.80  re.
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                                                            328
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        328              263
                         268
                                                                      16:33:45

-------
 &JGSSB&	i  nini
                          TCPD IIX5  C20 SHOT ZERO CflLIBRflTIONl
                                                           -IB
 SS        1
 Ml   257.00
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110-a
ES      178  BO       0  TO
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F2   322.00  F3   328.00  F4
  2.889           3.049
                                          110
                                       268.00
                                       332.88
GR     LNNP  SE      89
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SE 0 C

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3.200 3.388
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3.208 3.308
8.0500 STEP 0.2580
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-15.00 R2 -55.00
3.400 3.500
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328 MAX 50200
3.400 3. S00
332 MAX 116816
3.400 3.500
PE 0.00
TT 0.75
FP -20.00
m-3600 0
DM3 0.0000
RE3 85.00
R3 -65.00
                                                                    16:28:42
        G3-37.5; DI — 1.75; TT-. 75; CG-fiR
        320             257
        322             259
        328             263
        332             268

-------
              F2
                178  BO
             259.88  M3
             322.88  F3
                2.881
      C20 SHOT ZERO Cft_IBRflTION3
     0  TO      110  GR     LhM=
263.88  M4   268.88  SR       89
328.88  F4   332.88  ER       89
       3.11
                     *=	8
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                     IN
                                                                   320 MRX 1200
                 .               i       .

     lJ\fi-^J\r^M\-^^^
1101
2.733
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3.388
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                                                                   3.480   3.508

                                                                  328 MRX 45000
   2.733

1101
                  2.980
                      3.080
     3.180
  3.200
3.388
                                                                3.488   3.500

                                                              332 MfiX 187216
   2.733
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                 16:12:59
                      3.088
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3.300
                                                                3.488   3.580
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 61
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   228
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                         257
0.8500  STEP 0.2500  PE     0.80
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        MO   -1.088  FP   -20.88
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8.8888  CGT    32.5  DTP  8.8886
 75.00  CG     OFF   RE3   85.08
-15.88  R2   -55.80  R3   -65.80

                        16:12:59
                         263

-------
              Mini
                     "TCDD II/S  C20 SHOT  ZERO CflLIBRflTIONI
 Ml
 Fl
11
     1  ES
257.00  M2
320.00  F2
  2.713
   164  BO        0  TO
259.00  M3   263.00  M4
322.00  F3   328.00  F4
       2.879
         110  GR
      268.00  SR
      332.00  ER
                                      SE       82
                                  82  TI 80:02:58
                                  82  IN      1000
                              3 172    320 MAX 1200
   2.650
           2.800
         2.900
3.000
                                                  3.100
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                                      328 MPX 57608
   2.650
110-1
                 2.800
2.900
3.000
                                3.100
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                                                            332 MRX 135584
   2.650

   3-«JG-e5
SY      220  SE
Gl    0.000  IT

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                  2.800
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16:07:40  OP
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                               -55.00
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        320              257
        322              259
        328              263
        332              268
PE     0.00
TT     0.75
FP   -20.00
MJ  -2
DM3  0.1
RE3   85.00
R3   -65.00

   16:07:40

-------
PUG0303 1 MIMI TCDD II/S C20 SHOT ZERO Cfil TPPQTTr^i
SS
Ml
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110-
0-
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1 ES 178 BO 0 TO 110 GR LNNP SE 89
257.00 M2 259.00 M3 263.00 M4 268.00 SR 89 TI 00-03-05
320.00 F2 322.00 F3 328.00 F4 332.00 ER 89 IN 2200
>^v^r^^^^^
2.733 2.900 3.000 3.100 3.200 3.300
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1.733 2.900 3.000 3.
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S-ftUG-85 15:55:23 OP THP
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328 mx 26404
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332 MAX 57608
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3.400 3.500
PE 0.00
TT 0.75
FP -20.00
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DM3 0.0000
RE3 85.00
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G2-37.5; DI—1.75; TT-. 75; CG-PR
320              257
322              259
328              263
                 268
                                                              15:55:23

-------
    APPENDIX D
BLANK RESPONSE DATA

-------
ftLJGS332 1
SS 1
Ml 257.00
Fl 320.88
118-

2.758
11B-:
0_


2.750

11&:

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2.900 3.080


2.900 3.080
[FOR NEW CALIBRATION!
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328.08 F4 332.88

3.


3.
A its
188 3.288

'?'
188 3.288
GR Lt+f> SE
SR 88 TI 88
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: 83:86
608
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3.517
322 MAX 131424

3.308 3.480

3.517
328 MAX 13902
J.750

2.750
3-flUG-e5
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61 8.000
G2 0.000
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2.900 3.000
19:00:32 OP
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IT »»w^-r^"~ DTV

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85.80
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                                                              19:80:32
G2-37.5; DI—1.75; TT-. 75; CG-PR
328              257
322              259
328              263
332              268

-------
              DCflL 3  CFOR
                                                CflLIBRflTION3
                                               -IB
 SS        1  ES
 Ml   257.00  M2
 Fl   320.00  F2
110-a
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268.00
332.00
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LM*=»
  63
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 TI 00:02:59
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32B MflX
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110-3
2.800      2.900     3.000      3.100      3.200           3.367
                                                 322 MRX 147232
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2.800
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                                                3.367

                                       332 MAX 32004
   2.650

    3-«JG-85
 SY      220
 Gl    0.000
 G2    0.000
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2.800
2.900
3.000
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         1260

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                                     TH      150
                                     MO   -1.000
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                          CG
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                                          -55.80
                      PE     0.00
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                      R3    -65.00

                         18:54:57
        G2-37.5; DI —1.75; TT-. 75; CG-flR
        320              257
        322              259
        328              263
        332              268

-------
fiUG0330
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Ml 257.
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2.733
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1
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W-P— • 	 • 	 • 	 • 	 • 	 • 	 « 	 ( 	 • 	 • 	 • 	 • 	 1 	 1 	 • 	 • 	 1 	 p— i 	 r— »— i 	 , 	 1 	 1 	 , 	 , 	 , 	 , 	 , 	 , 	 , 	 , 	 , 	 ,_
2.733 2.900 3.000 3.100 3.200 3.300 3.400
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MPX
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   2.733        2.900     3.000     3.100    3.200     3.300     3.400    3.517
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   2.733        2.900     3.000     3.100    3.200     3.300     3.400    3.517

   3-flUG-e5     18:48:43  OP     TKP .  MTL  0.0500  STEP 0.2500  PE     0.00
SY      220  SE        0  C        10  MCL    1260  TH      150  TT     0.75
Gl    0.000  IT  »»•«"•«.««  DI    0.000               MO   -1.000  FP   -20.00
G2    0.000  LT  •»«•»»«  DIV  -0.044  IQ    -5.00               MU  -3600.0
G3   0.0000  DT    0.000  IN     0.00  DM1  0.0000  CGT    47.5  DM3  0.0000
SPF     0.0  GR     0.01  OR     0.00  R£l   75.00  CG     OFF   RE3   85.00
DTV   0.000  ST  •»»•»•»  R0   -38.00  Rl   -15.00  R2   -55.00  R3   -65.00

                                                                    18:48:43
       G2-37.5; DI —1.75; TT-. 75; CG-fiR
   1   320              257
       322              259
       328              263
       332              268

-------
SS 1
Ml 257.80
Fl 320.00



2.658



2.658
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2.658

2.658
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18:42:45
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263.80 M4 268.88
328.80 F4 332.88

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TVF MTL 8.8588
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8.88 DM1 0.8888
0.88 RE1 75.88
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SR 88 TI 82
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320 f
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3.280 3.300
322 f
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3.200 3.300
STEP 0.2588 PE
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CGT 89.9 Dt13
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R2 -55.80 R3
88
1:82:59
600
KX 26204

1 1 f T |
3.417
BX 28604


3.417
rax 7281

-i — i — i — i — |
3.417
«=tX 25204
3.417
8.88
8.75
*^rrYft n
•JD00.0
0.03QB
85.08
-65.80
                                                              18:42:45
G2-37.5; DI — 1.75; TT-. 75; CG-«R
320              257
322              259
328              263
332              268

-------
                                              NEK QPLIBRQTION3
ss
Ml
Fl
1101
1
257.00
320.00

ES
M2
F2

162
259.00
322.00

BO
M3
F3

0
263.00
328.00

TO
M4
F4

110
268.
332.
n
00
00

GR
SR
ER

U***
81
81

SE 81
TI 00:02:58
IN 600
320 MRK 233
                                                                                T
    2.650         2.800      2.900      3.000      3.100      3.200         3.350
110^,                                           .                    322 MAX 25604
   2.650         2.800      2.900      3.000      3.100      3.200         3.333
H0-.                                                                328 MfiX 7401
   2.650         2.800      2.900      3.000      3.100      3.200         3.350
H0-3                                                               332 MRX 26204
0-
SY
Gl
G3
DTV
2.650 I
3-AUG-85 1
220 SE
0.000 IT
0.0000 DT
0.0 GR
0.000 ST
i '' i ' ' — r ' ' '
2.800 2.900
8:37:44 OP , TW
0 C '10
«u>.» »«•«•* DI 0.000
«. .» «. .a «i +•*, nrw _ci e\^d
0.000 IN 0.00
0.01 OR 0.00
3.00Q
MTL
MCL
TQ
DM1
RE1
Rl
3.
0.0500
1260
0.0000
75.00
-15.00
100
STEP
TH
MO
CGT
CG
R2
' *" l
3.20C
0.2500
150
-1.000
13.7
OFF
-55.00
9
PE
TT
FP
MU
DM3
RE3
R3
3.350
0.00
0.75
-20.00
-3600.0
0. CTomd
85.00
-65.00
                                                                       18:37:44
        G2-37.5; DI—1.75; TT-. 75; CG-flR
        320              257
        322              259
        328              263
        332              268

-------
P«tfP7 * MTMI DCflL 2 CFOR N^" CPL
SS^ 1 ES 176 BO
Ml 257.00 M2 259.00 M3
Fl 320.00 F2 322.00 F3
1107
«
«
110-:

»[750 ^ 2.900 3.000
2.750 2.900 3.000
0 TO 110
263.00 M4 268.00
328.00 F4 332.00
/\JK
3.100 3.200
A* '*
3.100 3.200
IBRfiTIOm
GR LhTP SE
IM
88
SR 88 TI 00:03:06
ER 88 IN
320 rax
3.300 3.400
322 rax
Y
3.300 3.400
800
24804
3.517
25004
3.517
ll&l
                                                                    328 nPX 7201
   2.750

1101
                2.900
3.000
3.100
3.200
3.300     3.400    3.517

          332 MAX 27004
U;

SY
Gl
G2
G3
>.750
3-AUG-85
220
0.000
0.000
0.0000
SPF 0.0
DTV 0.000
2.900

SE
IT
l_y
DT
GR
ST
18:31:55
0
•n-t + ttt
«3»0«0»0«G«0«t
0.000
0.01
JO******
3.000 3.100
OP
C
DI
DIV
IN
OR
R0
THP
10
0.000
-0.042
0.00
0.00
-38.00
MTL
MCL

IQ
DM1
RE1
Rl
3.200
0.0500
1260

-5.00
0 • 0000
75.00
-15.00
3.
STEP
TH
MO

CCT
CG
R2
300
0.2500
150
-1.000

50.0
OFF
-55.00
3.400 3.517
PE
TT
FP
MU
DM3
RE3
R3
0.00
0.75
-20.00
-3600.0
0* 0000
85.00
-65.00
        G2-37. 5; DI—1.75; TT". 75; CG-PR
        320              257
        322              259
        328              263
                         268
                                                                      18:31:55

-------
PUG0326 1
SS
Ml
Fl
1
257.88
328.88
MIMI
ES
M2
F2
164
259.88
322.88
BO
M3
F3
DCflL 1
8
263.88
328.88
CFOR
TO
M4
F4
NEU CflLTBRPTIONI
118
268.88
332.ee
GR
SR
ER
LM*»
82
82
SE
TI
IN
IM
82
80:82:59
648
llBn
                                             v
                                                                   328 MPX 7372
   2.667        2.800      2.988      3.880      3.100       3.280         3.358
118-;
                                                                   322 MfiX 7535
   2.667        2.800      2.900      3.880      3.100       3.208         3.358
ne-
                                                                   328 MAX 5887
   2.667        2.888      2.988      3.888      3.188       3.288        ' 3.353

                                                                  332 MRX 37Q17


                                                >'•"?P
18
0aoot
.  n
— 3UBB. 0
8.0000
85.00
-65.88
                                                                      18:26:21
        G2-37.5; DI—1.75; TT-. 75; CG-flR
        328              257
        322              259
        328              263
        332              268

-------
OLG
ss
Ml
Fl
1101

257.
320.
1
1
00
00
MIMI
ES
re
F2
164
259.00
322.00
BO
M3
F3
DCflL 1
0
263.00
328.00
CFOR
TO
M4
F4
NEW C«_IBRfiTIONl
110
268.00
332.00
/\
GR
SR
ER
LNNP
82
82
in
SC 82
TI 00:02:59
IN 724
320 MAX 7535
   2.667        2.800      2.900      3.000      3.100      3.200          3.350
                                                                   322 MAX 7859
   2.667        2.800      2.900      3.000      3.100       3.200         3.350
110_                                                               328 MAX 5268
0-j
2.667
2.800
2.900
3.000
3.100
3.200
3.35C
110_j                                                              332 MBX 35940
                                           f\   •  s~t
                                                - 7 $3
0-
SY
Gl
G3
SflF
r\T\
'.667
3-flUG-e5
220
0.000
0.0000
0.0
r» nfif%
2.
1
SC
IT
DT
GR
CT
800
8:20:48
0

0.000
0.01
2.9C
OP
C
DI
BTV
IN
OR
oa
90 3
TVP
10
0flW3l
• uuu
0.00
0.00
• f '
1.000
MTL
MCL
TO
DM1
RC1
D1
3.1
0.0500
1260
—5 00
0.0000
75.00
-1^ on
00
STEP
TH
t^\
i *j
CGT
CG
t39
3.200 3.350
0.2500 PE 0.00
150 TT 0.75
MLJ -3600.0
56.8 DM3 0.0000
OFF RE3 85.00
-^c; on en -AS cva
                                                                      18:20:48
        G2-37.5; DI —1.75; TT-. 75; CG-fiR
        320              257
        322              259
        328              263
        332              268

-------
ftUG03g4
SS
m
Fl
             1  MIMI
            1  CS
      257.80  «2
      328.88  F2
   152  BO
259.80  M3
322.08  F3
     8  TO
263.00  M4
328.88  F4
   118  GR
268.88  SR
332.88  ER
             76
76  TI 80:82:57
76  IN      619
     328 MPX 8859
    2.658
                  2.888
            2.988
           3.888
          3.188
     3.288   3.283

     322 MRX 7878
   2.658

118-)
                  2.888
            2.988
           3.888
          3.188
     3.288   3.283

     328 MPK 5534
   2.658
1187,
                  2.888
            2.988
           3.888
          3.188
     3.288   3.283

    332 MRX 37965
0-1


2.650

SY
Gl
G2
G3
SPF
DTV
3-AUG-65
228
0* 000
8.888
8.8000
0.8
8.880

S£
IT
LT
DT
GR
ST
* * I *
2.880
18:15:36
0
«•»•» 
4010)010)010*
0.000
0.01
4ctataK*a|o*


OP
c
DI
DIV
IN
OR
R0

2.980
TVP
10
0. 088
-8.842
0.00
0.08
-36.00

1 * *
3.800
MTL
MCL

10
Dfll
RE1
Rl
0.0588
1268

-5.88
8.8888
75.08
-15.00


3.108
STEP
TH
MO

CGT
CG
R2
8.2500
158
-1.888

184.3
OFF
-55.88

* " ' "1
3.200 3.263
PE
TT
FP
ML)
0(13
RE3
R3
8. 88
8.75
-28.88
-3688.8
8.8888
85. DC
-65.88
        G2-37.5;DI—1.75; TT-.75;CG-PR
        328              257
        322              259
        328              263
                         268
                                                                      18:15:36

-------
OUG0503 1
SS 1
Ml 257.80
Fl 320.00
110:
MTMT DCflL 1
ES
«2
F2
192
259.00
322.00
DO
«3
F3
C BEGINNING OF ^IFT CfiLIBRftTION OEOO IM
0
263.80
328.00
TO
H4
F4
110
268.00
332.80
GR
SR
ER
LNNP
96
96
SE
TI
IN
96
80:83:84
1488
320 MPK 9602
   2.788   2.800

110-a
    2.980
                                3.000
        3.188
3.208
  3.300        3.450

       322 MPX 9802
  Of '  •  y.  r  .
   2.700   2.800
    2.988
                                3.888
        3.188
3.
118l
  3.388        3.458

       328 MflX 9882
                                                    3.208
                            3.380        3.450
                                332 MAX 43208
   2.700   2.800

    5-PUG-85
 SY      220  SE
 61    0.808  IT
 62    8.000  LT
 63   0.0888  DT
 SPF     8.8  GR
 DTV   8.888  ST
    2.908

22:44:53  OP
       0
                                3.800
        3.100
3.200
  3.380
3.450
THP   HTL  0.8500  STEP 0.2500  PE
                                                                         8.88
                                    10
                                 8.888
                                -8.836
                                  8.88
                                  8.88
                                -38.88
      MCL    1260  TH
                   MO
      10    -5.88
      DM1  8.8888  C6T
      RC1   75.88  CG
      Rl   -15.88  R2
          158
       -1.
        62-37.5; DI—1.75; TT-. 75; C6-flR
                         2S7
                         259
                         263
      TT     0.75
      FP   -20.88
      MU  -3600.0
 2.5  DM3  0.8880
OFF   RE3   85.88
      R3   -65.80

         22:44:53

-------

ss
Ml
Fl
257.
320.
I
1
00
00
mm
ES
M2
F2

178
259.00
322.00
/

BO
M3
F3
\
PE sflMPL
0
263.00
328.00
£
TO
M4
F4
r ^
1563G8420S-XP
110 GR
268.00 SR
332.00 ER
i »
5.13g
LNNP
89
89

SE
TI «
IN
320
TM
89
ne;4c*:4c*
1800
MRX 19004
   -1437.067
         -1436.800
              -1436.600
  -1437.067

110-1
                                                                       -1436.317
                                                                  322 MRX 20004
         -1436.800
              -1436.600
  -1437.067
110-j
  -1437.067
    S-flUG-85
                               -1436.317
                          328 MRX 43208
                              -1436.600
                                       -1436.317
                                  332 MRX
         -1436.800
              -1436.600
 5V      220  SE
 Gl    0.000  IT
 G2    0.000  LT
 G3   0.0000  DT
 SPT     0.0  GR
 DTV   Q.000  ST
23:57:35  OP
       0
  TJ-P   MTL  0.0500  STEP 0.2500  PE
    10
 0.000
-0.044
  0.00
  0.00
-38.00
MO.    1260  TH
             MO
IQ    -51gg
DM1  0.0000  CGT
RE1   75.00  CG
Rl   -15.00  R2
                               -1436.317
                                 0.00
        G2-37.5;DI—1.75;TT-.75;CG-PR
        320              257
        322              259
        328              263
   150  TT     0.75
-1.000  FP   -20.00
        MU  -3600.0
  17.5  DM3  0.0000
  OFF   RE3   85.00
-55.00  R3   -65.00

           23:57:35

-------
                           TCDD IIXS  C20 SHOT ZERO  CPLIBRflTIONl
                                                           -ID
                                                                   SC       87
                                                                   TI 00:03:06
                                                                   IN     7601
                                                                    320 WtX. 1000
                                                                  3.400     3.517

                                                                        MAX 1200
   2.750
2.900
3.000
3.100
                                              3.200
                                                     3.300
110H
                    3.400     3.517

                     328 MAX 51208
2.750
2.900
3.000
                                    3.100
3.200
                              3.400     3.517

                              332 MAX 118992
0H
•

SY
Gl
G2
G3
'.750
3-«JG-85
220
0.000
0.000
0.0000
SAT 0.0
DTV 0.000
2.900

SE
IT
LT
DT
GR
ST
17:59:11
0
*******
*******
0.000
0.01
*******
3.000
OP
c
DI
DIV
IN
OR
R0
3.100
TI-P
10
0.000
-0.042
0.00
0.00
-38.00
MTL
MCL

IQ
DM1
RE1
Rl
3.200
0.0500
1260

-5.00
0.0000
75.00
-15.00
3.
STEP
TH
MO

CGT
CG
R2
T — • — • — •"
300
0.2500
150
-1.000

31.2
OFF
-55.00
3.400 3.517
PE
TT
FP
MU
DM3
RE3
R3
0.00
0.75
-20.00
-3600.0
0.0000
85.00
-65.00
        G2-37.5; DI—1.75; TT-. 75; CG-PR
        320              257
        322              259
        328              263
        332              268
                                                                      17:59:11

