United States        Office of Water         July 1982
            Environmental Protection   Regulations and Standards (WH-553) EPA-440/4-85-018
            Agency          Washington DC 20460


            Water                 "
T/EPA      An Exposure
            and Risk Assessment
            for Trichloroethanes

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                                     DISCLAIMER

This is a contractor's final report, which has been reviewed by the Monitoring and Data Support
Division, U.S. EPA. The contents do riot necessarily reflect the views and policies of the U.S.
Environmental  Protection Agency,  nor  does mention  of trade names or  commercial products
constitute endorsement or recommendation for use.

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 0572-10?
REPORT DOCUMENTATION »• «PORT "«• *•
PAGE EPA-440/4-85-018
4. TOe and Subtitle
An Exposure and Risk Assessment for Trichloroethanes
1,1, 1-Tr ichloroethane 1 , 1 , 2-Tr ichloroethane
7. Authors Thomas, R. ; Byrne, M. ; Gilbert, D.;
Goyer, M. ; and Wood, M.
9. Performing Organization Name and Address
Arthur D. Little, Inc.
20 Acorn Park
Cambridge, MA 02140
12. Sponsoring Organization Nam* and Address
Monitoring and Data Support Division
Office of Water Regulations and Standards
U.S. Environmental Protection Agency
Washington, D.C. 20460
3. Recipient's Acea«slon No.
5. Raport Oat* Final Revision
July 1982
6.
8. Parformmg Organization Rapt. No.
10, Project/Taak/Work Unit No.
11. Contract(C) or Grant(G) No.
(0 68-01-6160
(G)
IX Typ* of Raport & Parlod Covered
Final
14.
15. Supplamantary Notes
'  Extensive Bibliographies
IS. Abatract (Limit 200 word*)

  This  report  assesses  the  risk  of  exposure   to   1,1,1-trichloroethane  and   1,1,2-
  trichloroethane.   This  study  is part  of  a  program to  identify  the  sources  of  and
  evaluate  exposure  to 129  priority  pollutants.   The  analysis  is  based  on available
  information from government, industry,  and technical publications assembled  in March of
  1981.

  The  assessment  includes  an  identification  of  releases  to  the  environment   during
  production, use, or  disposal of  the substance.   In addition,  the fate  of  trichloro-
  ethanes in the  environment  is  considered;  ambient  levels to which  various populations
  of humans and aquatic life are  exposed  are  reported.   Exposure levels  are estimated
  and available  data on toxicity are presented and interpreted.   Information  concerning
  all  of  these  topics  is  combined  in an  assessment  of the risks of exposure  to  tri-
  chloroethanes  for various subpopulations.
17. Document Analyai* a. Descriptor*
  Exposure
  Risk
  Water Pollution
  Air Pollution
  b. Identlflers/Open-Ended T«rma

  Pollutant Pathways
  Risk Assessment
  e. COSATI Hold/Group  Q6F  06T
Effluents
Waste Disposal
Food Contamination
Toxic Diseases
Trichloroethanes
1,1,1-Trichloroethane
1,1,2-Trichloroethane
                   U.S  Environmental Protection Agencjj
                   Region V, Library               ^-  '
                   230 South  Dearborn Street   ^
                   Chicago, Illinois  60604
ft. Availability Statement
Release to Public
19. Security Claaa (This Raport)
Unclassified
20. Security Ctatt (This Paga)
Unclassified
21. No. of Pagaa
180
22. Price
$17.50
                                      See Instruction* on fl*v*r*e
                                                                              OPTIONAL FORM 272 (4-77)
                                                                              (Formerly NTIS-35)
                                                                              Department of Commerce

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          AN EXPOSURE AND RISK ASSESSMENT

               FOR TRICHLOROETHANES

              1,1,1-Trichloroethane
              1,1,2-Trichloroethane
                                            EPA-440/4-85-018
                                            March 1981
                                            (Revised July 1982)
                      by

                Richard Thomas
          Melanie Byrne, Diane Gilbert
          Muriel Goyer, and Melba Wood
              Arthur D. Little, Inc.