-------
    APPENDIX E
SAMPLE ANALYSIS DATA

-------
ss
Ml
Fl

1
257.00
320.00
ES
M2
F2
176
259.00
322.00
BO
M3
F3
0
263.00
328.00
TO
M4
F4
110
268.00
332.00
GR
SR
ER
LNNP
88
88
SC
TI 80:
IN
. 320 MRX
88
83:16
1610
1225740
   2.917 3.000
      3.100
                          3.200
                                     3.300
           3.400
                                                             T
2.917 3.000"
                   3.100
               3.500          3.667

                   322 MftX 1283614
                3.200
 3.300
                                               3.400
                                                             T
2.917 3.000
                   3.100
               3.500          3.667

                     328 MRX 74791
                3.200
 0-
 3.300

r//-
     3.400     3.500          3.667
                     332 MRX 39948
   2.917 3.000
      3.100
                          3.200
3.300
     3.400
                                                         3.500
3.667
   6-AUG-85
SY      220
Gl    0.000
G2    0.000
G3   0.0000
SPF     0.0
DTV   0.000
   03:14:16
SC        0
XT  *******
l_T  *******
DT    0.000
GR     0.01
ST
OP
c
DI
DIV
IN
OR
R0
TT-P
10
0.000
-0.044
0.00
0.00
-38.00
MTL
MCL
0.0580
  1260
 10    -5.00
 DM1  0.0000
 RE1   75.80
 Rl   -15.08
                                                  STEP 0.2500
                                                  TH      150
                                                  MO   -1.800
        CGT
        CG
        R2
                                                          3.1
                                                         OFF
                                                       -55.00
       G2-37.5; DI—1.75; TT-. 75; CG-flR
       320              257
       322              259
       328            '  263
       332              268
                                                               PC     0.00
                                                               TT     0.75
                                                               FP   -20.00
                                                               MU  -3600.0
                                                               DM3  0.00GB
                                                               RE3   85.00
                                                               R3   -65.00

                                                                  83:14:16

-------
                                                             w
                                                              e
«JG0605 1
SS
Ml
Fl
1
257.00
320.00
MIMI
ES
M2
F2
166
259.00
322.00
BO
M3
F3
SHIRCO SAMPLE: sws-3-**-
0
263.00
328.00
/•N
TO
M4
F4
110
268.00
332.00
GR
5R
ER
LNNP SE
83 TI 00:
83 IN
320 MAX
IM
83
03:09
1419
1326519
   2.817   2.900

110T1
                                 3.100
                     3.000
                                  3.200
           3.300
                     3.000
                      3.400    3.500

                     322 MAX  1362566
                                 3.100
   2.817

110-1
2.900
3.200
   2.817  2.900
           3.300       3.400     3.500

                       328 MAX 74979
                      3.000
                                 3.100
                                  3.200
  3.300
                       3.400

                       332
                                3.500

                               3Z346
   2.817  2.900
                      3.000
                                 3.100
   6-«JG-85
SY      220
Gl    0. 000
G2    0.000
G3   0.0000
Sff     0.0
DTV   e.aae
                 03:04:01  OP
              SE        0  C
              IT  *******  DI
              LT  *******  DIV
              DT    0.000  IN
              GR     0A   OR
              ST  ***"*"«»*  R0
                                     10
                                 0.000
                                -3.044
                                  0.00
                                  0.00
                                -38.00
                              MTL
                              M0_
3.200

 0.0500
   1260
                              IQ    -5^00
                              DM1  0.0000
                              RE1   75.00
                              Rl   -15.00
  3.300

STEP 0.2500
TH      150
MO   -1.000

CGT    10.6
CG     OFF
R2   -55.00
                                                        3.400
                                3.530
       G2-37.5; DI—1.75; TT-. 75; CG-«R
       320              257
       322              259
       328              263
                        268
                       PE     0.00
                       TT     0.75
                       FP   -20.00
                       MU  -3600.0
                       DM3  0.0000
                       RE3   85.00
                       R3   -65.00

                          03:04:01

-------
                 1 MIMI
      ss
      Ml
      Fl
     1  E5
257.00  M2
320.00  F2
   180  BO
259.00  M3
322.00  F3
   SHIRCC
     0  TO
263.00  M4
328.00  F4
       0-
        110  GR
     268.00  SR
     332.00  ER
              3.434
                                                                                IM
                     gr       90
                 90  TI 00:03:16
                 90  IN     2219
                       320 MAX 876
 k.

 r
 u

 r
        2.917  3.000
             3.100
           3.200
     1101
        3.300     3.400      3.500         3.667

          3.318  3.384 3.443        322 MRX 1038
        2.917  3.000
             3.100
           3.200
        3.300
          3.400
        2.917 3.000
             3.100
     110H
               3.500          3.667

                     328 MfiX 36938
                               3.400     3.500         3.667

                                               332 MAX 81399
I
I
I
I
I
I
I
        2.917 3.000

         6-«JG-e5
      SY      220  SE

      G2    0!000  LT
      G3  0.0000  DT
      SAT     0.0  GR
      DTV   0.000  ST
             3.100

          02:41:16
                 0
           *******
           3.200
        3.300
          3.400
               3.500
                      3.667
             0.000
              0.01
        OP
        C
        DI
        DIV
        IN
        OR
        R0
  ThF
    10

-0.044
  0.00
  0.00
-38.00
MTL
MCL

IQ
DM1
RE1
Rl
0.0500
  1260

 -5.00
0.0000
 75.00
-15.00
STEP 0.2500
TH      150
MO   -1.000
CGT
CG
R2
   1.2
  OFF
-55.00
  G2-37.5;DI—1.75;TT-.75;CG-flR
  32O              257
  322              259
  328              263
  332              268
PE     0.00
TT     0.75
FP   -20.00
MU  -3600.0
Dt13  0.0OOO
RE3   85.00
R3   -65.00

   02:41:16

-------
                                                        A*
            1 HIHI _ SHIRCO SflfPLE  LlHLi ft Xft
           1  ES      180  BO        0  TO      110  GR     LN*»  SE      98
 Ml   257.00  M2   259.00  K3   263.00  M4   268.00  SR       90  TI 00:03:16
 Fl   320.00  F2   322.00  F3   326.00  F4   332.00  ER       90  IN     1600
H0-,                        A   A  A A  I       AA              *     320 MftX 1000
     LyWMyrwuwv^nAy^-*^^
   2.900   3.000    3.100     3.200    3.300 '    3.400 '•   3.500     3.600 3.683

116H                    .     3.187            3.36          3.504   322 MBX 1200

     /^^^AAAA^^/V^/^
   2.900   3.000    3.100     3.200    3.300     3.400     3.500     3.600 3.683
                                                                 328 MAX 50600
   2.900   3.000    3.100     3.200    3.300     3.400     3.500    3.600 3.683
110_
                                                                332 MAX 116592
O | ' • • •
2.900 3.
6-«JG-85
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Gl 0.000
62 0.000
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3.300 3.400
MTL 0.0500 STEP
MCL 1260 TH
MO
IQ -5.00
DM1 0.0000 CGT
RE1 75.00 CG
Rl -15.00 R2
3.500 3.600 3.683
0.2500 PE 0.00
150 TT 0.75
-1.000 FP -20.00
MU -3600.0
1.2 DM3 0.0003
OFF RES 85.00
-55.00 R3 -65.00
                                                                     02:55:20
        G2-37.5; DI — 1.75; TT-. 75; CG-flR
        320              257
        322              259
        328              263
        332              268

-------
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-------
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IN     1350
 320 MAX 2854
                                                                  3-285  3.329
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     2.936
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                3.005      3-068
                                   3.200    3.250    3.300 3.350

                                                    322 MAX 2263
                                       —	3.265    3.321
   2.917
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                                                                   328 MRX 4967
   2.917

110-1
               3.000    3.050    3.100    3.150   3.200    3.250    3.300  3.350
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   2.917
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                     8.8888  CGT
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        320              257
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               MJ   -3600.0
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                  07:32:57

-------
APPENDIX F






QVQC DATA

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-------
                               APPENDIX C
                        TECHNICAL WORK SCOPE FOR
                   THE ANALYTICAL PROGRAM PROVIDED TO
                          ROY F. WESTON BY ERT
1427J C3044

-------
A COMSAT COMPANY
ENVIRONMENTAL RESEARCH & TECHNOLOGY. INC.
69»; VIRGINIA ROAD CO'JCQRD MASSACHUSETTS 01742 USA (6!7) 369-8910 TELEX 923 325 ENVIRQRES CNCM CABLE
       EAS-5242
       ERT Document  No.  C-3044
                                            July  17,  1985
       Dr.  Kay Jones
       R.F. Weston
       Weston Way
       WestChester,  PA  19380
       Dear Dr.  Jones:
            This is to confirm our  recent  telephone  conversation regarding
       the analysis of samples from the  recent  field activities with Shirco
       Infrared Systems at  the Times Beach Dioxin  Research  facility.

            Two test runs,  designated as Runs  2 and  3, were conducted with
       the unit firing contaminated soil.   The  following  samples were
       collected and submitted to Earl Hansen  on 12  July,  1985:
       Waste Feed
                                  Run Designation
                                         2
                                         3
                         Samole Number
                             E-439
                             E-440
       Hopper Ash
                                         2
                                         3
                             E-441
                             E-442
       Fl-ue Gas

       (Consisting of
       particulate filter,
       front half rinse,
       XAD-2 resin and
       condensate)
         2a
         2b
         3a
Field Biased Blank
E-424 through E-427
E-428 through E-431
E-432 through E-435
E-436 through E-438

-------
                   Technical  Specifications for Dioxin Analysis
                                   Times Beach
 Analytical Protocols

      Sample preparation  protocols for each of the two solid matrices
 (waste feed, hopper ash)  should be consistent with those presently
 employed  by R.F.  Weston  as part of the EPA sponsored dioxin soil analysis
 program presently in  progress at the Times Beach site.  It is our under-
 standing  that these protocols represent an updated version of the EPA/CLP
 dioxin protocol  pertinent to the analyses of 2,3,7,8 TCDD in soil and
 sediment  samples tailored to the use of MS/MS technology.
                                                          ^
      Sample preparation  protocols for the flue gas samples should be
 consistent with  those outlined in Sampling and Analysis Methods for
 Hazardous  Waste  Incineration (first edition), February 1982 and employed
 by  Roy F.  Weston during  an earlier field demonstration program of dioxin
 destruction using the J.M. Huber advanced electric reactor.  The individual
 components from  the sampling trains (particulate filter, front half
 rinse  - 1:1 MC/AC, condensate and XAD-2 resin) will be combined in a
 manner consistent with this protocol to provide a single sample extract
 for each  train.   Actual  GC/MS analyses of all sample extracts should be
 conducted  in accordance  with the existing EPA protocol followed by R.F.
 Weston at  the Times Beach site.

      It is our understanding that these analyses will be conducted using
 an  IIS/MS  system  fitted with a fused silica capillary column.
Results

     Results for the flue gas extracts are to be provided in units of
total picograms (pg) per sample.  The results from the solid samples
will be reported as parts per billion (ppb), in units of ng/g or ug/kg.
It is assumed that all reported data points will reflect method blank
corrected values.  Results for all samples should be reported as both
total tetrachlorodibenzo dioxin isomers (TCDD) as well as 2,3,7,8 TCDD.
It is our further understanding that an absolute detection limit of
less than 10 pg will be achieved for 2,3,7,8 TCDD in each of the flue
gas samples.  Detection limits of less than 0.25 ppb will be required
for both the hopper ash and soil or waste feed samples.
Quality Control Requirements

     These again must be consistent with the QA/QC requirements of the
EPA sponsored dioxin analysis program presently in progress at the Times
Beach site.  These should include, at a minimum, the use of method
blanks, laboratory performance check solutions, laboratory fortified
spike samples, laboratory replicates, instrument tuning and performance
reference materials and isotopically labeled surrogates and internal
standards in each and every sample.

-------
Dr. Kay
EAS-5242
Page Two
     As discussed in our conversation, we will require the following
analyses:

        o  Gravimetric determinations for the collected
           particulate samples from each test run.

        o  Volumetric determinations for the collected
           condensate samples from each run.

        o  Dioxin analysis of duplicate samples of hopper
           ash and waste feed from Runs 2 and 3.

        o  Dioxin analysis of the collected flue gas samples
           from the field biased blank and Runs 2a and 3a.
           We will authorize the analysis of the flue gas
           samples from Run 2b only after receipt of prelim-
           inary results for the other two samples.


     Technical specifications to this program, including reporting
requirements and deliverables , are provided as an attachment to this
letter.  These specifications also serve to confirm specific analytical
protocols and requisite detection limits, as discussed with yourself
and Dr. David Ben Hur.

     We understand that the final data will be available by 2 August.
If we can provide any additional information in this regard, please
contact either myself or Gary Hunt at (617) 369-8910.
                                      Sincerely,
                                       ^.o- v.  \\\('( T.

                                      Mark McCabe
                                      Senior Scientist
                                      Engineering and Analysis Staff
MM/sj

Enclosures

cc:  K. Johansen, Shirco
     R. Dunla   ER1

-------
                               U S ENVIRONMENTAL PROTECTION AGENCY
                                    Contract Laboratory Program
                              SAMPLE MANAGEMENT OFFICE


        MEMORANDUM
          » •

        DATE:        3une 10, 1985

        TO:          Solicitation Community for SAS No. 1563-G

        FROM:       Roch A. Mongeon  ^E^Vu—
                     Analytical Services Coordinator
        THRU:       Linda Haas Boynton
                     Analytical Services Group Leader

:        SUBJECT:    SAS No. 1563-G, Quail Run and Related Sites

I
             Region VII  has  notified the Sample  Management Office (SMO) that operational
•       MS/MS analytical support  for SAS No. 1563-G, Remedial Action at Quail Run  and
I       Related Dioxin Sites, is needed by 3uly 8, 1985. Attached are:

             A.    Definitions and Criteria for Laboratory Solicitation and Award

             B.    Major Administrative and Procedural Terms for inclusion in the SAS 1563-G
                  Specific Scope of Work (SOW).

'            C.    Terms of Contractor Default and Termination

I             D.    Government-Furnished Supplies and Services

             E.    June 1985 Draft, MS/MS Protocol, Region VII

j             These attachments,  along  with the previously  supplied  SAS  Standard SOW,
        constitutes the solicitation package for this SAS.   The major issues raised at the  May
        23rd  Pre-Solicitation Meeting are addressed in this package and the terms stated herein
j        are not negotiable.  Please cajr fully  r^vif ftLthe-iolicliatiqn Packf*ft^ *nrf submit your  bids
'        to the SMO no later tharffiOO p.m.. EST. on Thursday, June  13, 1985^ Bids received later
        than this time will not be~considered. It is expected  that bid results will be announced by
I        Friday, 3une U, 1985.       '


.        cc:   W. Keffer, Region VII
I             R. Kleopfer, Region VII
             C. Hensley, Region  VII
             J. Woods, Region VII
I             M. Carter, HRSD
1             D. Thacker, SMO

-------
                                                                     Attachment A

                    Solicitation: SAS No. 1563-G  -  Quail Run


Definitions and Criteria for Laboratory Solicitation and Award

     1.    Solicitation Community

           Those  laboratories with  an identified GC/MS/MS capability and appropriate
           backup capabilities  that  can be located and operational within two  hours
           driving distance of the Quail Run Dioxin Site (Grey Summit, MO).

     2.    Competitive Community

           The community shall consist of either the following (a) or (b), as appropriate:

           (a)   At least  three CLP laboratories which have submitted responsive bids.
                All non-CLP bidders shall be considered nonresponsive.

                                                OR

                In  the event that  fewer than three CLP laboratories submit qualified
                bids:

           (b)   Bids from all  solicited laboratories (CLP and non-CLP) shall be  consi-
                dered and evaluated for award.

     3.    BidD* iline

           Firm,  xed per-sample price bids must be submitted to SMO by  5:00 p.m. EST
           on Thursday, June 13, 1985.

     
-------
                                                                     Attachment B

                    Solicitation: SAS No. 1563-G —  Quail Run


Major Administrative and Procedural Terms for Inclusion in

SAS No. 1563-G. Specific Scope of Work

     1.   Type of Contract; Indefinite  Quantity and Funding

          This  is  a firm,  fixed  per-sample price,  indefinite quantity contract for
          supplies or services specified in the SAS No. 1563-G contract, with penalties
          for late delivery of data.

     2.   Project Scale - Government's Minimum Obligation

          The minimum services  the Government is obligated to purchase  under this
          contract will be equivalent  to  the per-sample price bid by  the  contractor
          times 70, or $  ,	..

          The term of this contract is 70 consecutive days, beginning on the first day
          that  samples are received (not including  samples received  under the  pre-
          award validation option).  See Attachment A, item 5.

          Region VII anticipates taking  at  least 700 samples within  70 days.   The
          Region also indicates that the  total demand could reach 2,500 total samples
          within this timeframe.

      3.   Sample Delivery  to Laboratory

           Samples  may be  delivered to and  must be accepted by the laboratory at any
           time between 6:00 a.m. and 6:00 p.m., Monday - Saturday, during the term  of
           this contract.  A minimum of 0, to a  maximum of 50 samples  per day will  be
           delivered to and accepted by the laboratory for analysis.

      it.    Data Turnaround

           (a)   Primary Data Turnaround;  Primary data (consisting of items 1 - 17, 21)
                section XIV, Data Reporting of the Dune Draft Protocol) by EPA Sample
                No., for each sample received before 12;00 p.m. (noon)  on any one day
                is due by 6:00 a.m. on the following day at Tfte designated receipt point.
                Primary data for samples received after 12:00 p.m. (noon)  on any one
                day is  due  by  6:00   a.m.  on   the  second^  calendar day   thereafter.
                (Exception:  preliminary  hardcopy  data  for  all  samples received  at
                laboratory  on zTSaturdav are due by 6:00 a.m. on the following Monday.)

           (b)   Secondary  Data Turnaround; Secondary hardcopy data,  consistent with
                item 18. of Section XIV  of  the  3une Draft  Protocol are due seven  (7)
                days from the original  primary hardcopy data due date.

-------
                                 -2-
     The  Pre-Award  Validation  Analysis  must  be  completed  on the  same
     GC/MS/MS instrument(s) and on the same GC/MS/MS or LRMS instrument(s)
     and data production system that will be  used as the primary and secondary*/^'*"/
     (backup) instruments at the on-site  facility (should the laboratory be awarded^'***;
     SAS No. 1563-G).
     During performance of the Pre-Award Validation Analysis, laboratories shall   0
     be granted two  attempts (within a single period of 15 days) to meet the
     QA/QC and data  turnaround requirements of this  SAS.  Upon failing the
     second attempt  to meet these requirements, laboratory shall be considered
     not qualified for award for this SAS, and the second lowest bidder will then
     be considered for the award.

6.   On-Site and Operational Due Dates

     Laboratory  must  be  on-site and  operational (i.e., capable of performing
     according to all technical and administrative terms of the SAS No. 1563-G
     contract) within 15 days of notification of award from SMO.

-------
                                                                     Attachment C

                    Solicitation: SAS No. 1563-G —  Quail Run


Terms of Contractor Default and Termination

     Bidders are hereby notified that, for the purposes of this contract, any or all of the
     following shall constitute default:

     1.   Failure to maintain a capability to perform the required number of analyses
          according to the SOW for the SAS No. 1563-G contract.

     2.   Failure to meet delivery, and documentation requirements.

     3.   Failure to meet the minimum QA/QC criteria required by the SAS No. 1563-
        .  C contract.

     These conditions will endanger performance of the contract in accordance with its
     terms.  Therefore,  if such conditions persist  beyond the limits established in
     Schedules 1. and 2. below, the contract may be terminated for default.

     Schedules

     1.   Failure to analyze  the required sample load of up. to fifty (50) samples per
          day and the deliverable submitted within the time  specified by the contract
          on:

          (a)   Twenty  percent (20%) or more  of  total sample receipts at any time
                during the term of this contract,  or

          (b)   Two or more consecutive batches of samples for analysis.

     2.   Failure to meet the minimum analytical quality  control (QC),  instrument
          tuning  and calibration, detection limit, and reporting requirements of the
          analytical protocol for this contract on:

          (a)   Greater than or equal to 20% or more of the total sample  receipts at
                any time during the term of  this contract, or

          (b)   On two (2) or more consecutive batches of samples for analysis.