          U.S. EPA Contract 68-01-6160


        Patricia Cruse and Stephen Wendt
               Acurex Corporation

          U.S. EPA Contract 68-01-6017


                 Charles Delos
                Project Manager
    U.S.  Environmental Protection  Agency
                                            »
Monitoring and Data Support Division  (WH-553)
  Office of Water Regulations and Standards
           Washington, D.C.  20460
  OFFICE OF WATER REGULATIONS AND STANDARDS
               OFFICE OF WATER
    U.S. ENVIRONMENTAL PROTECTION AGENCY
           WASHINGTON, D.C.    20460

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                               FOREWORD
     Effective  regulatory  action  for  toxic  chemicals  requires  an
understanding of the human and environmental risks associated with the
manufacture, use,  and disposal  of  the chemical.  Assessment  of risk
requires  a  scientific judgment  about  the probability of harm to the
environment resulting from known or potential environmental concentra-
tions.   The risk  assessment process  integrates health  effects data
(e.g., carcinogenicity,  teratogenicity)  with  information on exposure.
The components of exposure include an evaluation of the sources of the
chemical, exposure pathways, ambient  levels,  and an identification of
exposed populations including humans and aquatic life.

     This assessment  was performed  as part of a program to determine
the  environmental risks associated  with  current use  and  disposal
patterns  for  65 chemicals and  classes of chemicals  (expanded to 129
"priority pollutants") named in the 1977 Clean Water Act.  It includes
an assessment of  risk for humans and aquatic life and  is  intended to
serve  as  a technical  basis  for  developing  the  most  appropriate and
effective strategy for mitigating these risks.

     This  document  is  a contractors1  final  report.    It  has  been
extensively reviewed  by  the  individual contractors pnd  by  the EPA at
several stages of completion.   Each  chapter  of  the draft was reviewed
by members of the authoring contractor's senior technical staff (e.g.,
toxicologists, environmental  scientists)  who had  not  previously been
directly  involved  in  the work.  These  individuals  were selected  by
management  to  be  the technical  peers of the  chapter  authors.   The
chapters  were  comprehensively checked  for uniformity in quality and
content by the contractor's editorial team, which also was responsible
for  the   production  of  the  final  report.   The contractor's  senior
project  management   subsequently reviewed  the  final report  in  its
entirety.

     At  EPA a  senior staff member  was  responsible  for guiding the
contractors, reviewing the manuscripts, and soliciting comments,  where
appropriate, from related programs  within EPA (e.g., Office  of  Toxic
Substances,  Research  and   Development,  Air   Programs,   Solid  and
Hazardous  Waste,  etc.).  A  complete  draft was summarized  by  the
assigned  EPA staff  member  and  reviewed for   technical  and  policy
implications with the  Office Director  (formerly  the  Deputy Assistant
Administrator)  of Water  Regulations  and  Standards.   Subsequent  revi-
sions were included in the final report.
                         Michael W. Slimak, Chief
                         Exposure Assessment Section
                         Monitoring & Data Support Division (WH-553)
                         Office of Water Regulations and Standards
                                  iii

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                           TABLE OF CONTENTS
 LIST OF FIGURES

 LIST OF TABLES                                                   x

 ACKNOWLEDGMENTS                                              xiii



 EPA PROGRAM CONSIDERATIONS                                      xv

 1.0  TECHNICAL  SUMMARY                                        1-1

 2.0  INTRODUCTION                                              2-1

 3.0  MATERIALS  BALANCE                                        3-1

 3.1  Introduction                                              3-1
 3.2  Summary                                                  3-1
 3.3  Manufacture of 1,1,1-Trichloroethane                      3-3
      3.3.1   Vinyl Chloride Process                             3-3
      3.3.2   Environmental Releases from the Vinyl              3-5
             Chloride Process
      3.3.3   Chlorination of Ethane                             3-5
      3.3.4   Environmental Releases from the Direct             3-7
             Chlorination Process
 3.4  Inadvertent Sources of 1,1,1-Trichloroethane              3-7
      3.4.1   Vinyl Chloride Manufacture                         3-7
      3.4.2   Chlorination of Water                              3-10
 3.5  Uses of 1,1,1-Trichloroethane                             3-11
      3.5.1  Degreasing Operations                              3-11
      3.5.2  Cold Cleaning                                      3-11
      3.5.3  Open-top Vapor Degreasing                          3-16
      3.5.4  Conveyorized Vapor Degreasing                      3-16
      3.5.5  Fabric Scouring                                    3-16
      3.5.6  Aerosol Formulation                                3-19
      3.5.7  Adhesives and Coatings                             3-19
      3.5.8  Small-Volume Uses of 1,1,1-Trichloroethane         3-21
      3.5.9  Paints                                             3-21
      3.5.10 Film Cleaning                                      3-21
      3.5.11 Leather Tanning                                    3-21
      3.5.12 Miscellaneous Small-Volume Uses                    3-22
3.6  Municipal Disposal of 1,1,1-Trichloroethane               3-22
3.7  Production and Use of 1,1,2-Trichloroethane               3-23

References                                                     3-27

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                     TABLE OF CONTENTS (Continued)
 4.0  ENVIRONMENTAL DISTRIBUTION                                    4-1