-------
                                                                      Attachment D

                    Solicitation:  SAS No. 1563-G  — Quail Run


Government-Furnished Supplies and Services

     1.    Samples  for  Analysis   —   Consisting  of 30  -  300 g  portions of  soil or
           vegetation in individual collection containers.

     2.    For the  purposes of electronic submission of primary  data, the  EPA  will
           provide a portable IBM-XT personal computer.

     3.    EPA is currently negotiating for a location to make available to the labortory
           contracted for services under SAS No.  1563-G  that  will  meet  the geo-
           graphical constraints of the contract.

           Note however, that there is not currently such a  site available (i.e., supplied
           by EPA)  and that labortory should consider it their responsibility to  provide
           themselves with a site within two hours drive of the Quail Run site  in Grey
           Summit,  Missouri.

-------
                                 -2-
5.   Point of Data Delivery

     Primary data will be delivered via electronic submission to the Region VII  /
     Laboratory in Kansas City, Kansas.                                      /

5.   Adjustment/Penalty Schedule

     (a)    Primary Hardcopy Data;  Two percent (2%) of the SAS per-sample bid
           price for each hour late.

           At  the end of 50 hours,  one-hundred percent (100%) of the SAS per-
           sample price will be withheld.  At the end of the 24th  hour after the
           time that  primary hardcoov data is due, forty-eight percent (48%) jaf
           the SAS per-sample price will be withheld  and the Region shall cease
           sending samples to the laboratory  to conduct  an on-site^ audit of the
           facility to  determine the cause for late  data delivery.  Once the cause
           for the late data is remedied, the Region shall  resume sending samples
           for analysis to the laboratory.  If late  data delivery  is not remedied,
           this contract may be terminated.  See Attachment C.

     (b)    Secondary  Hardcopy Data;  Two percent (2%) of the SAS per-sample bid
           price for each day late.

     (c)    Example of Penalty Assessment

           Following  Is an example  of assessment of penalties based on primary
           and  secondary late data penalty schedules.

           Per-Sample Price              $100.00

           Sample A Primary Data:       Two Hours Late
           Sample A Secondary Data:     Two Days Late

           o  Late Primary Data Penalty assessment at two percent (2%) per hour
              late.

                         $100.00  X .02 X 2 Hours = $4.00 Penalty

           o  Late Secondary Data Penalty assessment  at  two percent (2%) per
              day late, based on SAS per-sample price:

                         $100.00 X .02 X 2 Days = $4.00 Penalty

           o  Amount of per-sample price  due  laboratory,  after adjustments for
              primary and secondary late data penalties:

                        $100.00  -  $8.00 = $92.00 Due to Laboratory

-------
                                    -3-
    6.    Instrumentation

         GC/MS/MS is the required primary instrumentation for supplying services for
         SAS  No.  1563-G.   In the event  of failure  of  the  primary  GC/MS/MS
         instrument(s), backup instrumentation (either GC/MS/MS or LRMS) must be
         available to supply a continuum of analytical support in full compliance with
         all terms of the SAS No. 1563-G contract.

         Note that LRMS does not constitute  an acceptable long-term substitute for
         GC/MS/MS for provision of services under this SAS.  LRMS  may only be used
         as a backup when primary instrumentation has failed, as defined below, for no
7        longer than^wo days of laboratory analysis in a row, and/or for no more than
         twenty percent (20%) of the  total sample receipts  at any time during the
         term of this contract.

         GC/MS/MS Failure

         GC/MS/MS failure is defined as malfunction of the instrument which prevents
         consistent compliance with any or all of the  QA/QC requirements of the
         analytical protocol.
          'A>«v  //  »»>^«  «>^ *t r&*^f*e.e.  tobLA
            IS  jt^st+H+£j  &J   7^>»ff  or/rHajLj ^t

-------
                                                     JUNO 5 198
   RAPID DETERMINATION OF TCDD IN SOIL AND SEDIMENT



USING GAS CHROMATOGRAPHY AND TANDEM MASS SPECTROMETRY
                     June  1985
        U.  S.  ENVIRONMENTAL PROTECTION AGENCY



                      REGION VII

-------
                                                                   JUNO 5 198!
                             TABLE OF CONTENTS
                             ~~" ~         ^





                                                          Page


   I.   SCOPE AND APPLICATION	  1
 i

  II.   SUMMARY	  1



 III.   INTERFERENCES	  2
  •


  IV.   SAFETY	  2


   V.   APPARATUS AND MATERIALS	  4



  VI.   REAGENTS	  5


 VII.   CALIBRATION	  7


VIII.   QUALITY CONTROL REQUIREMENTS	  11


  IX.   SAMPLE  COLLECTION,  PRESERVATION,  AND  HANDLING	  13



   X.   SAMPLE EXTRACTION	  14



  XI.   CLEANUP	.'.  15


 XII.   GC/MS/MS ANALYSIS	  17


XIII.   METHOD PERFORMANCE	  19


XIV.   DATA REPORTING	  22

-------
 I.   SCOPE  AND  APPLICATION                                         JfN 05 1985

      This  method  1s  for  use  In the rapid determination of 2,3,7,8-Tetrachloro-
 d1benzo-p-d1ox1n  (2,3.7,8-TCDD) In soil and sediment, when 2,3,7,8-TCDD 1s
 known to be  the principal  or only tetrachlorod1benzod1ox1n Isomer present.
 The  method Is  not specific for the 2,3,7.8-TCDO Isomer, unless a capillary
 column which separates that  Isomer from the other 21 TCOO 1 sowers Is employed.
 The  method Is  applicable 1n  the concentration range of 0.3-25 ug/kg.

      The method employs  a  tandem quadrupole mass spectrometer (MS/MS) as the
 final  detector.  The specificity of detection Inherent In such a system
 significantly  reduces the  need for sample cleanup.  This, 1n turn, Improves
 productivity and cost-effectiveness relative to other high resolution and low
 resolution GC/HS analysis  techniques.  The apparatus and methods described
 are  designed for use in  a mobile laboratory, which permits on-slte analyses.
 •
      The method 1s Intended  to be used when analytical results are required
 rapidly, such  as when site cleanup operations are 1n progress.  Since the
 method is  not  isomer specific, false positives, Including isomers other than
 2,3,7,8-TCDD,  may occur.  But errors in this regard would be on the side of
 safety.  Emphasis in the method 1s placed on avoiding false negatives, as
 this  is a  more critical  consideration when public health is to be protected.

      This  method 1s  restricted to use only by or under the supervision of
 analysts experienced in  the  use of gas chromatography/triple quadrupole mass
 spectrometers  and skilled  in the interpretation of mass spectra.

      Because of the  extreme  ';oxicity of this compound, the analyst must
 prevent exposure to himself, or to others, by materials known or believed to
 contain 2,3,7,8-TCOD.  Section IV of tnis method contains guidelines and
 protocols  that serve as  minimum safe-handling standards in a limited access
 laboratory.

                 Analyte                CAS Number

               2,3.7,8-TCOO               1746-01-6

 II.   SUMMARY OF METHOD

      Five  (5)  grams  of anhydrous sodium sulfate 1s placed 1n a 10 ml serum
 vial  and the vial with cap and septum is weighed.  Approximately 5 grams of  a
 soil  sample  is added and the vial is re-weighed.  The sample is spiked with
 internal and surrogate standards of Isotopically labelled 2,3,7,8-TCOD.  The
 sample is  mixed by shaking,  and extracted with acetonitrile/dichloromethane
 in the closed  vial.  An  aliquot of the extract 1s taken and, after separation
 from acetonitrile, the dichloromethane is used directly for GC/MS/MS analysis.
Clean-up should usually  not  be necessary, but a clean-up procedure is included
 for  those  samples which  do not meet quality assurance criteria.  Concentration
of the extract may be done to lower the minimum detectable concentration.
Capillary  column GC/MS/MS conditions are described which allow for separation
of TCDO from the bulk sample matrix and measurement of TCDD 1n the extract.

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Quantification Is based on the response of native TCOO relative to the isotopic^
labelled TCOD Internal standard.  Performance Is assessed based on the results  fi
surrogate standard recoveries, EPA performance evaluation samples, spike recover
tests, and method and field blanks.

III.  INTERFERENCES

  ,   Method Interferences may be caused by contaminants In solvents, reagents,
glassware and other sample processing hardware that lead to discrete artifacts
and/or elevated backgrounds at the Ions monitored.  All of these materials
must be routinely demonstrated to be free from Interferences under the
cpnditions of the analysis by running laboratory method blanks as described
In Section VIII.

     The use of high purity reagents and solvents helps to minimize interference
problems.  Purification of solvents by distillation In all-glass systems may
be required.

     Matrix interferences may be caused by contaminants that are co-extracted
from the sample.  The extent of matrix Interferences will vary considerably
from source to source, depending upon the nature and diversity of the sample.
2,3,7,8-TCDD is often associated with other interfering chlorinated compounds
which are at concentrations several magnitudes higher than that of 2,3,7,8-TCDD.

     The use of a triple quadrupole mass spectrometer as the detector serves
to minimize the influence of many of these Interferents.

IV.  SAFETY

     The following safety practices are excerpted directly from EPA Method
613, Section 4 (July 1982 version):  See following page.

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 •  4  4.« ,w*rvnf (X
 ••eh njagent used in this method he
 not been precisely defined; however.

••ch chemical compound should be
treated •• • potential health hazard.
From this viewpoint. eiposur* to these
Chemicals mult b« reduced to the
lowest possible level by whatever
me»ns available. The laboratory •
responsible for maintaining • current
awareness M« of OSHA regulations
regarding the safe handling of the
chemicals specified in this method. A
rtft.
Benzene and  2.3.7.8-TCDD have been
identified as suspected human or
mammalian carcinogens.

4.2   Each laboratory must develop a
strict safety program for handling of
2.3.7.8 TCDO. The following labora-
tory practices are recommended:

4.2.1  Contamination of the labora-
tory will be minimn ad by conducting alt
manipulations in a hood.

4.2.2 The' effluents of sample
splitters fo> the gss chiometograph end
toughing pumps on the GC/MS should
pass through either a column of
activated charcoal or be bubbled
through a trap containing oil Of high-
boding alcohols.

4.2, J Liquid waste should be
dissolved in methanol or ethanol and
irrad>ated with ultraviolet light with
wavelength greater than 290 nm for •
several days. (Use f 40 81 lamps or
equivalent.) Analyze liquid wastes and
dispose of the solutions when
2.3.7.8-TCDD can no longer be
detected.

4.3   Dow Chemical U S A has issued
the following precautions (revised
 11/78) for safe  handling of
2.3.7.8-TCDO in the laboratory:

4. J. f  The following statements on
safe handling are as complete as
possible on the bens of available
toiico'og-cal information. The
precautions for safe handling and uee
are necessarily general in nature smce
detailed, specific recommendations can
be made only for the particular eiposure
and circumstances of each individual
use. Inquiries about specific operations
or uses may be addressed to the Dow
Chtrmcai Company  Assistance •»
 evaluating the health hazards of
particular plant conditions may be
 obtained from cenem consurt*o
 labo»atones and from State  Depart-
 ments of  Health or of Labor, many of
 which have an industrial health service.
 2.3.7.8 TCDD « extremely lo«iC to
                                                                                                   f'Mj
                                                                        0 5  /g
      laboratory animals. However, rt has
      b«tn handled for years without injury In
      enalyt
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V.  APPARATUS AND MATERIALS
     All glassware Is Initially cleaned with aqueous detergent and then  rinsed
with tap water, delonlzed water, acetone,  toluene and methylene chloride.
Other cleaning procedures may be used as long as acceptable method blanks  are
obtained.
•
     Electronic balance, capable of weighing at least 50 g, with an accuracy
of at least +. O.OS g.
     Shaker, vortex-type or equivalent
     Centrifuge, 4UOO rpm, capable of handling 25 mm diameter vials
     Centrifuge tubes
     1U ml serum vials; with teflon faced septa and aluminum caps (Chrompak
•10204 and 10213 or equivalent)
     1 ml serum vials; with teflon faced septa and aluminum caps (Chrompak  .
10201 and 10211 or equivalent)
     Crimper for 10 ml serum vial  (Chrompak 10233 or equivalent)
     Crimper.for 1 ml serum vial  (Chrompak 10231 or equivalent)
     Disposable teflon 0.45 micron filters (Millipore.SLHV025 HB, or equivalent
     5 ml disposable Glaspak syringes  (Sargent Welch S-79401-B or equivalent)
     18  gauge  disposable  syringe  needle (Sargent Welch S-79402-G or equivalent)
     Disposable pipets, 5 3/4  inches  x 7 mm o.d.
     Glass wool, silanized
     Nitrogen  blowdown  apparatus
     Gas chromatograph  -  an  analytical system with  all required accessories
 including syringes  and  analytical  columns.  The  injection  port must be designed
 for capillary  columns  and splUless  Injection.
     Triple  quadrupole  mass  spectrometer with GC transfer  line and glow
discharge ion  source (TAGA*  6000, SCIEX®,  Thornhill,  Ontario. Canada)
     Compressed Gases:   Zero Grade Air (from distillation, not water
                          hydrolysis)
                          Ultra High Purity Nitrogen
                          Ultra High Purity Argon
     Column:             15  m long, wide  bore  fused silica capillary  (eg.  U.32
                          mm  I.D.)
                          DB-5 1.0 micron  film  thickness.

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                                                                   JUNO 5  ijt


 VI.  REAGENTS

 Stock Standard Solutions^

     Stock standard solutions correspond to three toluene solutions containing
 unlabelled 2,3,7.8-TCOD at varying concentrations, and iJCi2-2,3,7,8-TCDD
 (Internal standard, CASEIN 80494-19-5) at a constant concentration.   These
 Solutions also contain 37Cld-2,3.7,8-TCDD (surrogate compound, CASRN 85508-
 50-5) at varying concentrations.  These stock solutions are to be used 1n
 preparing the calibration standard solutions, and are to be obtained from  the
 Quality Assurance Division, USEPA, Environmental Monitoring Systems Laboratory
 (EMSL-LV), Las Vegas, Nevada.  If not available from EMSL-LV, stock standard
 solutions may be prepared from commercially available standards.  However,
'the accuracy of these solutions must be checked against EPA supplied standard
 solutions.

     The three stock solutions Mill have the following concentrations of
 unlabelled, Internal and surrogate standards.

 Stock Solution II (CC1)
     Uqlabeled 2,3,7,8-TCDO - 0.2 ng/ul
     J;Cl2-2,3,7,8-TCDD - 1.0 ng/ul
     37CTj-2,3.7.8-TCDO - 0.06 ng/ul
Stock  Solution 12   (CC2)
     Uqlabeled  2,3,7,8-TCOO - 1.0 ng/ul
     i;Ci2-2.3,7,8-TCDO - 1.0 ng/ul
     37CTj-2.3,7,8-TCDD - 0.12 ng/ul
Stock  Solution  13   (CCS)
      Uqlabeled  2,3,7,8-TCDD - 5.0 ng/ul
      "C12-2.3.7.8-TCDD  -  1.0 ng/ul
      37CtJ-2,3,7,8-TCOD  -  0.2 ng/ul
 NOTE:   Store  stock  solutions  In  1 ml  amber m1ni-v1als under  refrigeration.

 Calibration Standard  Solutions

     Calibration standard  solutions  are  prepared  to  simulate the conditions
 of  sample analysis  as nearly  as  possible.  Three  calibration standard solutions
 are prepared  from the stock standard solutions  so as to  contain constant
 amounts of Internal standard  (5  ug/kg equivalent) with variable amounts of
 unlabeled standard  (1,5, and  25  ug/kg equivalent) and surrogate standard
 (0.3,  0.6, and 1.0  ug/kg equivalent). The equivalent concentrations are
 based  on the  use of 5-gram samples,  extraction  with  5 ml  of  2:1 acetonitrile:
 dichloromethane. and a final  extract volume  of  approximately 1.66 ml dichloro-
 methane after removal of acetonitrile, as called  for 1n  the  procedure.

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                                                                    UN 05 198
Low Level
     Add 75 ul  of stock solution fl to a 5 ml  volumetric  flask  and bring to
volume-with dlchloromethane.   Mix well.   This  solution-contains an equivalent
concentration of 1 ug/kg of 2,3,7.8-TCDD, 5 ug/kg of  13C12-2,3.7.8-TCDD, and 0.3
ug/kg of 37Cl4-2,3,7,8-TCDD.

Medium Level

 <    Add 75 ul  of stock solution 12 to a 5 ml  volumetric  flask  and bring to
volume with dlchloromethane.   Mix well.   This  solution-contains an equivalent
concentration of 5 ug/kg of 2.3.7,8-TCDD, 5 ug/kg of  1JC12-2,3,7,8-TCDD, and 0.6
ug/kg of 37C14-2,3,7,B-TCDD.
 «
High Level

     Add 75 ul  of stock solution 13 to a 5 ml  volumetric  flask  and bring to
volume with dichloromethane.   Mix well.   This  solution  contains an equivalent
concentration of 25 ug/kg of 2,3.7,8-TCDD, 5 ug/kg  of 1<3C12-2,3,7,8-TCDD,  and  1.
ug/kg of 37Cl4-2,3,7.8-TCDD.

     NOTE 1:  Although the surrogate. 37Cl4-2,3,7,8-TCDD, is present in all  thre
level calibration solutions, only the high level  solution is used for calculatin
the  relative response factor for the surrogate.

     NOTE 2:  All calibration standard solutions  must be  stored in an Isolated
refrigerator and protected from  light.  Check these standard solutions frequen
for  signs of evaporation.

Sample  Spiking Solution

     The  sample  spiking solution  1s also to be obtained from the Quality
Assurance Division, U. S. EPA Environmental Monitoring Systems Laboratory
 (EMSL-LV),  Las Vegas.  Nevada.  The spiking solution will  have the following
concentrations of internal and surrogate standards.
      HC12-2.3.7.8-TCOD  -  0.5  ng/ul
      37CTi-2,3.7,8-TCDO  -  0.1  ng/ul
      When 50 ul  of  this  solution  is  spiked in 5 g of soil, the resulting
 concentrations in the soil  are  5  ug/kg  and 1 ug/kg of internal and surrogate
 standard, respectively.

      It is recommended that approximately 2.5-5 ml of the spiking solution be
 transferred to a 5  ml serum vial  and sealed with a septum and cap prior to
 each day's work for use In  spiking samples that day.

      NOTE:  It is very Important  that no evaporation of sample spiking solution
 be allowed to occur, since  the  accuracy of results are directly dependent on
 the addition of a known amount  of internal standard.

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Field Blank Spiking Solution

     The field blan* spiking solution 1s  also  to  be  obtained from the Quality
Assurance Division, U. S. EPA, Environmental Monitoring  Systems Laboratory
(EMSL-LV), Las Vegas, Nevada.  The spiking  solution  will have the following
concentrations of unlabelled, Internal, and surrogate  standards:
     2«3,7,8-TCDD - 0.1 ng/ul
     "c12-2,3.7,8-TCDD - 0.5 ng/ul
     37CTj-2,3,7,8-TCDO - 0.1 ng/ul
     When 50 ul  of this solution 1s spiked 1n  5  grams  of  soil,  the  resulting
concentrations 1n the soil are 5 ug/kg of Internal  standard  and 1 ug/kg each
of unlabelled and surrogate standard.

     NOTE:  It 1s very Important that  no evaporation of field blank spiking
solution be allowed to occur, since the accuracy of results  are directly
dependent on the addition of a known amount of internal standard.

Sol vent
     All solvents should be pesticide grade or equivalent.   The following
solvents will  be needed:

     Acetonitrile
     Dichloromethane
     Cyclohexane
     Toluene
     Benzene
     Methanol

Silica Gel

     Type 60,  70-230 mesh. Soxhlet extracted with dichloromethane for 24 hours,
then activated for 24 hours at 130°C.

Acid Alumina

     AG 4, 100-200 mesh, soxhlet extracted with dichloromethane for 24 hours,
then activated for 24 hours at 190°C.

Carbopack C


CelUe S4S

Sodium Sulfate

     (ACS) granular, anhydrous.

VII.  CALIBRATION AND LIMIT OF DETECTION DETERMINATIONS

     Calibration must be done using the Internal standard technique.  In this
case, the internal standard 1s an Isotope of the compound-of-Interest, and

-------
therefore, the technique 1s  also referred to as 1sotope-d11ut1on-mass  spectro-
metry.  The three calibration  standard solutions described  In  section  VI  are
required.

     Inject 1-2 ul  of each of  the calibration standard solutions  and acquire
selected reaction monitoring data for the following parent- daughter tons:

     m/z « 320 *257
     m/z » 322 -*259
     m/i - 328 ->263
     m/z « 332 ^268
  t
     For simplicity in subsequent sections, we will refer only to the  daughter
Ions, since quantltatlon 1s  based on daughter Ion response.