 4.1  Introduction                                                  4_^
 4.2  Monitoring Data                                               4_^
 4.3  Environmental Fate                                            4-14
      4.3.1  Overview                                               4-14
      4.3.2  Aquatic Fate Processes                                  4-14
             4.3.2.1 Hydrolysis                                    4-14
             4.3.2.2 Sorption  onto  Sediments                        4-16
             4.3.2.3 Volatilization from Water                      4-16
             4.3.2.4 Biodegradation                                4-17
      4.3.3  Soil  Transport and  Volatilization                       4-17
      4.3.4  Atmospheric Fate Processes                              4_2Q
 4.4  Modeling of  Environmental  Distribution                         4-20
      4.4.1  Ambient Concentrations                                  4-20
      4.4.2  EXAMS Model Results                                     4_2i

 References                                                         4-31

 5.0   EFFECTS AND EXPOSURE—HUMANS                                   5_i

 5.1   Human Toxicity                                                c _i
      5.1.1  1,1,1-Trichloroethane                                   5-1
             5.1.1.1 Introduction                                   5_1
             5.1.1.2  Metabolism and Bioaccumulation.                 5-1
             5.1.1.3  Human and Animal Studies                       5-5
      5.1.2   1,1,2-Trichloroethane                                   5.9
            5.1.2.1  Introduction                                  5.9
            5.1.2.2  Metabolism and Bioaccumulation                5-9
            5.1.2.3  Human and Animal Studies                      5-10
      5.1.3  Overview                                               5-12
            5.1.3.1  Ambient Water Quality Criteria -              5-12
                     Human Health
            5.1.3.2  Other Human Effects Considerations            5-13
     5.1.4  Estimates of Human Dose-Response Relationships         5-15
            5.1.4.1  1,1,1-Trichloroethane                         5-15
            5.1.4.2  1,1,2-Trichloroethane                         5-15
5.2  Human Exposure                                                5-22
     5.2.1  Introduction                                           5-22
     5.2.2  Exposure through Ingestion                             5-22
            5.2.2.1  1,1,1-Trichloroethane                         5-22
            5.2.2.2  1,1,2-Trichloroethane                         5-23
                                  vi

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                      TABLE OF CONTENTS (Continued)
      5.2.3  Exposure through Inhalation                             5-24
             5.2.3.1  1,1,1-Trichloroethane                          5-24
             5.2.3.2  1,1,2-Trichloroethane                          5-25
      5.2.4  Percutaneous Exposure                                   5-28
             5.2.4.1  1,1,1-Trichloroethane                          5-28
             5.2.4.2  1,1,2-Trichloroethane                          5-28
      5.2.5  Total Exposure Scenarios                                5-29
             5.2.5.1  1,1,1-Trichloroethane                          5-29
             5.2.5.2  1,1,2-Trichloroethane                          5-29

 References                                                          5-32


 6.0   EFFECTS AND  EXPOSURE—NON-HUMAN BIOTA                          6-1

 6.1   Effects on Biota                                                6-1
      6.1.1 Freshwater Species                                       6-1
      6.1.2 Saltwater Species                                        6-1
      6.1.3 Phototoxicity                                           6-1
      6.1.4 Biological Fate                                          6-3
      6.1.5 Conclusions                                              6-3
 6.2   Exposure of  Biota                                               6-3

 References                                                          6-5

 7.0   RISK  CONSIDERATIONS                                             7_!

 7.1   Risks to Humans                                                 7_1
      7.1.1 1,1,1-Trichloroethane                                    7-1
      7.1.2 1,1,2-Trichloroethane                                    7-1
 7.2   Risk  to Aquatic Biota                                           7-2

 Appendix A Supporting Notes to Chapter 3                           A-l

 Appendix B Vinyl Chloride Manufacture via the Balanced Process     B-l

Appendix C  Solvent Recycle Calculations                            C-l

Appendix D  Estimation of Volatilization from Water                 D-l

Appendix E  Atmospheric Fate of Trichloroethanes                    E-l
                                  vii

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                            LIST OF FIGURES

 Figure
   No-                                                          Page

 3-1 Materials Balance:  1,1,1-Trichloroethane,  1979            3-2

 3-2 Water Releases  from 1,1,1-Trichloroethane  Production      3-4
     via Vinyl Chloride  Process

 3-3 Waste Releases  from 1,1,1-Trichloroethane  Production      3-8
     via Direct Chlorination  of Ethane

 3-4 Geographic Distribution  of Cold Cleaning Operations       3-17

 3-5 Geographic Distribution  of Vapor Degreasing Operations    3-17

 3-6 Geographic Distribution  of Fabric  Scouring Operations     3-18

 3-7 Geographic Distribution  of the Adhesives Industries       3-20

 4-1 Fraction  of 1,1,1-  and 1,1,2-Trichloroethane Remaining    4-18
     During Biodegradation Tests

 4-2 Percentage of Trichloroethane Loss due to Volatilization  4-28
     as  a Function of Distance  from Point Source

 E-l Mixing Ratio Distribution  of 1,1,1-Trichloroefhane as a   E-3
     Function  of Tropopause Height   March 1976, 4V°N
     Latitude

 E-2 Mixing Ratio Distribution  of 1,1,1-Trichloroethane as a  E-3
     Function of Tropopause Height, April 1977,  37°N
     Latitude

 E-3  Mixing Ratio Distribution of 1,1,1-Trichloroethane as a  E-4
     Function of Tropopause Height, July 1977,  9°N Latitude

 E-4  Global Distribution of 1,1,1-Trichloroethane by Latitude E-5
     in Late 1977

 E-5  Latitudinal Gradient of 1,1,1-Trichloroethane Corrected  E-5
     to November 1978

 E-6  Diurnal Variations in Atmospheric Levels of 1,1,1-       E-6
     Trichloroethane in New York City

E-7  Atmospheric Levels of 1,1,1-Trichloroethane in Nonurban  E-6
     Areas due to Transport from Urban Areas
                                 viii

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                     LIST OF FIGURES (Continued)

Figure
 No-                                                          Page

E-8  Weekly Averages from Continuous Ground Monitoring        E-9
     of 1,1,1-Trichloroethane Levels, June 1977 through
     January 1979, 47°N Latitude

E-9  Observed NH and SH Mixing Ratios for 1,1,1-Trichloro-    E-9
     ethane

E-10 Atmospheric Levels of 1,1,1-Trichloroethane, 1972-       E-10
     1978, Northern Hemisphere

E-ll Total Ozone Losses for Various Scenarios                 E-10
                                 ix

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                             LIST  OF  TABLES

 Table
 No.                                                            Page

 3-1  Environmental Releases  of  1,1,1-Trichloroethane           3-6
     During Production by  the Vinyl  Chloride Process,  1979

 3-2  Environmental Releases  of  1,1,1-Trichloroethane           3-9
     During Production by  the Ethane Process, 1979

 3-3  Use of 1,1,1-Trichloroethane and Estimated                3-12
     Environmental Releases, 1979

 3-4  Estimated Environmental Releases of 1,1,1-Trichloro-      3-14
     ethane from Degreasing Operations, 1979

 3-5  Production, Use, and  Estimated  Environmental Dispersion   3-24
     of 1,1,2-Trichloroethane in 1979

 4-1  Concentrations of 1,1,1-Trichloroethanes Detected in the  4-2
     Atmosphere

 4-2  Concentrations of Trichloroethanes Detected in- Water

 4-3  Status of STORET Data for Concentrations of 1,1,1-
     Trichloroethane in Ambient Water and Effluents

 4-4  Distribution of Unremarked Values in STORET for          4-10
     Concentrations of 1,1,1- and 1,1,2-Trichloroethane
     in Ambient Water and Effluents

 4-5  STORET Data Concerning Concentrations of Trichloro-      4-11
     ethanes in Sediment

4-6  STORET Data Concerning Levels of Trichloroethanes        4-12
     in Fish Tissue

4-7  Levels of 1,1,1-Trichloroethane Detected in Foods in     4-13
     the U.K.

4-8  Physical Properties  of 1,1,1-Trichloroethane arid  1,1,2-  4-15
     Trichloroethane

4-9  Fate of 1,1,2-Trichloroethane Applied to a  Soil Column   4-19
     in the Laboratory

4-10 Input Parameters  for Trichloroethanes Used  in EXAMS       4-22
     Analysis

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                      LIST OF TABLES (Continued)
 Table
 No.
                                                                     Page

 4-11  Flow and Depth of EXAMS Simulated Aquatic Systems             4-23

 4-12  Steady State Concentrations in Various Generalized            4-24
       Aquatic Systems Resulting from Continuous 1,1,1-
       Trichloroethane Discharge at 1.0 kg/hr

 4-13  The Fate of 1,1,1-Trichloroethane in Various                  4-25
       Generalized Aquatic Systems

 4-14  Steady-State Concentrations in Various Generalized            4-26
       Aquatic Systems Resulting from Continuous 1,1,2-
       Trichloroethane Discharge at 1.0 kg/hr

 4-15  The Fate of 1,1,2-Trichloroethane in Various Generalized       4-27
       Aquatic Systems