     Relative response factors for unlabelled 2,3,7,8-TCDD  vs  the Internal
standard for triplicate determinations of each of the three calibration
standard solutions are calculated.

Equation I:  Relative Response Factor (RRFs) for 2,3,7,8-TCDD

     RRFs - (AsCis)/(AisCs')

     where As * the sum of the area responses for the ions, m/z 257 and 259,
                 corresponding to the unlabelled standard,  2,3,7,8-TCDD.

           AJS « the area response of,the ion m/z 268, corresponding to the
               .  internal standard, i<5C12-2,3,7,8-TCDD.

            Cs « the concentration of the unlabelled standard, 2,3,7,8-TCDD

            CjS « the concentration of the Internal standard,  ^C12*2,3,7,8-TCDD.

     In the case of the unlabelled 2,3,7,8-TCDD each of the calibration
standard solutions must be analyzed in triplicate, and the  variation of the
RRF values for each compound at each concentration level must  not exceed 101
RSD.  If the three mean RRF  values for each compound do not differ by  more
than +_ 10%, the RRF can be considered to be independent of  analyte quantity
for the calibration concentration range, and the mean of the three mean RRFs
shall be used for concentration calculations.  The overall  mean is termed a
calibration factor.

     Similarly, relative response factors for the surrogate standard vs the
internal standard for the triplicate determinations of the  high level  calibration
solution are also calculated.

Equation II; Relative Response Factor (RRFSS) for 37Cl4-2,3,7,8-TCDD

     RRFS$ - (A$$C1$)/(A1$C$S)

     where Ass • the area response of the.daughter ion, m/z 263, corresponding to
                 the surrogate standard, <3/Cl4-2,3,7,8-TCDD.*


* Subtract 0.0108 of any 257  response from the  263 response to correct for
  contributions of 2,3,7,8-TCDD to the 263 response.

-------
                                                                       l'rf 05 IS
                                 i  of.the  1on  m/z  268, <
                                 I. l3C12-2.3,7,8-TCOO.
- the area response  othe  1on m/z 268, corresponding to the
  Internal standard,
           Css « the concentration of the  surrogate  standard,  3  014-2,3,7,8-TCDD.

     and   Cjs « the concentration of the  Internal standard,   Ci2-2,3,7,8-TCDO.

     In the case of the surrogate standard,  37Cl4-2,3,7,8-TCDD,  the  variation
of the three RRF values for the high level calibration  solution  should not
exceed 101 RSO.  If this 1s the case, the  mean  of  the three RRFs shall be
used for concentration calculations.  The  overall  mean  Is  termed a calibration
factor.

     The calibration factor for the unlabelled  2,3,7,8-TCDD must be  verified on
each work shift of 8 hours or less by the  analysis of a low level calibration
standard.  If the RRF for the low level  calibration  differs from the calibration
factor by more than 101, the entire calibration must be repeated and a new
calibration factor determined.  The most recently  verified calibration factor
must be used in all calculations.  This  verification Is only  required for the
unlabelled standards.  There 1s no need  to check the surrogate calibration
factor unless the surrogate recoveries appear biased or consistently fall outside
the 60-140% control limits.

     The theoretical ratio of the m/z 257 to 259 ions  for native 2,3,7.8-TCDD
is 1.02.  However, in practice this ratio will  differ  from the theoretical  due
to the very low resolution used in both  analyzing quadrupoles for this  type of
analysis.  The'ratio must therefore, be  determined empirically as follows:

Equation Hit  (Ratio of native TCDO daughter Ions)

     Ratio • A257/A259

     where *2S7 * Area response for ion  m/z  257

           A259 * Area response for ion  m/z  259

     The mean of the ratios calculated for each of the nine  calibration
solutions is used for comparison purposes for qualitative identification of
2,3.7,8-TCDO.

     It has been found that the sample spiking solution also gives  responses
for the 257 and 259 daughter ions corresponding to 2,3,7,8-TCDD.  These
contributions must be subtracted out for each sample.   In order to  determine
this correction factor, add 150 ul of the sample spiking solution to a 5 ml
volumetric flask and bring to volume with dlchloromethane.  Twenty  1-2 ul
Injections of this solution must be made and the ratio of the area  responses
for the sum of the m/z 257 and 259 Ions  vs the m/z 268 1on must be  calculated.
Twenty separate ratios must be determined.

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                                                                    -'"" 05 i98.
 Equation  IV:  Blank Response (B) of Sample Spiking Solution

                     B  »Ab/A1s
         >
     where Ab • the sum of the area responses for the Ions, m/z 257 and 259,
                obtained with the spiking solution

     and   AfS « The area response of the 1on m/z 268, corresponding to the
           Internal standard l
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            W « 5 grams (the  weight  of  Met  soil  used  for each sample)

     The standard deviation of  the blank  responses  (1n concentration units)
must then be calculated.

Equation VII;  (Standard  Deviation of The Blank  Responses)

  1         SD •   (r Cb2) -  (I  Cb)2/n
                           n-1

   ' where Sb • standard deviation  of  the  blank  responses  (In units of ug/kg)

           Cb • blank response  1n concentration  units  (calculated using
                Equation VI)

            n « number of replicate blank  results  used (20 are  required)


     Finally, the limit of detection must  be  calculated from the standard
deviation of the blank.


Equation VIII;  {Limit of Detection Based  on  "Well-Known"  Blank)*

     LOO « 2 t Sb

     where LOD « Limit of Detection

             t • the 10% point  of the  t statistic  for a double-sided  table
                   with n-1 degrees of freedom (where n 1s equal to the  number
                   of blank results used).  NOTE:  The LOD  must  be calculated
                   based on at  least 20 replicate  blank (I.e. spiking solution)
                   analyses.  For n  « 20,  t • 1.72.

     The limit of detection calculated from equation VIII  should be less than
the required limit of detection of  0.3 ug/kg.

VIII.  QUALITY CONTROL REQUIREMENTS

     The following quality control  (Q.C.)  requirements are listed  In  the
order that they must be run.   Requirements 1 and 2 are to  be run  Initially
before any other samples.  Requirements 3 through 7 are the Q.C.  samples to
be Included with each batch of real samples (requirement 18) that  1s  run In
one 8-hour time period or on each shift.  The requirements 3 through  8 are to
be run 1n the order as they appear  In the list below on each shift.
*  Reference - Currle, Lloyd A. "Limits for Qualitative Detection and
Quantitative Determination' Anal, Chem., 40, 3, 586-S93, 1968
                                    11

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                                                                       ^ U5  191
     1.  An Initial  calibration must be performed  using calibration  standard
solutions with varied (1,5,  and 25 ug/kg equivalent) native TCDO  and 5  ug/kg
equivalent Internal  standard.   Calibration for the surrogate  standard will
be based only on the high level standard (1 ug/kg  equivalent).  The  criteria
given 1n Section VII must be met or the calibration must be repeated.

     2.  Initially,  20 replicate determinations of the spiking  solution must
be run and area responses for  the sum of m/z 257 and 259 Ions vs  the m/z 268
1op must be calculated.   Twenty separate ratios must be determined (Equation
IV) and used 1n calculating  the mean correction factor  (Equation  V).

     3.  A 1-point check verification using the 1  ug/kg equivalent native
TQDO and 5 ug/kg equivalent  Internal standard must be run  once  every 8  hours  or
on every shift.  If  the  RRF  values from this calibration check  differ by more
than + 10% from the  previously determined mean relative response  factor (RRFs),
the 3~point calibration  must be repeated.  The calibration check  for
the surrogate is not necessary unless the surrogate recoveries  appear biased
and/or consistently  fall outside the 60-140% control  limits.

     4.  A laboratory "method  blank" must be run along with each  batch  of 24
or fewer samples.  A method  blank is performed by  executing all of the
specified extraction steps,  except for the introduction of a  5  gram sample.
The method blank is also dosed with the internal standard  and surrogate
standard.  Results for the method blank must be calculated the  same way as
samples.  This  includes correction for the spiking solution contribution as
indicated in Equation IX.  A positive response ^ LOD (Equation  VlII)must be
followed by reinjection.  If still positive, re~extraction and  reanalysis of
all related samples must be  done.

     5.  "Field blanks" will be provided to monitor for possible cross-
contamination of samples 1n  the field.  The "field blank"  will  consist of
uncontaminated  soil  (background soil taken off-site).   A  positive response >.
0.1 ug/kg native TCOD must be  followed by  reinjection.   If still  positive, "
all samples associated with  the field blanks must be re-extracted and reanalyzed.

     6.  One  sample, designated by EPA, must be spiked with  native 2,3,7,8-TCDD
at a level of  1 ug/kg for each set of 24 or fewer samples.  The Field Blank
Spiking  Solution  (Section VI)  should be used to spike the  designated sample.
The  recovery  must be 0.6 to 1.4 ug/kg or the analysis stopped and all related
samples  must  be re-extracted and  reanalyzed.

     7.  The  laboratory will be given performance  evaluation samples by EPA
to run with each  batch  of samples.  The  results from these performance evaluation
samples  will  be evaluated by EPA.   If  a  result Is  not within the acceptance
criteria set  by EPA, all samples  in the  batch  associated with that PE sample
must be  reanalyzed.

     8.  Each  sample must be dosed with  50 ul  of the sample spiking solution
containing internal standard  (equivalent  to 5.0 ug/kg) and surrogate standard
 (equivalent  to 1.0  ug/kg).  The surrogate  recovery must be 0.6 to 1.4 ug/kg
or the sample must  be reanalyzed.
                                       12

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     9.  The following qualitative requirements  must be met  1n order to
confirm the presence of native 2,3,7,8-TCOD:
                                                       >
          a.  The retention time must equal  (within 3  seconds) the retention
time for the Internal standard.

          b.  The 257/259 ratio must be within the range  1 101 of the value
of the ratio determined in Section VII, (Equation III).   ~~

 '         c.  The ion responses at 257 and 259 must be present and maximize
together.  The signal to mean noise ratio must be 2.5  to  1 or better for both
daughter Ions.  (Determine the noise level by measuring the  random peak to
valley signal present on either side [within 20  scans] of the 2,3,7.8-TCDD
detention window.  The 2,3,7,8-TCDD signal must  be at  least  2.5  times larger
than this.)

          d.  For those samples giving non-detect results, the result must be
less than the 0.3 ug/kg required limit of detection.   Otherwise  the analysis
must be stopped and interferences identified and corrected until the 0.3
ug/kg required limit of detection is met.

          e.  For each sample, the Internal standard must be present with at
least a 10 to 1 signal to noise ratio based on the m/z 268 ion response.

IX.  SAMPLE COLLECTION, PRESERVATION AND HANDLING
             •
     The procedures for sample collection, shipping and handling will be
specified by the EPA Regional Office responsible for the  monitoring exercise.
The sampling team will be provided with an 8 ounce  glass  jar,  and  30-300  grams
of soil will be collected.  When received in the laboratory, the sample should
be thoroughly mixed in the jar for a minimum of  3 minutes, using a  stainless
steel spatula.  The spatula should be used to  break up large clumps of soil
while mixing to achieve a homogeneous sample.

     A 5 gram aliquot sample should be taken and placed  in a pre-weighed  10 ml
serum vial containing approximately 5 grams of anhydrous  sodium  sulfate
together with a Teflon-faced septum and cap (The entire  vial, NagSO^  septum
and cap is pre-weighed and labelled).  The 5 gram aliquot sample should be
representative of the entire sample.  Thus, large stones  or  other  particles
which are uncharacteristic of the sample, should not  be  included in the
aliquot.

     Samples may be stored under ambient  conditions as long as temperature
extremes (below freezing or above 90°F) are avoided.   Samples must be  protected
from light to avoid photodecomposition.

     All samples must be extracted and completely analyzed within 24 hours.
Extracts must be held for 6 months prior  to disposal.

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X.  SAMPLE EXTRACTION

     CAUTION:   Although  the  sample and standards  are  sealed  throughout the
extraction procedure, there  is  always  the  possibility of  leakage  and  breakage
(especially during the sample spiking  and  centHfuging steps).  The analyst
should, therefore, be fully  protected  by wearing  plastic  gloves and laboratory
jacket (a face protector 1s  optional). See Section  IV for details on specific
safety requirements.

     1. Prepare extraction solvent by  mixing two  volumes  acetonltrile with  one
volume dichloromethane.  Mix  solvents thoroughly.

     2.  Weigh the sample vial  and determine the  net  weight  of  sample (to 3
significant figures).

     3.  Add 50 ul of the sample spiking  solution (containing both  internal
and surrogate standards).  The solution will contain 0.5  ng/ul  of internal
standard and 0.1 ng/ul of surrogate standard.  Add the 50 ul solution directly
to the soil, spreading 1t over several sites on the  surface  of  the  soil.

     4.  Attempt to mix the soil and sodium sulfate  by shaking.  (Extremely
wet samples may not mix well, but DO NOT  open the vial to stir the  contents.)
Additional anhydrous sodium sulfate should be added  if needed.


     5.  Pierce the septum with a disposable needle  and leave the needle in
place  to vent -the contents while the extraction solvent Is Introduced.

   •  6.  Add 5 ml of the 2:1 acetonltrile: dichloromethane extraction solvent
using  a  5 ml syringe and disposable needle.  Retain the syringe for solvent
additions only.

     NOTE:  Additional extraction solvent can be added 1f the analyst judges
this necessary to achieve efficient extraction on a particular sample.

      7.  Remove the  syringe  and both  needles (they should be treated as
though contaminated). Dispose  of  both needles.

      8.   Shake the vial  vigorously  on a vortex mixer  for  2 minutes.

      9.   Centrifuge  the  vial and  contents  at 4000 rpm for 2 minutes.  Remove
carefully  so  as  not  to  disturb the  sediment.

     10.   Insert  a needle through  the  septum so that  it just breaks the  surface
of the septum Inside the vial.  Using a clean disposable  syringe and needle,
withdraw approximately  1 ml  of the  extract;  NOTE: The other needle through the
 septum serves to equilibrate the  pressure upon withdrawal of the extract.

      11.  Invert the syringe and withdraw the plunger to  remove  the  extract
 from the needle.  Dispose of the needle  (1t 1s contaminated).

      12.  Place  a 0.45 micron  disposable  Teflon  filter on the  syringe and  •
 the extract into a clean 10 ml serum vial containing 9 ml distilled  water.
 Dispose of the syringe and  the filter.

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                                                                          05 19


     13. Using a Teflon lined septum ind an aluminum cap, cover and crimp the
vial containing the Mater-extract mixture.

     14. Manually shake the vial vigorously for  about  one minute.

     15. Centrifuge the vial to separate the dichloromethane phase from the
water/acetonltrlle phase.  The dichloromethane phase will appear as a small
bubble at the bottom of the vial.

     16. Prepare a miniature drying tube as follows:

         a. Plug the tip of a disposable plpet with a  small amount of silanized
            glass wool.

         b. Add approximately 1/2 cm anhydrous sodium  sulfate.

     17. With a disposable syringe and needle, remove  the dlchloromethane phase
from the vial (step IS) as completely as possible.

     18. Transfer the dlchloromethane phase through the  drying  tube Into a clear
1 ml serum vial.

     19. Rinse the drying tube with one-half ml  dlchloromethane, and collect
1n the same 1 ml serum vial.

     20. Under a stream of nitrogen, evaporate the  solvent  gently  until the
volume of solution remaining in the serum vial 1s 0.05-0.1  ml.

     21. Seal the 1 ml serum vial with a Teflon  lined  septum  and cap. Label  the
vial appropriately.

XI.  CLEANUP

     The need for cleanup 1s indicated when a particular extract does not  meet
the QC criteria for the coelution of all four monitored  ions, surrogate recover
or the ratio A257/A250.  Two cleanup procedures  are given below.

A.   Modified Option A Cleanup

     1. Plug the tip of a disposable plpet with  a small  amount  of  silanized
        glass wool.

     2. Place approximately a 1 cm layer of silica  gel over the glass wool.

     3. Place approximately a one-half cm layer  of  anhydrous  sodium sulfate
        over the $111ca gel.

     4. Plug the tip of • second disposable plpet with a small  amount  of
        silanized glass wool.

     5. Place approximately 0.5 cm add alumina over the sllanired glass  wool.

     6. Place approximately 0.5 cm anhydrous sodium sulfate over the alumina.
                                  15

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     7. Arrange the two columns so  that  the  silica  gel column will elute onto
        the alumina coluon,  and the alumina  column  drippings will be collected
        In a vial.

     B. Rinse the two columns with  0.5 ml  cyclohexane  and discard the eluate.

     9. Open the vial containing the  extract and  add 1 ml cyclohexane to the
        extract.
»

 (   10. Under a stream of nitrogen, carefully evaporate  the dichloromethane fro
        the extract vial  (the volume  of  the  remaining  solution should be just
        under 1 ml).

    11. Transfer the entire  contents  of  the  extract vial onto the silica column
        arranged as specified in step 7.

    12. When the solution just  reaches the surface  of  the sodium sulfate layer
        In the silica gel column, add 0.5 ml  cyclohexane.

    13. Repeat step 12 a second time. Allow the  solution to drip completely
        after the second addition of  cyclohexane.

    14. Discard the silica gel  column.

    15. Rinse the alumina column with an additional 1  ml cyclohexane.   Discard
        the accumulated eluates in  the  vial  beneath the  column.

    16. Place a clean 1 ml serum  vial under the alumina  column.

    17. Elute the alumina column with three successive portions  of  0.5  ml  each
        of 15% by volume dichloromethane 1n cyclohexane, collecting the eluate
        in the clean vial.

    18. With gentle heating and under a  stream of nitrogen,  evaporate the  solv<
        until the volume in the vial  1s  0.05-0.1  ml.

    19. Seal the serum vial  with  a  teflon lined septum and  cap.  Label  the vial
        appropriately.  NOTE:   If  1t  is  a priori  known that  the  second  step  of
        cleanup is  required, evaporate  the sample in stage  18  to just below
        1 ml and Immediately proceed with a second cleanup  as  described below.

B. Option D Cleanup

     1. In advance,  prepare a mixture of 3.6 g Carbopack C  with  16.4 g  Celite
        545.  Activate the mixture  at 130°C for 6 hours.

     2. Plug the tip of  a disposable pipet with a small  amount of  silanized  gl<
        wool.

     3. Place 2 cm layer  of the carbopack-Celite mixture over  the  glass wool
        plug, using suction to pack the column.
                                   16

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      4. Rinse the column sequentially  with 2 ml toluene. 1 ml dlchloromethane-
         methanol-benzene (75:20:5 by volume), 1 ml cyclohexane-dlchloromethane
         1:1  by volume),  and finally 2  nl cyclohexane.  Collect the eluate 1n a
         vial  and  discard the eluate.

      5. Dilute the extract  which has been cleaned up by the Modified Option A
         procedure to 1 ml with  cyclohexane.
 •
 t    6. Maintaining a discard vial under the column. Introduce the extract
         onto  the  column.

      7. After the solvent has drained, rinse the column successively with 2 ml
         cyclohexane,  1 ml cyclohexane-dichloromethane mixture (1:1 by volume)
         and  1 ml  dlchloromethane-methanol-benzene mixture (75:20:5 by volume).

      8. Allow the column to drain completely and discard the accumulated eluate

      9. Place a clean serum vial  under the column.

     10. Elute the dloxin from the charcoal with 2 ml toluene.

     11. With  gentle heating and under  a stream of nitrogen, concentrate the
         extract to a  volume of  0.05-0.1 ml.

     12. Seal  the  serum vial  with a Teflon lined septum and cap. Label approprij

 XII.  GC/MS/MS ANALYSIS

      1. Table 1  summarizes the 15 m D8-5 gas chromatographic capillary
 column  and operating  conditions.  The  15 m DB-5 column has been us«d for
 chromatography which  Is  not Isomer specific (no valley 1s observed between the
 1,2,3,4-TCDD  and  2.3,7.8-TCDD Isomers).

      2.  Standards  and samples  must be analyzed under Identical MS/MS
 conditions.   Selected Reaction  Monitoring (SRM) scans are used, using a scan
 time  to give  at least five  points per chromatographic peak.  Recommended
MS/MS conditions  are  given  1n Table 2.

      3.  Verify the  Calibration  of the system daily as described 1n Section
 VII.  The volume  of calibration  standard Injected should be approximately the
 same  as  all sample  injection volumes.  The requirements described In Section
 VIII. Parts 9b and  9c must  be met for all calibration standards.

  -   4.  Inject a  1 to 2 ul  aliquot of the sample extract.
•
     5.  The  presence of TCOO Is qualitatively confirmed If the criteria of
Section  VIII,  Part  9, are achieved.
     6.  For quantltatlon, measure the area response of the m/z 257 and
peaks for 2.3.2.8-TCDD; the m/z 268 peak for "Cl2-2.3,7,8-TCOO. and the
263 peak for */Cl4-2.3.7,8-TCOO.  Calculate the concentrations df nativi
                                                                        259
                                                                     the m/z
                                                                      ve and
surrogate standards using the following equations:
                                    17

-------
                                                                           05


Equation IX: (Calculation of concentration of native 2,3,7,8-TCDD)

                  «) - C.F.)
                RRFs x M

where Cs » The concentration of native 2,3,7,8-TCDD in ug/kg

      AS * the sum of the area responses for the Ions, m/z 257 and 259

         • the area response for the ion m/z 268
     C.F. • correction factor for spiking solution (blank) previously determined
            (Equation V)

     Qfs • quantity (1n nanograms) of 13Ci2"2.3,7,8-TCDD added to the sample beft
           extraction

     RRFS « Relative response factor for 2,3,7,8-TCDO calculated previously
            (Equation I)

       W * weight (fh grams) of wet soil or sediment sample.

     In evaluating the results* a distinction must be made between quantitative
measurement and qualitative Identification of 2,3,7,8-TCDO.  The following steps
must be followed In the treatment of all sample results:

     1.  Calculate the concentration of native 2,3,7,8-TCDD using equation IX.

     2.  Determine 1f all of the qualitative Identification criteria are met.

     3.  If all qualitative Identification criteria are met, report the
concentration  found by equation IX, regardless of concentration.

     4.  If the qualitative Identification criteria are not met, and the
concentration  calculated  by equation IX 1s less than the required limit of
detection of 0.3 ug/kg, report the concentration as less than 0.3 ug/kg (I.e.
<0.3 ug/kg).

     5.  If the qualitative Identification criteria are not met, and the
concentration  calculated  by equation IX 1s greater than the required limit of
detection of 0.3 ug/kg, the extract must be  reinjected.  If the qualitative
Identification criteria are still not met and the result 1s still greater than
0.3 ug/kg, the extract must be cleaned up or the sample reanalyzed until a
satisfactory result 1s obtained,   (i.e. positive result or negative  result
below  0.3 ug/kg).

NOTE:   In  reporting results for sample analysis, a comparison is made with
the required  Unit of detection.  The  limit  of detection based on the blank
 (Equation  VIII) might also  be used,  but  interferences may be present and
introduce  false positives in some cases.  However, as explained 1n Section
VII,  the empirical  limit  of detection  based  on the blank must be less than
the required  limit  of detection of  0.3 ug/kg.
                                       18

-------
Equation X:  (Calculation  of concentration  of surrogate standard, 37Cla-
~*	        2.3,7,8-TCOO)

            Ass x Q1s
     ^SS •	5,5,	JT
            AJJ x RRFjj  x W

     where Css « the concentration  of surrogate standard 37Cl4-2,3,7,8-TCDD
                 in ug/kg.

           Ass « the area response  for the  1on m/z 263*

           *is * tne area response  for the  ion m/z 268
                                            "'•I

                                                37,
- quantity (in nanograms)  of  13C12-2,3,7,8-TCDD added to the
  sample before extraction.
           RRFSS » Relative response factor for    C14-2,3,7.8-TCDD  calculated
                   previously (Equation II).            _ .

            W « Weight (in grams) of wet soil  or sediment  sample.

*  Subtract 0.0108 of any 257 response from the  263 response  to correct for
contributions of any 2,3.7,8-TCDD to the 263 response.

     Native 2,3,7,8-TCOO contains an innate quantity of 37Cl4-2,3,7,8-TCDD.
Except at high concentrations of native 2,3,7,8-TCDD, this contribution is
too small to significantly affect the calculated concentration of  surrogate
  Cl4-2,3,7,8-TCDD.  The theoretical correction  Is calculable on the basis of
isotope distribution and amounts to 1.08% of the m/z 257 peak.  (This correction
should be checked at low resolution by analyzing about  200 pg/ul of unlabelled
2,3,7,8-TCDD.)  On this basis, the correction to the area  count of the surrogate
is made as follows:

     A263 « *263 ' °-0108 A257

     Calculate the analytical percent recovery of the surrogate standard.

     Surrogate          amount measured* (nanograms) X  100
     Analytical      «            5 ng
     Percent Recovery

    * NOTE:  The amount measured is equal to the concentration found by
equation X multiplied by the weight of soil used for the sample (I.e., Css x
W).

XIII.  METHOD PERFORMANCE

     The required detection  limit for this  method 1s 0.3 ug/kg.  For certain
samples, this detection limit may not be achievable because of Interferences.
These samples require cleanup as described  in Section XI.  This method has
been compared with the EPA-IFB GC/MS Method for 2,3,7,8-TCDD  and found to  be
applicable to analyses of  soils where 2,3.7,8-TCDD  1s the only tetrachloro
isomer known to be present.


                                19

-------
          >             TABLE I
OPERATING CONDITIONS FOR DB-5 GAS CHROMATOGRAPHY  COLUMN
 COLUMN
 Length
 I. D.
 Film Thickness
 2,3.7,8-TCDD R. T. (approx.)
 Carrier gas
•»
 Initial Temperature
 Initial Time
 Splitless Time
 Program Rate
 Final Temperature
 Split Flow
 Se   urn Purge Flow
 Capillary Head Pressure
 Transfer Line Temperature
 DB-5
 15 m
  0.32 mm
  1.0 micron
  5-6 min.
  N2
  150°C
  l.U min.
  1.0 min.
 20°C/min.
240»C
20 ml/min.
 0.6 ml/min.
   8 psi
240°C
                            20

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                                   TABLE 2
                          MS/MS OPERATING CONDITIONS
Instrument
Ion Source
CI Reagent Gas
Reagent Gas Flow
Source Temperature
Discharge Current
Ql Resolution
Q3 Resolution
Collision Energy (LAB)
Collision Gas
Collision Gas Thickness
TAGA* or TAGA« 6000E
Townsend/glow discharge  CI
Zero grade air (H? and He free)
35 ^  ml/min.
200 *C
•1 mA
3 amu at 501 peak  height at  m/z  * 320 (singl<
3 amu at 501 peak  height at  m/z  * 320 (singl<
55eV [(OR * GR)/2-R2] or 55eV (OR - R2)
Ar
400 x 1012 molecules/cm2
Ions Monitored:
                                    320      257 (native-TCOD)   '
                                    322      259 (native-TCDD)
                                    328      263 (surrogate standard)
                                    332      268 (internal standard)
                                    21

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XIV.  DATA REPORTING

     Report all data 1n units  of mlcrograms per kilogram of wet  soil.   Use
three significant figures at concentrations above 1 ug/kg and  2  significant
figures at concentrations below 1 ug/kg.  The data package must  Include the
following Information:

     1.  Individual and mean response factor for the three-point calibration
of unlabelled 2,3,7,8-TCDD.   (Based on High level standard only).

     2.  Individual and mean response factors for the Isotopic surrogate
standard (based on high level  standard only).

     3.  The Individual ratios of the sum of areas 257 and 259 ions to the
268 ion for 20 replicate measurements of the blank (I.e.. sample spiking
solution), and the mean Correction Factor based on these ratios.

     4.  The empirical  limit of detection based on the 20 blank  measurements

     5.  The daily or shift  verification of the mean response  factors.

     6.  The percent accuracy  I.e., (analytical percent recovery)  for  the
surrogate standard.

     7.  The result for the  method blank.

     8.  The percent recovery  of native TCDO from the spiked sample.

     9.  The result- for the  PE sample

     10.  The result for the field blank.

     11.  The data filename  (to facilitate data retrieval).

     12.  The sample identification number (as assigned by the field samplin
team).

     13.  Analytical date and  time.

     14.  The area responses for ions 257, 259, 263, and 268.

     15.  The observed response ratio of Ions 257/259 for the  sample.

     16.  The calculated value for native 2,3,7,8-TCDD.  (Values above or
below 0.3 ug/kg are to be reported only If qualitative Identification  criter
are met.)

     17.  If no 2,3,7,8-TCDD was detected, report "not detected" or N.D. and
the 0.3 ug/kg required detection limit.

     18.  The mass chromatograms for all samples and standards.   Include t
the real-time display data and reduced data showing limits of  integration.
Include any computer generated response tables.

-------
                                                                          5 1981
     19.  The weight of the original wet sample aliquot.
     20/* Documentation on the source and history of the  native and  labelled
2,3,7,8-TCDO standards used.
     21.  Any other supporting documentation.  An example of the required
.data format follows:
                                     23

-------
INITIAL  CALIBRATION SUMMARY \
Data
File Name
Sample
I.O.f
Analysis
Date 1 Time
Un labeled (Native)
2,3.7,8-TCDO
Equiv. I
Cone" 1 RF
Mean
RF
Surrogate . •
2,3,7.8-TCDD
Equiv.
Cone"
RF
Mean
RF

-------
DAILY OR SHIFT CALIBRATION VERIFICATION
Data
File Name
Sample
I.D.I
Analysis
Date I Time
Unlabeled (Native)
2,3,7,8-TCDD
RF
l Difference
from Mean RF
              25

-------
BLANK RESPONSE SUMMARY
Number
Data
File Name
Sample
I.D.I
Analysis
Date Time
Response Areas
257 | 259 | 268
Blank Response (B)
257 * 259
26B
Equivalent tone"
of 2.3.7.8-TCDD"
                                                                     c
                                                                     c
                                                                     2

                                                                     C
                                                                    cr

-------
Calculations;
* Note:  The equivalent concentrations  of 2,3,7,8-TCOO  (last column) are calculated using Equation VI
     CD ' *b * Qls
     Other calculations required are:
          1.  Equation V:  Correction  Factor  (C.F.) for Blank Contribution
               C. F. • r B
                         n
          2.  Equation Vll;   (Standard  Deviation of  the Blank Responses)
               SD •  ( t Cb2 ) - (E Cb)2/n           '   '	
                               n-1
          3.  Equation VIII;   (Limit  of  Detection based on  "Well Known" Blank)
          LOG - 2 * t " SD •   	.
                                                     27
                                                                                                                 cn
                                                                                                                 CO
                                                                                                                 00

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                                                 TCDD DATA REPORT FORN
Lab:
Case No.:
                                                                                          Report Date:
   Data
File Name
  Analysis
Date   Time
                                          Aliquot        Response Areas
£
Ib
                                        Wet *t.  (q)   Z57  259  263   268   257/259   uq/kq TCDD
 Surrogate
ug/kq  tAcc.  Comments
MB - Method Blank
FB • Field P
                                                    N - Native TCUO Spike
                                                   DL « DeterMon Limit
                                                   Nn • Nnt    »rt**rf
                                                                                            cn

                                                                                            CD
                                                                                            CX7

-------
     Add i 1 1 'Mini r  rcnti 1 1 cHrnt s must  furtmlr  I'll-  usi1 ->r  fdrrt.il  ch.iiti
n(' custody nn
-------
                               APPENDIX D
                      DRAFT ASME SAMPLING PROTOCOL

         •SAMPLING FOR THE DETERMINATION OF CHLORINATED ORGANIC
                      COMPOUNDS  IN  STACK EMISSIONS-

                           DRAFT, OCTOBER 1984
1430J C3044-A

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           SAMPLING FOR THE DETERMINATION OF CHLORINATED
               ORGANIC COMPOUNDS IN STACK EMISSIONS
1.  PRINCIPLE AND APPLICABILITY

    1.1 Principle;    Stack gases that may contain chlorinated
        organic compounds are withdrawn from the stack using a
        sampling train.  The analyte is collected in the sampling
        train.  The compounds of interest are determined by
        solvent extraction followed by gas chrooatography/mass
        spectroscopy (GC/MS).

    1.2 Applicability;   This method is applicable for the deter-
        mination of chlorinated organic compounds in stack emis-
        sions.  The sampling train is so designed that only the
        total amount of each chlorinated organic compound in the-
        stack emissions may be determined.  To date, no studies
        have been performed to demonstrate that the particulate
        and/or -gaseous  chlorinated organic compounds collected in
        separate parts  of the sampling train accurately describes
        the actual partition of each in the stack emissions.  If
        separate parts  of the sampling train are analyzed separ-
        ately, the data should be included and so noted as- in
        Section 2 below.  The sampling shall be conducted by
        competent personnel experienced with this test procedure
        and cognizant of intricacies of the operation of the
        prescribed sampling train aod constraints of the analyti-
        cal techniques  for chlorinated organic compounds, especi-
        ally PCDDs and  PCDFs.

        Note:  This method assumes that the XAD-2 resin collects
        all of the compounds of interest from the stack emissions.
        Since the method at the present time has not been vali-
        dated in the presence of all the other components present
        (HC1, high organic load) in the stack emission, it is
        recommended that appropriate quality control (QC) steps be
        employed until  such validation has been completed.  These
        QC steps aay include the use of a backup resin trap or the
        addition of a representative labeled standard (distin-
        guishable from  the internal standard used for quantita-
        tion) to the filter and/or the XAD-2 in the field prior to
        the start of sampling.  These steps will provide informa-
        tion on possible breakthrough of the compounds of inter-
        est.

2.  REPORTABILITT

    Recognizing that modification of the method may be required
    for specific applications, the final report of a test where
    changes are made shall include:  (1) the exact modification;
    (2) the rationale for the modification; and (3) an estimate of
    the effect the modification will produce on the data.

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i
i
t
                                                                         DR
              3.   RANGE  OF  MINIMUM  DETECTABLE  STACK GAS  CONCENTRATION
jj                The range of the analytical method  may  be  expanded  consider-
,T*                ably through concentration and/or dilution.   The total  method
•                  sensitivity is also highly dependent  on the  volume  of  stack
M                gas sampled and the detection limit of  the analytical  finish.
.^                The user shall determine for their  system  the minimum  detect-
                  able stack gas concentration for the  chlorinated organic con-
•                  pounds of interest.  The minimum detectable  stack gas  concea-
Tj                tration should generally be in the  ng/m  or  lower range.

              4.  INTERFERENCES

;/f.                Organic compounds other than the compounds of interest may
                  interfere with the analysis.  Appropriate  sample clean-up
;  '                steps shall be performed.  Through all  stages of sample
II                handling and analysis, care should be taken to avoid contact
~                of samples and extracts with synthetic  organic materials oth
•                  than polytetrafluorethylene (TPE*).  Adhesives should not be
;-|                used to hold TFE* liners on lids (but,  if  necessary, appro-
3                priate blanks must be run), and lubricating and sealing
                  greases must not be used on the sampling train.

J            5.  PRECISION AND ACCURACY

                  Precision and accuracy measurements have not yet been made
j|                PCDD and PCDF using this method.   These measurements are
1                needed*  However, recovery efficiencies for source.samples
                  spiked with compounds have ranged  from 70 to 120Z.  '

              6.  SAMPLING RONS. TIME, AND VOLUME

                  6.1  Sampling Runs;  The number of sampling- runs must be
                  sufficient  to provide minimal statistical data  and  in no
                  case shall  be less than three (3).

                  6.2  Sampling Time;  The  sampling  time must  be  of  sufficien
                  length to provide coverage of the  average operating conditi
                  of the source.  However,  this shall not be  less  than  three
                  hours (3).

                  6.3  Sample Volume;  The  sampling  volume  must  be sufficient
                  provide  the required amount  of  analyte to aeet  both the HDL
                  the analytical finish and  the allowable stack  emissions.   I
                  may be calculated using the  following  formula:

                                 ,   „ ,       .   100   100   1
                             Sample Volume -Ax  -  x-—r— x TT



                   A •  The analytical MDL  in  ng
                   B -  Percent (Z) of  the  sample required  per analytical f
                        run
                   C »  The sample  recovery (Z)
                                             A-2

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                                                            DRAFT
     D -  The allowable stack emissions  (ng/m )

     Example:  A - 0.050 ng; B - 10Z;  C  - 50Z;  and D - 1  ng/m


                   « «c   100   100   1    .  3
              SV - 0.05 x -JQ x -^ x  y  - 1m


7.  APPARATUS

    Sampling Train:   The train consists  of nozzle, probe,  heated
particulate filter,  and sorbenc module followed  by four impiogers
(Fig. 1).  Provision is made for the addition of (1) a cyclone  in
the heated filter box when testing sources emitting high  concen-
trations of particulate matter, (2) a  large  water trap between  the
heated filter and the sorbent module for stack gases with high
moisture content, and (3) additional implngers  following  the
sorbent module.  If  one of the options is utilized, the option
used shall be detailed in the report.  The train may be construct-
ed by adaption of an EPA Method 5 train.  Descriptions of the
sampling train components are contained  in the  following  sections.

7.1.1  Nozzle

    The nozzle shall be made to the specifications of EPA Method
5.  The nozzle may be made of nickel plated  stainless steel,
quartz, or boro-silicate glass.

7.1.2  Probe

    The probe shall  be lined or made of  TFE*, borosilicate,  or
quartz glass.  The liner or probe extends past the retaining  nut
into the stack.  A temperature controlled jacket provides protec-
tion of the liner or probe.  The liner or probe  shall be*equipped
with a connecting fitting that Is capable of forming a leak-free,
vacuum-tight connection without sealing  greases.

7.1.3  Sample Transfer Lines (optional)

    The sample transfer lines, if needed, shall  be heat traced,
heavy walled TFE9 (1.3 cm [1/2 la.] O.D. x 0.3 cm [1/8 In.]  wall)
with connecting fittings that are capable of forming leak-free,
vacuum-tight connections without using sealing greases.  The  line
should be as short as possible and must  be maintained at  120°C.

7.1.4  Filter Holder

    Borosilicate glass, with a glass frit filter support  and a
glass-to-glass seal or TFE* gasket.  A rubber gasket shall not  be
used.  The holder design shall provide a positive seal against
leakage from the outside or around the filter.  The holder shall
be attached immediately at the outlet  of the probe (or cyclone, if
used).
                                A-3
                                         Rr ...

-------
                  Vi.
                                                             .
                                                   .^—. Nt.n — -.«.Z_^L
 I
                                         I »
                                                                            DP'
i
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  >    *_ \
•fL-,  *^«  \';'T'*-i-iip.
J.^.../.....V^4i
               L~1=sru''BL   «•
                        w^
                        Z?F
                      Fif. 1  Modified E?A Method 5 Train'for Ori»nics Saspliag
                      Source:  Kechoda Manual Saopliof and Analysis  Procedure*
                        for Assessing Organic* Inissiena froa Stationery Con-
                          bust ion Sources in Exposure lvalo»tion Division
                           Studies, U.S. Znvironaental Protection Agency
                             leport Ko. r?A-560-82-OlA (January 1982).
                                              A-4

-------
F
     7.1.5   Cyclone  in  Filter  Box  (optional)

         The  cyclone shall  be  constructed  of  borosilicate  glass  with
     connecting  fittings  that  are  capable  of  forming  leak-free,
     vacuum-tight  connections  without  using sealing greases.

     7.1.6   Filter Heating  System

         The  heating system must be  capable of  maintaining  a  tempera-
     ture around  the filter holder (and  cyclone,  if used)  during sampl-
     ing  of  12(H14°C (248+25°F).   A  temperature gauge  capable  of
     measuring  temperature  to  within 3°C (5.4°F)  shall be  installed so
     that the temperature around the filter holder  can be  regulated and
     monitored  during sampling.

     7.1.7   Solid  Sorbent Module
     used  as  the  sorbent.   The  sorbent  module  shall  be  made  of  glass
     with  connecting  fittings that  are  able  to  fora  leak-free,  vacuum-
     tight  seals  without use  of  sealant greases  (Figs.  2  and  3).   The
     XAD-2  trap must  be in  a  vertical position.   It  is  preceded by a
     coil-type  condenser, also  oriented vertically,  with  circulating
     cold  water.  Gas entering  the  sorbent module must  be maintained at
     <_20°C (68°F).  Gas temperature shall  be monitored  by a  thermo-
     couple placed  either at  the  inlet  or  exit  of the sorbent  trap.
     The sorbent  bed* must be  firmly packed and  secured  in place to
     prevent  settling or channeling during sample collection.   Ground
     glass  caps  (or equivalent)  must be provided  to  seal  the  sorbent-
     filled trap  both prior to  and  following sampling.  All  sorbent
     aodules  must be  maintained  in  the  vertical  position  during sampl-
     ing.

     7.1.8  lapingers

        Four or  more impingers  with connecting  fittings  able  to  fora
     leak-free, vacuum-tight  seals  without sealant .greases when con-
     nected together, shall be  used. All  impingers  are of the
     Greenburg-Smith  design modified by replacing the tip with  1.3 cm
     (1/2  in.)  ID glass tube  extending  to  1.3  cm  (1/2 In.) from the
     bottom of  the  flask.

     7.1.9 Metering  System

        The  metering system  shall  consist of  a  vacuum  gauge,  a leak-
     free  pump,  thermometers  capable of measuring temperature  to  within
     3  C (-5  F),  a  dry gas  meter with 2 percent  accuracy  at  the
     required sampling race,  and related equipment,  or  equivalent.

     7.1.10  Barometer

        Mercury, aneroid,  or other barometers  capable  of measuring
     atmospheric  pressure  to  within 2.2 Eg (0.1  in.  Eg) shall  be  used.
                                    A-5

-------
                                                                D
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                                  OS •«.?••'71-4 •• I
   tfri 2f.  Aeetpeablc iorbenc codulc design

-------
                                      Flow DIrtcllon
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-------
                                                                         DR
./'A
 1            7.2  Sanple Recovery,  Supplies,  and  Equipment

'4            7.2.1  Ground Glass Caps  or Hexane  Rinsed  Aluminum  Foil
%                           ^^^^^         ^^"^^      ™^~^^ - — -    '     ^^—^»™«

 *                To cap off adsorbent  tube and  the  other  sample-exposed  por-
             tions of the train.  If TFE* screw  connections  are  used,  Chen TFE*
             screw caps shall  be used.

**            7.2.2  Teflon FEP* Wash Bottle
|                                :	
r4                Three 500 ml,  Nalgene No. 0023A59, or  equivalent.

•4            7.2.3  Probe and  Transfer Line  Brush

 I                Inert bristle  brush with stainless steel  rod-handle of  suffi-
             cient length chac  is compatible  with the liner  or probe and trans-
             fer line.

1
.-*            7.2.4  Filter Storage  Containers
                 Sealed  filter  holder  or precleaned,  wide-mouth  amber  glass
             containers  with TFE*-lined screw caps  or wrapped in hexane  rinsed
             aluminum foil.

             7.2.5   Balance

                 Triple  beam, Ohaus  model 7505,  or  equivalent.

             7.2.6   Aluminum Foil

                 Heavy duty,  hexane-rinsed.

             7.2.7   Preeleaned  Metal Can

                 To  recover  used silica gel.

             7.2.8   Preeleaned  Graduated Cylinder,  e.g.,  250 ml

                 250 ml, with 2 ml graduations,  borosilicate glass.

             7.2.9   Liquid Sample Storage Containers

                 Frecleaaed  nmber glass bottles  or  clear  glass  bottles vrapped
             in opaque material, 1 L,  with TFE*-lined screw cape.

             8.   REAGENTS

             8.1  Sampling

             8.1.1   Filter — Fiberglass Reeve-Angel  934  AH or Equivalent

                 Prior co use la Che field, each lot  of  filters  shall  be sub-
             jected  co precleaning and a quality control  (QC) contamination
             check co confirm chac there are  ao  contaminants present that will
                                            A-8

-------
Tl                                                                 DRAFT
     interfere  with  the  analysis  of  analyte at the  target detection
     limits.

         If performed, filter  precleaning shall consist of Soxhlet
     extraction,  in  batches  not to exceed 50 filters, with the sol-
     vents)  to  be applied to  the field samples.  As a QC check, the
     extracting  solvent(s) shall  be  subjected to the same concentra-
     tion, cleanup and analysis procedures to be used for Che field
     samples.  The background  or  blank value observed shall be con-
     verted to a  per filter  basis and shall be corrected for any
     differences  in  concentration factor between the QC check (CFQC)
     and  the  actual  sample analysis  procedure (CF ) .             "
        where:

               CF - Initial volume of extracting solvent
                    Final Volume of concentrated extract

        The quantitative criterion for acceptable filter quality will
    depend on the detection limit criteria established for the field
    sampling and analysis program.  Filters that give a background or
    blank signal per filter greater than or equal Co the target detec-
    tion limit for the analyte(s) of concern shall be rejected for
    field usel  Note that acceptance criteria for filter cleanliness
    depends not only on the inherent detection limit of Che analysis
    method but also on Che expected field sample volume and on the
    desired limit of detection in Che sampled stream.

        If the filters do not pass Che QC check, they shall be re-
    excracced and Che solvent extracts re-analyzed until an acceptably
    low background level is achieved.

    8.1.2  Amberlite XAD-2 Resin

        The cleanup procedure may be carried out in a giant Soxhlec
    extractor, which will contain enough Amberlite XAD-2* resin
    (XAD-2) for several sampling traps.  An all glass Chimble 55-90 mm
    OD x 150 mm deep (top Co frit) containing an excra coarse frit is
    use£—fret—e*A^«ccion of XAD-2.  The fric if recessed 10-15 mm above
       renelateduring at Che bottom of the Chimble Co facilieaee
    drTluajje.  The XAD-2 muse be carefully retained ia Che extractor
    cup with a glass wool plug and stainless steel screen since it
    floacs on methylene chloride.  This process involves sequencial
    excraccion in che following order.

           Solvent                    Procedure

       Wacer                Inieial rinse with 1 L H-0 for 1 cycle,
                            Chen discard HO
                                   A-9


                                  'v'?'^> \

-------
                                                               DHf;
                                                               ^f i \
                                                               ivr
   Water

   Methyl alcohol

   Methylene chloride

   Hexane
Extract with H-0 for 8 hr

Extract for 22 hr

Extract for 22 hr

Extract for 22 hr
The XAD-2 must be dried by one of the following techniques.

(a) After evaluation of several methods of removing residual
solveot, a fluidized-bed technique has proven to be the caszssc
and most reliable drying method.

    A simple column with suitable retainers as shown in Fig. 4
will serve as a satisfactory column.  A 10.2 ca (4 in.) dianeter
Pyrex pipe 0.6 m (2 ft. long) will hold all of the XAD-2 from the
Soxhlet extractor, with sufficient space for fluidizing the bed
while generating a minimum XAD-2 load at the exit of the coluan.

    The gas used to remove the solvent is the key to preserving
the cleanliness of the XAD-2.  Liquid nitrogen from a regular
commercial liquid nitrogen cylinder has routinely proven to be a
reliable source of large volumes of gas free from organic concaa
nants.  The liquid nitrogen cylinder is connected to the column
a length of precleaned 0.95 ca (3/8 in.) copper tubing, coiled
pass .through a heat source.  As nitrogen is bled from the cyll
der, it is vaporized in the heat source and passes through  the
column.  A convenient heat source is a water bath heated from a
steam line*  The final nitrogen temperature should only be  war:
the touch and not over 40 C.  Experience has shown that about 5
g of XAD-2 may be dried overnight consuming a full 160 I. cylind
of liquid nitrogen*

    As a second choice, high purity tank nitrogen may be used c
dry the XAD-2.  The high purity nitrogen must  first be  passed
through a bed of activated charcoal approxiaately  150 mL in
volume.  With either type of drying method,  the  rate of flow
should gently agitate the bed.  Excessive  fluidation may cause
particles to break up.

(b) A* an alternate, if the nitrogen process  is  not available,
XAD-2 aay be dried in a vacuum oven, if  the  temperature never
exceeds 20°C.

    The XAD-2, even if purchased clean, mast  be  checked for *>'
methylene chloride and hexane residues,"plus  noraal blanks  be
use.

(c) Storage of Clean XAD-2:  XAD-2  cleaned  and  dried as press
above is suitable for iaaediate use  in  the field,  provided  "
passes the QC contamination  check  described in (d),  below.
ever, precleaned dry XAD-2 aay  develop  unacceptable levels  o
                              A-10

-------
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                                                                             -
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                                                             DK,
              contamination if  scored  for  periods  exceeding  a  few weeks
    If precleaned XAD-2 is not to be used immediately, it shall b<
stored under distilled-in-glass methanol.  No more than two weeks
prior to initiation of field sampling, :he excess methanol shall
be decanted; the XAD-2 shall be washed with a small volume of
methylene chloride and dried with clean nitrogen as described in
(b) above.  An aliquot shall then be taken for the QC contamina-
tion check described in (d), below.

    If the stored XAD-2 fails the QC 'check, it may be recleaned b;
repeating the final two steps of the extraction sequence above:
sequential methylene chloride and hexane extraction.  The QC
contamination shall be repeated after the XAD-2 is recleaned and
dried.

(d) QC Contamination Check:  The XAD-2, whether purchased, "pre-
cleaned", or cleaned as described above, shall be subjected  to a
QC check to confirm the absence of any contaminants that might
cause interferences in the subsequent analysis of field samples.
An aliquot of XAD-2, equivalent in size to one field sampling  tub
charge, shall be taken to characterize a single batch of XAD-2.

    The XAD-2 aliquot shall be subjected to the same extraction.
concentration, cleanup, and analytical procedure(s) as is  (are) t
be applied to the field samples.  The quantitative criteria  for
acceptable XAD-2 quality will depend on the detection limit  cri-
teria established for the field sampling and analysis program.
XAD-2 which yields a background or blank signal greater than or
equal to that corresponding to one-half the MDL for the analyteCs
of concern shall be rejected for field use.  Note that the accept
anee limit for XAD-2 cleanliness depends not only on  the inherent
detection limit of the analytical method but also on  the.expected
field sample volume and on the desired limit of detection  in the
sampled stream.

8.1.3 Class Wool

    Cleaned by thorough rinsing, i.e., sequential immersion  in
three aliquots of hexane, dried in a  110°C oven,  and  stored  in a
hexane-washed glass jar with TFE*-lined screv cap.

8.1.4 Water

    Deionized, then glass-distilled, and stored in hexane-rinsed
glass containers with TFE*-lined screw caps.

8.1.3 Silica Gel

    Indicating type, 6-16 mesh.  If previously used,  dry  at  175;.-
for 2 hr.  New silica gel may be used as received.

8.1.6 Crushed Ice

-------
                                                             D
PA F
{ v. /"I'
    Place crushed ice in the water bath around the impingers
during sampling.

9.   SAMPLE RECOVERY REAGENTS

9.1   Acetone

    Pesticide quality,  Burdick and Jackson "Distilled  in Glass" or
equivalent, stored in original containers.  A blank must be
screened by the analytical detection method.
                                            Distilled  in Glass'
                                            A blank must be
or
9.2  Hexane

    Pesticide quality, Burdick and Jackson '
equivalent, stored in original containers.
screened by the analytical detection method.

10.  PROCEDURE

    Caution:  Sections 10.1.1.2 and 10.1.1.3 shall be done in the
              laboratory.

10.1  Sampling

10.1.1  Pretest Preparation

    All train components shall be maintained and calibrated
according-to the procedure described in APTD-0576 unless otherwise
specified herein.

    Weigh several 200 to 300 g portions of silica gel in air-tight
containers to the nearest 0.5 g.  Record the total weight of the
silica gel plus container, on each container.  As an alternative,
the silica gel may be weighed directly in its impinger or sampling
holder just prior to train assembly.

    Check filters visually against light for irregularities and
flaws or pinhole leaks*  Pack the filters flat in a precleaned
glass container or wrapped hexane-rinsed aluminum foil.

10.1.1.1  Preliminary Determinations

    Select the sampling site and the minimum number of sampling
points according to EPA Method 1.  Determine the stack pressure,
temperature, and the range of velocity heads using EPA Method 2;
it is recommended that a leak-check of the pitot lines (see EPA
Method 2, Sec. 3.1) be performed.  Determine the moisture content
using EPA Approximation Method 4 or its alternatives for the
purpose of making isokinetic sampling rate-settings.  Determine
the stack gas dry molecular weight, as described in EPA Method 2,
Sec. 3.6; if integrated EPA Method 3 sampling is used for molecu-
lar weight determination, the integrated bag sample shall be taken
simultaneously with, and for the same total length of time as, the
EPA Method 4 sampling.
                              A-13

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                                                              DF,
    Select a nozzle size based on the range of velocity heads,
such that it is not necessary to change the nozzle size in order
to maintain isokinetic sampling rates.  During the run, do not
change the nozzle size*  Ensure that the proper differential
pressure gauge is chosen for the range of velocity heads
encountered (see Section 2.2 of EPA Method 2).

    Select a suitable probe length such that all traverse points
can be sampled.  For large stacks, consider sampling from opposite
sides of the stack to reduce the length of probes.

    Select a total sampling time greater than or equal to the
minimum total sampling time specified in the test procedures for
the specific industry such that (1) the sampling time per point is
not less than 2 min.. and (2) the sample volume taken (corrected
to standard conditions) will exceed the required minimum total gas
sample volume determined in Section 6.3.  The latter is based on
an approximate average sampling rate.

    It is recommended that the number of minutes sampled at each
point be an integer or an integer plus one-half minute, in order
to avoid time-keeping errors.

10.1.1.2  Cleaning Glassware

    All glass parts of the train upstream of and including the
sorbent medule and the first impinger^T should be cleaned as
described in Section 3A of the 1980 issue of "Manual of Analytical
Methods for the Analysis of Pesticides in Humans and Environmental
Samples."   Special care should be devoted to the removal of resi-
dual silicone grease sealants on ground glass connections of used
glassware.  These grease residues should be removed by soaking
several hours in a chromic acid cleaning solution prior to routine
cleaning as described above.

10.1.1.3  Amberlite XAD-2 Resin Trap

    Use a sufficient amount (at least 30 gms or 3 gms/m  of stack
gas to be sampled) of cleaned XAD-2 to fill completely the glass
sorbent trap which has been thoroughly cleaned as prescribed and
rinsed with hexane.  Follow the XAD-2 with hexane-rinsed glass
wool and cap both cads.  These caps should not be removed until
the trap is fitted iato the train.  See Fig. (3)£or details.     ——

    The dimensions and XAD-2 capacity of the sorbent trap, and  the
volume of gas to be sampled, should be varied as necessary to
ensure efficient collection of the species of interest.  Some
illustrative data are presented la Table 1.

10.1.2  Preparation of Collection Train

    During preparation and assembly of the sampling train, keep
all traia openings where contamination can enter covered until

-------
:ifl
TABLE  1
*ff-$\
5$J SAMPLE B1ZB AND PLOW RATE COMPARISON POtt SEVERAL SORBIiNT TRAP DESIGNS 	 r
•w3
•>( ijj
^Ail
I.'W
-•Itf
. *•>'
*<$
ri
P*&
v- '
'.-!&
7$
m
in
«'>i.i
>i
h>
e-j
••>^
.»•«
^
&
ibw
%£
l:w'-
V&
F$
1*1
^
^
Charge
nimcnslon. (w») of XAD-2 Plow Equivalent
Trap Depth Diameter Resin (B) to 43 cm/acc

BASS 70 90 130 ' »65 Lpm
8ASS /U (5.9 cfm)
u!SS)

••«•»• » 3° " («:«iSf.)


'upper liait beyond vhich collection efficiency drops off.
^ bColcul«ted fro. VgT for SOX breakthrouBh. Specified value includes a
i



/ 3
Max. Cnmple Sire \c|O^
for Efficient Capture of
FollouinR Compoundob
Octane Denzcnc Phenol

150 3.0 240
45 0,9 74

22 0.4 35


•
aafety factor of 2.




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  1
just prior co assembly or until saopling is  about  to  begin.
Caution:  Do not use sealant greases in assembling the  train.

    Place approximately 100 gas of water in  each of the  first  two
irapingers with a graduated cylinder, and leave the third impinger
empty*  Place approximately 200 to 300 g or  more,  if  necessary,  of
silica gel in the last impinger.  Weigh each impinger (stem
included) and record the weights en the iapingers  and on the  data
sheet .

    Assemble the train as shown in Fig. 1.

    Place crushed ice in the water bath around the iapingers.

10.1.3  Leak Check Procedures

10.1.3.1  Initial Leak Cheek

    The train, including the probe, will be  leak checked prior to
being inserted into the stack after the sampling train has been
assembled.  Tarn on and set (if applicable)  the heating/cooling
system(s) to cool the sample gas yet remain  at a temperature
sufficient to avoid condensation in the probe and connecting line
to the first impinger (approximately 120 C).  Allow time for the
temperature to stabilize.  Leak check the train at the sampling
site by plugging the nozzle with a TFE* plug and pulling a 330 ma
Rg (12 in. Hg) vacuum.  A leakage.rate in excees of 42 of the
average sampling rate or 0.0057 m /min (0.02 cfm) whichever is
less, is unacceptable.  Sampling must cease  if pressure during
sampling exceeds the leak check pressure.
    *
    The following leak cheek instruction for the sampling train
described in APTD-0576 (2) and APTD-0581 (4) may be helpful.
Start the pump with bypass valve fully open and coarse adjust
valve completely closed.  Partially open the coarse adjust valve
and slowly close the bypass valve until 380  mm Hg  (12 in. Hg)
vacuum is reached.  Do not reverse the direction of the bypass
valve.  This will cause water to back up into the probe.  If 380
mm Hg (12 la. Eg) is exceeded during the test, either leak check
at this higher vacuum or end the leak check as described belov  and
start the test over.

    When the leak check Is completed, first slowly remove the TFE*
plug from chc inlet to the probe then immediately  turn  off the
vacuum pump.  This prevents the water In the Impingers  from being
forced backward Into the probe.

10.1.3.2  Leak Checks During a Test

    A leak check shall be performed before  and after a  change  of
port during a test.  A leak check shall be  performed before and
after a component (e.g., filter or  optional water  knockout  trap)
is changed during a test.

-------
                                                             DRAF!
    Such leak checks shall be performed according to the  procedure
      In Section 10.1.3.1 of this method except that it shall be
performed at a vacuum equal to or greater than the highest value
recorded up to that point in the test..   If the leakage rate is
found to be no greater than 0.00057  m /min (0.02 ft /min)  or 4Z of
the average saopling rate (whichever is smaller) the results are
acceptable.  If, however, a higher leakage rate is observed, the
tester shall either:  (1) record Che leakage rate and Chen correct
the volume of gas sampled since Che  last leak check as shown in
Section 10.1.3.4 of this  method, or  (2) void Che test.

10.1.3.3  Post-Test Leak  Cheek

    A leak check is mandatory at the end of  a test.  This  leak
check shall be performed  in accordance  with  Che procedure  given in
Section 10.1.3.1  except that  it shall be conducted at a vacuum
equal Co or greater Chan  Che  highest value recorded during Che .   . _
test.   If  the leakage  rat e (^>Tound  Co  be  no greater Chan  0.00057
a /min (0.02 ft  /min)  or  4Z of Che average sampling race  (which-
ever is smaller),  Che  results are acceptable.  If, however,  a
higher leakage race is  observed, Che tester  shall either:   (1)
record che leakage  race and correcc  che volume as gas sampled
since che  last leak check as  shown in Section 10.1.3.4 of  this
method, or (2) void Che Cesc.

10.1.3.4  Correcting for  Excessive Leakage Rates

    The equation  given  in Section 11.3  of  this  method for  calcu-
 jting V (scd),  Che corrected volume of gas  sampled, can  be  used
is  written unless  che  leakage race observed  during any leak  check
tfcer che  scare  of  a test exceeded L ,  the maximum acceptable
leakage rate (see  definitions below).   If  an observed leakage rate
exceeds L  ,  then  replace  V  in Che equation  in Section 11.3  with
:he following expression:
•here :

    V   •  Volume  of gas  sampled  a* measured by  the  dry gas
         mecer  (dscf).

    I*m  -  Maximum acceptable  leakage rate equal  Co  0.00057 m  /min
         (0.02  fc /Bin)  or 4Z of che  average sampling race,
         whichever la smaller*

    L   •  Leakage race observed  during  che post-test  leak check.
    p    m-Vmin  (fc^/min).

    L.  •  Leakage race observed  during  Che leak  check performed
         prior  co che ~i th' leak check  (i - 1,2,3. ..n), in /ain
         (fc3/min).
                               A-17

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     BJ  -  Sanpllag  time interval between two successive leak checks
          beginning vith the interval between the first and second
          leak  checks, min.

     9   •  Sampling  time interval between the last (n th) leak check
     P    and the end of the test, min.

 Substitute only for Chose leakages (L. or L ) which exceeded L .
                                     ip                  a
 10.1.3.5  Train Operation

     During the sampling run, a sampling rate within 10Z of the
 selected  sampling  rate shall be maintained.  Data will be con-
 sidered acceptable if readings are recorded at least every 5 min.
 and  not aore than  102 of the point readings are ^n} excess of ^.lOZ
 and  the average of the point readings is within VlOZ.  During the
 run, if ie becomes necessary to change any system component ia any
 part of the train, a leak check must be performed prior to
 restarting.

     For each run,  record the data required on the data sheets.   An
 example is shown in Fig. 4.  Be sure to record the initial dry gas
 aeter reading.  Record the dry gas meter readings at the  beginning
 and  end of each sampling time increment and when sampling is
 halted.

     To  begin sampling, remove the nozzle cap, verify (if  applic-
 able) that the* probe and sorbent module temperature control sys-
 tems are  working and at temperature and Chat the probe is properly
 positioned.  Position the probe at the sampling point.  Immedi-
 ately start the pump and adjust the flow rate.

     If  Che stack is under significant sub-ambient pressure  (height
 of impinger stem), take care to close the  coarse adjust valve
 before  inserting the probe into the stack  to avoid water  backing
 into the  probe.  If necessary, the pump may be turned  on  with  the
 coarse  adjust  valve closed.

     During the test run, make periodic adjustments to  keep  the
 probe temperature  at the proper value.  Add more ice and,  if
 necessary, sale to ch« lee bath.  Also, periodically check  the
 level and zero of  the manometer and maintain the temperature  of
 sorbent module at  or less than 20°C but above 0°C.

     If  the pressure drop across the train  becomes high enough to
 make the  sampling  rat* difficult Co maintain, the east run  shall
 be terminated  unless the replacing of the  filter corrects the
 problem.  If the filter ia replaced, a leak  check shall  be
 performed*

     At  the end of  Che sample run, turn off  the pump,  remove the
 probe and nozzle from the stack, and  record  Che  final  dry gas
 meter reading.  Perform the post test leak check.*

*With acceptability of the test run to be based on the same
 criterion as in 10.1.3.1.

-------
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-------
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*
10.2  Sataple Recovery

    Proper cleanup procedure begins as soon as  the probe is
removed from the stack at the end of the sampling period.

    When the probe can be safety handled,  wipe  off all external
particulate matter near the tip of the probe.  Remove the probe
from the train and close off both ends with hexane-rinsed aluminua
foil.  Seal off the inlet to the train with a ground glass cap or
hexane-rinsed aluminum foil.

    Transfer the probe and inpinger assembly to the cleanup  area.
This area should be clean and enclosed so  that  the chances of
contaminating or losing the sample will be minimized.  No sacking
shall be allowed.

    Inspect the train prior to and during  disassembly and note an?
abnormal conditions, e.g., broker/filters, color of the iapinger
liquid,  etc.  Treat the samples as follows:

10.2.1  Container Ho. 1

    Either seal the ends of the filter holder or carefully remove
the filter from the filter holder and place it  in its identified
container.  Use a pair of precleaned tweezers to handle the
filter.   If it is necessary to fold the filter, do so such that
the particulate cake is inside the fold.  Carefully transfer to
the container any particulate matter and/or filter fibers which
adhere to the filter holder gasket, by using a  dry inert bristle
brush and/or a sharp-edged 'blade.  Seal the container.

10.2.2  Sorbent Modules
                Remove  the  sorbent  module  from  the  train  and  cap  it  off.

            10.2.3   Cyclone Catch

                If  the  optional  cyclone  is  used,  quantitatively recover  the
            particulate into a sample  container and cap.

            10.2.4   Sample  Container No. 2

                Quantitatively recover material deposited in  the  nozzle,
            probe,  transfer line,  the  front half  of the  filter holder,  and  the
            cyclone, if used, first by brushing and then  by sequentially
            rinsing  with acetone and then  hexane  three  times  each and  add  all
            these rinses  to Container  No.  2.  Mark  level  of liquid on  con-
            tainer.

            10.2.5   Sample  Container Wo. 3

                Rinse the back half of the  filter holder, the connecting  line
            between  the filter and  the condenser  and the  condenser (if  using
            the  separate condenser-sorbent  trap)  three  tiaes  each with  acetone

-------
                                                             unMf
and hexane collecting all rinses in Container 3.  If using the
combined condenser-sorbent trap, the rinse of the condenser shall
be performed in the laboratory after reaoval of the XAD-2.  If the
optional water, knockout trap has been eoployed, it shall be
weighed and recorded and its contents placed in Container 3 along
with the rinses of it.  Rinse it three times each with acetone,
and hexane.  Mark level of liquid on container.

10.2.6  Sample Container No. A

    Remove the first impinger.  Wipe off the outside of the
impinger to remove excessive water and other material, weigh (stem
included), and record the weight on data sheet.  Pour the contents
and rinses directly into Container No. 4.  Rinse the impinger
sequentially three times with acetone, and hexane.  Mark level of
liquid on container.

10.2.7  Sample Container No. 5

    Remove the second and third impingers, wipe the outside to
remove excessive water and other debris, weigh (stem included) and
record weight on data sheet.  Empty the contents and rinses into
Container No. 5.  Rinse each with distilled DI water three times.
Mark level of liquid on container.

10.2.8  Silica Gel Container
               •
    Remove the last impinger, wipe the outside to remove excessive
water and other debris, weigh (stem included), and record weight
on data sheet.  Place the silica gel into its marked container.

11.  CALCULATIONS

    Carry out calculations,  retaining at least one extra decimal
figure beyond that of the acquired data.  Round off figures after
final calculations.

11.1  Nomenclature

    G       - Total weight of chlorinated organic compounds in
              stack gas sample, ng.

    C*      • Concentration  of chlorinated organic compounds in
              stack gas, US/° > corrected to standard conditions
              of 20°C. 760 am Hg (68°F, 29.92 in. Hg) on dry
              basis .

    A       - Cross-sectional area of ndzzle, m  (ft ).

    B       " Water vapor la tnc gas stream, proportion by volume.

    I       • Percent of isokinetic sampling.

    M       - Molecular weight of water, 18 g/g-mole (18
     w        Ib/lb-mole)


                               A-21


-------
                               .
                                                             D

     .
*

i
I
                          - Barometric pressure at the saopling site,  mm Hg
                            (in. Hg).

                          - Absolute stack gas pressure,  ma Eg (in.  Hg ) .

                          - Standard absolute pressure, 760 ma Hg (29.92 in.
                            _ »
                            Hg).
       .
     s to.
                  R       » Ideal gas constant. 0.06236 mm Hg-m / K-g-mole
                            (21.83 in. Kg-ft3/6R-lb-mole).

                  T       • Absolute average dry gas meter temperature °K. (°R).

                  T       • Absolute average stack gas temperature °K (°3.) .

                  Tstd    - Standard absolute temperature, 293°K (68°F).

                          -. Total eass of liquid collected in iapingers and
                            silica gel.

                  V       • Voluae of gas saaple as aeasured by dry gas aeter,
                            dca (dcf) •

                  V (std) - Volume of gas sample measured by the dry gas meter
                            'corrected to standard conditions, dsca (dscf).

                  Vtf(std) » Volume of vater vapor in the gas saaple corrected t
                            standard conditions, sea (scf).

                  v       • Stack gas velocity, calculated by combustion calcu-
                            lation, m/sec (ft/sec).
     .
    T

    AH
                          • Meter box correction factor.

                          • Average pressure differential across  the orifice
                            aeter, aa H-0 (in. H.O).
    8

    13.6

      60

     100
• Density of vater, 1 g/al (0.00220 Ib/al).

• Total saapling tiae, min.

• Specific gravity of aercury

• Sec/ain.

• Conversion to percent.
11.2  Average Drv Gas Meter Teaperature and Average Orifice
      Pressure Drop

    See data sheet (Tig. A).

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1F1
                                                                    Uh'Ar i
11.3  Dry Gas Volume

    Correct the sample volume measured by the dry gas meter to
standard conditions [20°C, 760 ^mm Hg (68;rF, 29.92 in. HG ) ] by
using Equation 1.
     where:

                                    a       std              T            ...
                                                              a           (1)
           ,-y0.3855 °K/mm Hg  for  metric  units

           • 17.65 °R/in. Hg  for  English units

      11.4  Volume of Water Vapor
                                    RT                               '     (2)
                    V (std) - nL   M     Std - K m
                     w       ~lc  «  x P      2 Ic
     where:

         K. «  0.00134 B  /ml  for  metric  units

            •  0.0472 ft3/al  for  English units

     11.5  Moisture  Content

                    B
                     ws   Vm(.td)
         If liquid droplets  are  present  in  the  gas  stream assume the
     stream to  be saturated  and  use  a  psychrometric chart to  obtain an
     approximation of  the moisture  percentage.

     11.6  Percent Isokinetie  Sampling
                                  »Tv
                    100
                 I	
                           60ev»P3  An

     where:

         K4  "  0.003454  me  Hg  -  m /ml  - °K for metric units

             -  0.002669  in  Hg  -.fC3/al - °R for English units

     11,7  Concentration of  Chlorinated Organic Compounds in  Stack Gas

         Dcceraine  the  concentration  of chlorinated organic compounds
     is  the  stack gas  according to  Equation 5.
                                    A-23

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 I
 4
 I

 I
f

I
i
I

I

I
                                                                          DP'
                                         G
                              C - K      S
                               s  "5  V(std)                             (5)
             where:
 *                                       33
                            K5 - 35.31  ffVn

             12.  QUALITY ASSURANCE  (QA)  PROCEDURES

                 The positive identification and  quantification  of  specific
             compounds in this assessment of stationary  conventional  combustion
             sources is highly dependent  on the  integrity  of  the samples
             received and the precision and accuracy  of  all  analytical  proce-
             dures employed.  The QA procedures  described  in  this section  were
             designed to monitor the performance  of  the  sampling methods and to
             provide information to  take  corrective  actions  if  problems are
             observed.

             Field Blanks

                 The field blanks should  be submitted as pare of the  samples
             collected at each particular testing site.   These  blanks should.
             consist of materials that  are used  for  sample collection and
             storage and are expected to  be handled  with exactly the  saae
             procedure as each sample aedium.
Blank Train

    For each series of test runs, set up a blank train in a manne
identical to that described above, but with the probe inlet cappe<
wich hexane-rinsed aluminum foil and the exit end of the last
iapinger capped with a ground glass cap.  Allow the train to
remain assembled for a period equivalent to one test run.  Recove
the blank sample as described in Sec* 7.2.

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                                                            DP/* P
                            REFERENCES
1.  Cooke, M., DeRoos,  F., and Rising,  B.,  "Hot Flue Gas Spiking
    and Recovery Study  for Tetrachlorodibenzodioxins (TCDO)  Using
    Method 5 and SASS Sampling with a Simulated Incinerator",  EPA
    Report, Research Triangle Park, NC   27711 (1984).

2.  Roa, J.J., "Maintenance, Calibration and Operation of Isokine-
    tic Source-Sampling Equipment", EPA Office of Air Programs,
    Publication No. APTD-0576 (1972).

3.  Sherma, J., and Beroza, M.,  ed., "Analysis of Pesticides in
    Humans and Environmental Samples",  Environmental Protection
    Agency, Report No.  600/8-80-038 (1980).

4.  Martin, Robert M.,  "Construction Details of Isokinetic Source
    Sampling Equipment",  Environmental  Protection Agency, Air
    Pollution Control office, Publication No. APTD-0581 (1971).

5.  Taylor, M.L.,  Tiernan, T.O.,  Garrett, J.H.,  Van Ness, G.F.,
    and Solch, J.G., "Assessments of Incineration Processes  as
    Sources of Supertoxic Chlorinated Hydrocarbons:   Concentra-
    tions of Polychlorinated Dibenzo-p-dioxins/dibenzo-furans  and
    Possible Precursor  Compounds  in Incinerator Effluents",
    Chapter 8-Chlorinated Dioxins and Dibenzofurans  in the Total
    Environment-, Buttervorth Publishers, Woburn, Mass. (1983).
                               A-25
                                      --i  «f
                                           *

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          APPENDIX  C
TIMES BEACH DIOXIN RESEARCH AREA





        SITE SAFETY PLAN

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                TIKES BEACH DIOX1N RESEARCH AREA
                         SITE SAFETY PLAN
 Current  data  indicates  that soils at the research area ere
 contaminated  with 2,3,7,6-TCDD up to 2 ppm  (2000 ppb).  Detailed
 information on the hazards of exposure to this pollutant are
 contained  in ^ggt-i.on f>. the Health Effects  Chapter of Dioxins..
 USEPA. IERL.  published  late in 1980.  The introductory paragraph
 of Section 6  is reproduced below:  On a molecular basis
 2,3,7,6-TCDD  is perhaps the most poisonous  synthetic chemical.
 Only bacterial exotoxins are more potent poisons.  Not only is
 this TCDD  isomer extremely poisonous but it also has extremely
 high potential for producing adverse effects under conditions of
 chronic  exposure.  Human exposure to 2,3,7,8-TCDD has induced
 chloracne  (an often disfiguring and persistent dermatologic
 disorder), polyneuropathy  (multiple lesions of peripheral
 nerves), nystagmus (involuntary rapid movement of the eyeball),
 and liver dysfunction*as manifested by hepatomegaly  (increase in
 liver size) and enzyme  elevations (Pocchiari, Silano, and
 Sampieri 1979).  In animals, this compound  has been shown to be
 teratogenic, embryotoxic, carcinogenic, and cocarcinogenic
 (Neubert and Dill man 1972; Courtney 1976; Kociba et al. 1976,
 and Kouri et al. 1976).  It has been established that under
 certain  conditions ', 7;3 ,7 ,8-TCDD tan -enter—t-he--hwnan body f.ro.m a
 2,H,5,7-T-treated food  chain and can accumulate in the fatty
 tissues  and secretions, including milk (Galston 1979).  The
 available data indicates significant risks  associated with the
 use of dioxin-contaminated herbicides.  Based upon the work of
 Van Miller et el., estimates done by accepted risk assessment
 procedures indicate that daily human exposure to 0.01 ug (10 ng)
 of 2,3,7,6-TCDD is the dosage expected to result in "incipient
 carcinogenic!ty".  Additionally, daily human exposure to 4 ug
 2,3,7,6  TCDD would be expected to result in a shortened
 lifespan, and daily exposure to 290 ug would result in acute
 toxicity (Colston 1979)."

 In addition to the dioxin contamination in the soil being worked
 with there may be several other chemicals of concern encountered
 in decontamination or sample packaging.  These chemicals
 include:

 1.  Inhibited chloroform 1,1,1. Trichloroethane.  The TLV-TWA
 for this chemical substance is 350 ppm.  This volatile substance
 can enter the body t-hru inhalation," ingestion and contact and
 may cause a variety of effects beginning with headache, general
 lassitude,  poor equilibrium and eye or skin irritation.

2.  Ethyl Alcohol.  The TLV-TWA for'this chemical is 1,000 ppm.
This volatile substance can enter the body thru inhalation,
 ingestion and skin contact and may cause a variety of effects
beginning with eye irritation, headaches, drowsiness, nausea and
vomiting.

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3.  Vermiculite.  The vermiculite packaging materiel  is a
potential eye irritant and contains a small percentage of
asbestos.  Asbestos fibers larger than 5.0 microns can represent
a cancer risk if inhaled.

The very nature of the business operated by the spiller who
created the St. Louis area dioxin contamination problem
indicates that there is a substantial opportunity for the
presence of a wide variety of additional organic chemicals in
the contaminated soil where 2,3,7,8-TCDD has been confirmed.
Previous investigations have already disclosed the presence of a
number of volatile organics, PCB's and some of the process
chemicals from which the dioxin was created.  Analyses have not
been conducted of the research areas to either confirm or
discount the presence of other contaminants.

Personnel Health Monitoring
                      •
Physical Examinations - Personnel working on any suspected or
confirmed site must have completed a baseline physical exam
meeting the guidelines listed below for hazardous waste work
within 12 months prior to the site work.  Personnel who have not
had such a physical may not be authorized to enter the site.

Physical Examination Guidelines for Hazardous Waste Vork

    ried'Jcal/Occupyffr^nal --Quest-icmnair*  .  ..		

    Full Physical Examination by Physician-

    Vitals (height, weight, blood pressure, pulse)

    Screening Audiametric Test with Otoscopic Exam for Wax

    Pulmonary Function Test (Spirometry)

    Resting ECC, Reed by Board-Certified Cardiologist

    Chest X-Fay (PA) Read by Board-Certified Radiologist  (once
    per 2 year*)

    Laboratory Analysis

   •Blood Chemistry Profile

  •  Complete Blood Count with Differential
                    •
    Urinalysis with Kicrospoic Examination

    Zinc Protoporphyrin

    Urinary Arsenic

    Urinary Mercury

    Urinary Cadmium

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 •Blood Chemistry Profiie

     Calcium          Direct Bilirubin          SGPT

     Phosphorus       Indirect Bilirubin        CCT

     Clugose          Alkaline Phosphatase      Creatinine

     BUN              LDH                       Tri£lycerides

     Uric Acid        SCOT                      Osnolality

     Cholesterol       Sodium                    Bun/Creatinine
                                                    Ratio

     Total Protein    Potassium                 Globulin

     Albumin          Chloride                  A/G Ratio

     Total Bilirubin  CPK                       Beta Cholesterol
                                                     (LDL)

 To gain entry to the research area all  researchers shall provide
 a statement from their examining physician to the MDNR that
 there are no medical impairments which  would prevent use of
 respiratory equipment for performance of work under the
 conditions at the research area.

-Personnel -Pret-ective Equipment
                                           i

 Respiratory Protection:

 Personnel within the contaminated area  are required to wear a
 f_uli  face respirator equipped with combination organic vapor,
 high  efficiency  participate cartridges  or canisters.  Corrective
 vision inserts are required for those who normally wear
 glasses.   No facial hair interfering with the face to mask seal
 will  be allowed.  Researchers must pass a qualitative fit test
 for their chosen mask before entering the research area.

 George Carson, a Certified Industrial Hygienist with NIOSH, in a
 January 15,  1983 release stated:

 "If the sites to be investigated are similar to those at Times
 Beach,  Missouri, in that the contaminant was sprayed on the soil
 along with waste oil some ten years ago, during which time the
 potential for Dioxin. to  volatize has been virtually eliminated
 and the fact that the only potential exposure to Dioxin is by
 disturbing and aerosolizing the soil particles, to which it may
 be  attached,  we  would recommend that adequate respiratory
 protection would be afforded by the. use of air purifying
 respirators  in a complete respiratory protection program."

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Dermal Protection

1.  Personnel within the contaminated area  are  required  to  veer
a full-body, one-piece coverall  suit manufactured  from
saran-coated spun bonded olefin.  Uncoated  spunbonded olefin  may
be worn during certain conditions (see Section  3 of  this plan,
Health Monitoring).

In a test conducted by the Southwest Research Institute  in  San
Antonio, Texas, it was confirmed that Tyvek,  a  spun  bonded
olefin, consistently stopped particulate permeation.

2.  All personnel working on site are required  to  wear an inner
glove of lightweight PVC or latex accompanied by an  outer glove
of buna nitrile rubber.  External work gloves of cotton  or
leather which provide additional thermal protection,  enhance  a
worker's grip, and protect rubber gloves from physical damage
may be used to meet individual preferences.

3.  Clove to coverall seam and boot to coverall seams will  be
sealed with duct tape to prevent dirt from entering  at those
areas.  In the event clothing is ripped or torn,  the clothing is
to be removed and replaced at once.

t4.  In compliance with OSHA standard 1910.136,  all personnel
will wear neoprene steel-toed, steel-shanked work  boots.

5.  In compliance with OSHA standard 1910.135,  hard  hats will be
worn when operating overhead equipment.  -

6.  In the event of direct skin contact, the affected area is to
be washed immediately with soap and water.  All clothing
provided for on-site use is to be considered disposable  and
handled as contaminated trash before personnel  may leave the
designated work area.

De contamination

Cross contamination must be cleaned from all equipment before on
site storage by using a thorough water rinse at the wash station
provided.  Additionally workers' boots, gloves and any other
heavily contaminated articles must be cleaned with the same
procedure before going into the support area.

All equipment and gear must be thoroughly steam cleaned or
washed with soap and water then rinsed before leaving the site.
Decontamination must.be suf f icient';to prevent transport of
contamination off site.

Personnel decontamination will consist of removal of
contaminated clothing with its subsequent storage in 55-gallon
metal drums with ring seal lids.  Footwear may be temporarily
stored in the contamination reduction area.

Following removal of clothing, personnel shall take a thorough
cleansing shower prior to redress and departure from the site:

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           Procedures
 In  the  case  of physical  injury to any personnel the DNR
 representative is to stop all work  immediately and provide Tor
 medical  attention for  the injured person as the highest
 priority.  A list will be posted by DNR with the following
 emergency  numbers:

     Times  Beach Police

     Eureka Fire Department

     Ambulance Service

 Stress  Monitoring

 There are  no known personnel exposure routine monitoring
 procedures for 2 ,3 ,7 ,BrTCDD.  Protective clothing standards and
 decon procedures are established and enforced to minimize the
 potential  for exposure to this contaminant.

 In  site  specific situations where other contaminants may involve
'additional screening,  monitoring services and equipment are
 available.   Where site history indicates that problems may
 exist,  specific guidance for upgrading personnel monitoring will
 be  provided  in the site  study plan.
 Weather Variations:  During cold weather, employees are provided
 with  insulated safety footwear and oversized  impervious suits to
 facilitate additional clothing required for thermal protection.

 It  is recommended that during site operation  periods where
 ambient daily maximum temperatures exceed 70  degrees Fahrenheit,
 the researchers should implement measurements of Wet Bulb Globe
 Temperature Index  (WBCT) as described  in TLVs, Threshold Limit
 Values for Chemical Substances in Work Air Adopted by ACCIH for
 1962.  Due to the levels of protective clothing worn by all
 personnel, the researchers should calculate the WBCT at 1 hour
 intervals whenever the daily maximum temperature exceeds 70
 degrees Fahrenheit.  All measurements and calculations should be
 recorded.  Where possible, work hours are to  be changed to
 cooler periods of the day to avoid unnecessary heat stress on
 personnel.

 From the heat stress monitoring data that has been collected
 during the summer investigations, the following guidelines have
 been suggested concerning the work/rest regimen for dioxin
 samplers wearing Level C protection:

 1.  With WBCT's from 75-65 degrees Fahrenheit, workers shall not
 be allowed to work more than one hour without taking at least a
 15 minute break.

 2.  With WBCT's from 85-95 degrees Fahrenheit, workers should
 not be allowed to work more than H5 minutes without at least a
 15 minute break.

-------
 3.   With VBCT's  exceeding 95 decrees Fahrenheit, workers should
 not  be  allowed to  work  more than 15 minutes without at least a
 15 minute break.

 n.   Individuals  definitely have variable limits as to the amount
 of heat they  can tolerate.  Employees should be informed that
 they are responsible  for their own physical well-being.
 Monitors can  only  judge heat stress by what they see.  Only the
 individual  knows how  he feels and what his limits are.

 It is recommended  that  at the end of each work period the
 workers shall remove  their protective clothing and do the
 following:

 1.   Take their oral temperature and proceed as below:

     a.   99  degrees Fahrenheit - no action.
                      *
     b.   99  degrees Fahrenheit and 99.7 - cool them off with a
 water spray and  do not  allow a return to work unless their
 temperature is 99  degrees Fahrenheit at the end of the rest
 period..

     c.   99.7  degrees  Fahrenheit and 100.U - cool them off with a
 water spray,  double their rest period, and do not allow a return
 to work unless their  temperature is 99 degrees Fahrenheit.  If
 liBdt'-exhaustien or* heat stro-k-e—symptoms are present., _.s_e.e.k	
 medical  attention.

     d.   100.4 degrees Fahrenheit - cool them off immediately
 with a  water  spray, begin standard first-aid procedures, and
 seek medical  attention.

 2.   Check each worker carefully for symptoms of heat illness and
 react accordingly.

 3.   Drink slowly,  cool  but not cold, eight  (8) ounces of water,
 six  (6)  ounces of  water plus two (2) ounces of a natural
 unsweetened fruit  juice, or eight (6) ounces of 0.1% saline
 solution.   They can drink more if desired.  Do not use Catorade,
 it depletes potassium.

 Personnel Training

 All personnel shall be  provided with a copy of this plan and
 they must be familiar with its contents before entering the
 research  area.  All personnel must be fully familiar with the
 use of  respiratory protective devices and protective clothing.

 Site Safety

 1.  Access  - Only  authorized personnel conducting business  will
 be allowed  to enter Times Beach.  Personnel must sign any
release  required by the City and follow all rules established  by
the City.   Personnel  must use designated travel routes only.

2.  No  one  shall be permitted to eat, drink or smoke within the
site, and shall thoroughly wash hands and face with soap and
water before doing so outside the site.  Individuals must wash

-------
 3.  Under no conditions are personnel to be authorized to enter
 any alleged contaminated site without a work partner and one
 additional person stationed outside the contaminated area in
 constant visual or radio contact with the work party.

 H.  In  order to facilitate removal of any injured personnel, the
 site  vehicle must must be parked near to the research activity
 and facing the support area at all times.

 ACKNOWLEDGMENTS

 Content of this plan  is modified from a document prepared by the
 USEPA Region VII.  The MDNR wishes to acknowledge the following
 people:

    William Keffer, USEPA Lab Region VII

    Daniel Harris, USEPA Lab Region VII

    Dennis .Howard, Veston TAT Region VII

    Dr. George A. Carson, CIH, N10SH Region VII

    Dr. George D. Kleopfer, USEPA Lab Region VJI

    Dr. Steven Gertz, Roy P. Ueston, Inc., Vest Cheater, Penn.

 REFERENCES

    Occupational Safety and Health Administration, 2981  (Rev.).
 OSHA Safety and Health Standards. General Industry Standards.
 2206.   United States Department of Labor, Washington, D.C. p.
 297.

    United States Environmental Protection Agency, 1962  (Rev.).
 Interim Standards Operating Safety Guides.  Washington, D.C.
 Sec. 5, pp 1-12.

    Carson, George A., Ph.D., CIH.  Jan 1983 Statement of
 Respiratory Protection.  NIOSH Region VII release.  Kansas City,
 Missouri.  1 p

    Chemical & Engineering News, June 1963.  Dioxin. C&EN,
 Washington, D.C. 66 pp

    Hageman, John P., Kay 1962.  Evaluation of Anticontamination
Clothing Material to Protect Aeainst Radioactive Contamination.
Southwest Research Institute.  San Antonio, Texas, 7 pp

-------
     APPENDIX  D
TEST SITE DESCRIPTION

-------
                                  TIMES BEACH
 location
      Legal Description:  Floodplaln of  the Meremec
                          River, principally W 1/2. Sec. 32,
                          and I  1/2, E 1/2. Sec. 31, 7.44 N.,
                          N., R. 4  E., 5th P.M.
                          Manchester Quadrangle
                          St. Louis County
                          Latitude:  38° 30' 33"
                          Longitude: 90° 36' 08"
                          Population 2,061 (None at Present)
Accessibility
      Times Beach can be'entered  by  any of three routes.  Interstate 44 exits
      onto a northern outer  road  which goes Into the City.  Lewis Road from the
      north also connects  with  the 1-44 outer road.  The third access route is
      from the City of Eureka south  of 1-44 onto Times Beach Service Road.
History -Summary-
                •i- - -
      In June 1972, a dty ordinance was passed to contract with a waste oil
      hauler to spray the roads  for dust control.  Apparently all of the grevel
      streets were oiled  that  sunmer twice and a third time where needed, as re-
      called by residents.  In 1973, the roads were again sprayed by contract.
      The agreement was to have  approximately ten miles of road oiled.  Five
      additional  streets  had been  paved so less oiling was done that year.  EPA
      sampled the roads and right-of-ways In November and December 1982, and
      found 2,3,7,8-TCDD  levels  up to 127 ppb.  In December 1982, the Meramec
      River flooded the town.  EPA sampling in January 1983 following the flood
      showed that the contaminated soil remained quite immobile throughout the
      flooding.  On February 22, 1983, the EPA Administrator announced a $33
      million pledge from superfund to purchase the Times Beach property under
      a relocation plan to be  developed and implemented by the Federal
      Emergency Management Agency  (FEKA).  EPA is planning to have a feasi-
      bility study conducted to  determine the scope and costs of cleanup
      alternatives.  The  city  is on the National Priorities List.

Site Description  (see maps)                     -

      Times Beach 1s principally bounded by the Meramec River, Interstate 44,
      and the Burlington  Northern  Railroad tracks.  Being 1n the 100-year
      fjoodplain,  the area is  relatively flat.  The majority of the city's 28
      miles of paved and  gravel  road, shoulders, and ditches are contaminated.
      Maximum levels of 2,3,7,8-TCDD are shown on the city map.  Contamina-
      tion has been found  down to  at least two feet below the surface.  The
      City of  Eureka,  population 3,862 lies immediately to the south and west
      of  Times Beach.  None of Eureka's streets were oiled and no contamination
      has been found within the  city.  Results of all groundwater sampling in
      the area have been  negative.

-------
Geologic and Soils Description

      Times Beach is on an alluvial  setting,  underlain by alluvial silt to a
      depth of more than 5 feet.  Below the alluvial  silts; sand,  gravel, and a
      mixture of silt, sand,  and clay  would be expected to a depth of from 40
      to 50 feet where bedrock is encountered.  The water table would be expect-
      ed to be about at the Meramec  River  level, between 10 and 20 feet from
      the surface in most of  the area.

      The alluvial  silt has a relatively low  permeability and would be expected
      to be wet natured in that 1t does  not readily or rapidly drain water.
      Due to this and the screening  effect of the silt, it 1s not  likely that
      soil  particles contaminated with dioxin would move down into the water
      table. ~

      It can be assumed that  the contaminated material consists of road bed
      material  plus  native soil  where  the  contamination has eroded into the
      ditches.   .

-------
                                                     "»>^/A_J\{-.;V, eta l"*fc  1
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                                                                        MANCHESTER, MO.
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         MISSOURI  OE'

-------
TIMES  BEACH, MISSOl Rl
v.s
                                                  AGENCY
                            REGION 7 - KANSAS CITY
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-------
             TIMES BEACH DIOXIN RESEARCH FACILITY

     One  oT  the conclusions of the Missouri Dioxin Task Force
 was  that further research needs to be conducted to determine
 dioxin destruction methods. As a result, the Missouri
 Department  of Natural Resources (MDNR) assisted in
 establishing a dioxin research group.  This group consists of
 governmental agencies (MDNR, EPA, Missouri Division of
 Health), industry and the University of Missouri.  This group
 then concluded that in-situ research at Times Beach, Missouri,
 would be of great help in determining destruction methods for
 dioxin contaminated soils.  Based on the group's conclusions,
 the  MDNR solicited proposals for conducting in-situ research
on dioxin contaminated soil at Times Beach, Missouri,
beginning during the summer of 198M.
    The objectives of this project are twofold.  The first is
to isolate those technologies that have potential to detoxify
dioxin contaminated material.  The second objective is to
compare different successful technologies for application to
solve the crisis.  Once potential technologies have been
identified, long-tern funding mechanisms can be looked at for
those processes by the regulatory agencies.
    Laurel Road in Times Beach, Missouri, was selected as the
area for conducting in-situ dioxin destruction
investigations.  The street is bounded on the west and east
sides by Orchid Drive and Beach Drive, respectively (see
map).  The concentration of dioxin in soils is in the range of
100-300 ppb.

-------
     The  MDNR, acting on the suggestions of the research croup,

 set  up the  program by excavating a two block portion of Laurel

 Road.  The  soil and gravel were homogenized by mixing them

 thoroughly.  The soil was then screened to remove the larger

 gravel and  rocks, laid back into stainless steel bins six feet

 by eight feet by two feet deep and compacted back to the

 original density.  A bottom liner was installed to drain

 liquids seeping through the soil.  Water and power outlets are

 provided at each plot.  An on-site soils laboratory is

 available.  Security arrangements such as lockers and a
                          •
 decontamination facility are also available.  A full-time MDNR

 on-site coordinator is available to oversee operations and

 ensure that security is maintained.  Emergency services are

 also available.

    A comprehensive sampling and analysis program was

 conducted to determine initial reference levels prior to

 implementing research proposals.  The plots are currently

 available for in-situ investigations.  The group has decided

that at least three units be made available per research

group.  This would give the researcher an opportunity to

create a standard reference unit and vary parameters as

necessary in the other two units.  Standardized soil could  be

made available for in-house research, if the researcher

demonstrates that he has the resources for in-house management

of dioxin.

-------
 \
-    During the investigation,  close monitoring will  be
 maintained by the research group to assess the progress.   At
 the end of the investigation,  the group will  review  the
 project's accomplishments and  will take the appropriate
 actions such as disbursing the information or recommending
 that the process be applied at a given site.
     Funding mechanisms for the program are being evaluated.
 It is anticipated that the majority of the proposers would be
 self-funded industrial entities.  The cost for leasing a  plot
 (set of three units) is $16,500 to be paid initially.  This
 one time fee is essentially the cost of preparation  of the
 plot along with sampling and analysis costs before and after a
 research project is complete.   This sampling  and analysis will
 provide MDNR verification of a project's success.
     To date, three sets of plots have been leased  to companies
 doing various types of research.  The three companies are
 Monsanto, doing fate and transport studies on dioxin in the
 environment; Agro-K Corporation, doing tests  on enzymatic
 degradation of dioxin; and PPM, doing two separate degradation
 studies using a sodium based compound and biological
 organisms.   In addition, two experiments have been performed
 at the facility without the use of the research plots. J. M.
 Huber Company brought in a pilot version of their  Advanced
 Electric Reactor to incinerate contaminated soil,  and Agro-K
 sponsored research by the RMC  Corporation where a  dilute
 solution of hydrezine was applied to contaminated  soil.
 Following is a brief description of  each of these  projects.

-------
flonsanto;  The purpose of Monsanto's research is to determine

how dioxin in the environment behaves. They hope to establish

whether dioxin gradually degrades naturally.  First round

sampling on their plots is inconclusive at this time.



Agro-K;  Currently, Agro-K is applying a solution of enzymes

to their plots to determine if the enzymes are capable of

digesting dioxin. First round sampling on this process is

inconclusive. Agro-K has also sponsored research proposed by

RMC Corporation to determine if a dilute solution of hydrazine
                ,                •       •
applied to the soil is effective at destroying dioxin.

Hydrazine solution was applied to trays of soil over a period

of several days.  First round results  indicate no significant

reduction in dioxin levels.  A second  round of treatment with

hydrazine solution is currently underway.



J. M. Huber;  The Advanced Electric Reactor, which was

demonstrated in November of 196M, successfully reduced the

level of dioxin in contaminated soil to well below the 1 ppb

safety level designated by the Centers for Disease Control

(COO.  The original level of contamination in the soil  was

120 ppb.



PPM;  This company's research using both a sodium based

compound and biological organisms has  also been  inconclusive

to date.

-------
  APPENDIX  E
OPERATING LOGS

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                          '  OPERATING LOG
 USTOMER:         ~) r A 1
       TDIE METER J<* 7/HRS Q_
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TIME
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DAY
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       SETTING
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-------

-------
                          SIIIRCO MOBILE PILOT
                            OPERATING LOG
CUSTOMER:
RUNNING TDK METER
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                                                              DATE:
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-------
SH1RCO MOBILE PILOT
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-------

-------
   SHIRCO MOBILE PILOT
     OPERATING LOG
CUSTOMER:
RUNNING TIME METER
HRS
DATE:
OPERATOR:
TIME
or
DAY

-------
                    H.OU
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MATERIAL
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                                                                                                       COJWEHTS

-------

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	 	 — — 	 	

COKHEOTS
	 	 	 . 	









•

























-------
          APPENDIX  F








UNIVERSITY OF MISSOURI, COLUMBIA





   LABORATORY ANALYSIS REPORT

-------
                                                     Environmental Trace Substances Research Center

                                                                              Route 3 Sinclair Road
UNIVERSITY OF MISSOURI                                                     SSX
                                        August 8,  1985
     Robert  J.  Schreiber,  Jr.
     Director
     Division  of  Environmental Quality
     Missouri  Department  of Natural Resources
     P.O. Box  1368
     2010 Missouri  Blvd.
     Jefferson City,  MO   65102

     Dear Mr.  Schrieber:

          The  results of  tetrachlorodibenzo-p-dioxin  residue  analysis of three
     samples are  enclosed.   Please feel free to contact  me  for any questions you
     have regarding these  analysis.

                                        Sincerely,
                                         . Kapila, Ph.D.
                                        Group Leader
     SK:ds

     Enclosure
                       COLUMBIA   KANSAS CITY    ROLLA    ST. LOUIS

                                     «n «qu*l ootxxlinty nstKuien

-------
Customer:
Robert Schreiber,  Jr.  - DNR
ETSRC ID:
                  85070717 - 85070719
       The attached pages, have been checked and  vetitled.
                                                      Date
                                                      Date
                                                      Dace

-------
, sis summary    "*et_
ML 0
5-0276
5-0277
5-0988
5-0276




-

ETSRC t
85070717
85070718
85070719
8507071 7Du
Reagent
Blank

-
•
'
•
SML Wet
Weight
10.0
10.0
• 10.0
i 10.0

-
•

• . -•
•
Cone
R/KC
<1.0
306.0
<1.0
<1.0
<1.0






Z Rec.
70.9
89.0
104.3
99.0
90.1

:.



Ion Count (Area)
257
B
99438
1190
B
B
-
•

. •

320
B
177182
B
B
B



-
i
322
135
229828
B
B
B


•
•

328
1289
2946
1601
2083
1403





332
3329
4668
5145
4631
4409





334
4363
5507-
6403
6093
5546





Ratio
320/322
- •
0.77
•_-

-



-
•
Comments
Data File:
TCDDSMLl
Date File: TCDDSML
Data File: TCDDSML
Data File: TCDDSML
Data File: TCDDSML

•




-------
                                RESULT SUMMARY

Analyte:  2,3,7,8 Tetrachlorodibenzo-p-dioxin
Sample Matrix:  Soil and Soil + Water
Sample Source:  Missouri Department of Natural Resources
Date Analyzed:  August 5, 1985
Analyst:  S. Kapila

         Sample *        ETSRC ID       2,3,7,8 TCDD Cone.
          85-0276        85070717                   <1.0
          85-0277        85070718                  306.0
          85-0988        85070719                   <1.0
                            Reagent Blank Analysis
                              Duplicate Analysis

          85-0276                                   <1.0
          85-0276 Duplicate                         <1.0
                                 Z Rel. Dif.         0.0

-------
                      Environmental Trace Substances Research Center

                            INITIAL QC CALIBRATION DATA
.
2,3,7,8 Tetrachlorodibenzo-p-dioxin
Quantltation Mass 322
2,3,7,8 Tetrachlorodibenzo-p-dioxin
Cl-37
•
•
.
i
i
i
I

.


t
. RT
17. 47

17.47



-







•
R 150
3385


26. 942











b
. R 400
10199

123111










'

b
R 1000
28395







.




•

c
~RF
25.4

24.6
26.9




•






ccd
0.9997














Notes:
       a    RT Is the average      .    retention time
       b    R  is the          response        at the level indicated
           	J.150, 400 and 1000 picograms)
       c  '  RT is the average          response factor
       d   CC is the correlation coefficient of the multilevel calibration
             data for each compound .
       1   500 picograms
       2   100  picograms       •                  ,

-------
   1C5-
                                     INITIAL CALIBRATION

1
I :
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t p
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                                    AMI. INJ  (PICOGRAMS)

-------
                        Environmental Trace Substances Research  Center

                                   ONGOING QC DATA  '
Name
2 ^,7,8 Tetrachlorodibenzo-p-diox

'





.


...


	 a
RF
Aup.. 5:85-1
.n 28. A-












i
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A
Aug. 5:85-1
28.5 •
•
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Notes:
             RF is                  response factor  from  Che  most  recent
              initial calibration.

            Report the date the  RF was obtained,  and  the data  file  name.
            Use letters (A, D,  C, etc.) for more than  one data  point on a
            'single day.

-------
             Hnvironmcn tnl Trace Substances Research Cetitcr
          IA - CC/N5 PERFORMANCE STANDARD - D«caf luototrlph«ny lpho»phiQ«
          Data  8/5/85    Run no.  DFTPP1      An*ly»t     SK
-/•
31
68
70
127
197
198
199
273
363
441
442
443
Ion Abundanc* Crit*ri*
30-601 of MIS 198
!«•• than 21 of iu«« 69
•
!«•• than 21 of- BAB* 69
40-60X of «*•• 198
ICCB ttvaa IX of »«•• 198
b«i« p«*k, 1001 r«l«ci.T* abundAoe*
3-91 of MSC 198
10-301 of •*•• 198
greater than 1Z of m*»t 198
!••• thaa »*•• 443
gr«*car thaa. 40X of •*•• 198
17-23X of »..• 442
SPEC /
A4.2
0
0
42.3
0.75
100
6.8
21.6
2.2
14.9 ^^
x/9.3
62.4
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•








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•

Coaa«nta i
•

Column  description  30 M.   _DB-5
T««p«r«tur.   120-260°
Scan Time    0-5 sec.	
laoth* ma 1
Tailing Factor
8 per n>in.
Base/Neutral
Benzidine

Acids
Pcntachlorophenol


-------
              APPENDIX  G
PERSONNEL HEALTH MONITORING DATA

-------
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-------
     RIEDEL

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-------
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-------
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-------
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-------