 4-16  Half-Lives  for  Trichloroethanes in Generalized Aquatic         4-30
       Systems

 5-1    Pulmonary Elimination  of  1,1,1-Trichloroethane in  Humans       5-2

 5-2    Incidence of Hepatocellular Carcinoma in  B6C3F1  Mice Fed       5-11
       1,1,2-Trichloroethane  For 76 Weeks

 5-3    Conversion  of Carcinogenicity Data for  1,1,2-Trichloro-        5-17
       ethane  into  Equivalent Human Doses

 5-4    Estimated Lifetime Excess Probability of  Cancer  in Humans      5-21
       due  to  1,1,2-Trichloroethane Absorption at Various Dose
       Levels  Based on Four Extrapolation Models

 5-5    Estimated Daily Human Exposure  to  1,1,1-Trichloroethane       5-26

 5-6    Estimated Daily Human Exposure  to  1,1,2-Trichloroethane       5-27

 5-7   Total Exposure Scenarios for 1,1,1-Trichloroethane            5-30

 6-1   Acute Toxicity of 1,1,1- and 1,1,2-Trichloroethane for        6-2
      Freshwater Species

6-2   Acute Toxicity of 1,1,1-Trichloroethanes for Saltwater        6-2
      Species
                                   xi

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                      LIST OF TABLES  (Continued)
                                                                     Page
7-1   Estimated Lifetime Excess Probability of Cancer in Humans      7-3
      due to Absorption of 1,1,2-Trichloroethane at Doses of
      0.6 mg/day and 1.3 ug/day on the Basis of Four Extrapola-
      tion Models

D-l   Measured Reaeration Coefficient Ratios for High-               D-6
      Volatility Compounds
                                 xii

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                           ACKNOWLEDGMENTS

     The Arthur D. Little, Inc. task manager for this study was
Richard G. Thomas.  Major contributors to this report were Melanie
Byrne  (Biological Effects and Biota Exposure), Diane Gilbert  (Human
Exposure), Muriel Goyer  (Human Effects), and Melba Wood (Monitoring
Data).  In addition, Kate Scow did the EXAMS analysis, Elizabeth Cole
provided substantial inputs to the human effects section, John Ostlund
estimated dose/response  for 1,1,2-trichloroethane and Jane Metzger
and Nina Green edited and documented the report.

     The materials balance for the trichloroethanes (Chapter 3.0) was
provided by Acurex, Inc., produced under contract 68-01-6017 to the
Monitoring and Data Support Division (MDSD), Office of Water Regulations
and Standards (OWRS), U.S. EPA.  Patricia Cruse was the task manager
for Acurex, Inc.

     Charles Delos, MDSD, was the project manager at EPA.
                                xiii

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                      EPA PROGRAM CONSIDERATIONS


     1,1,1-Trichloroethane (often called methyl chloroform) is widely
used as a solvent and in related applications.  Concern about this chemi-
cal stems perhaps less from its toxicity (which is relatively low) than
from its role in depleting ozone.  The other isomer, 1,1,2-trichloroethane
(occasionally called vinyl trichloride) is used primarily as a feedstock.
Although it has substantial toxicity and suspected carcinogenicity, its
environmental distribution is somewhat limited.

     U.S. production of 1,1,1-trichloroethane in 1979 was 322,000 MT/yr,
which represents somewhat less than half of worldwide production.   About
68% of production was consumed domestically as a degreasing solvent
(mostly for metal), and thereby released mostly to the atmosphere.  Recycle
and reuse was practiced to a very limited extent in this application,
resulting in total degreasing use being about 16% greater than degreasing
consumption.  The remaining uses dissipate the chemical almost entirely
to the atmosphere:  7% of production as an aerosol propellant, 7% in adhe-
sives and coatings, and 7% in other solvent uses.  Some 10% of production
was exported or stockpiled.  The ultimate disposition of the total domes-
tic consumption is as follows:  84% to air, 10% to land, 4% to water or
sewage, and 2% destroyed by incineration.  About 80% of the chemical dis-
posed of in sewers is volatilized before discharge.

     U.S. production of 1,1,2-trichloroethane is estimated to be  roughly
190,000 MT/yr.  The exact quantity is  the proprietary information of Dow
Chemical Company, the sole producer, which captively consumes most of  it
as a feedstock to produce 1,1-dichloroethylene.  Dow indicated that  they
sell a small amount, in the "low millions of  pounds" (low  thousands  of
metric tons), to various other  industries.  Although small quantities  of
1,1,2-trichloroethane are also  produced  inadvertently during production
of other  chlorinated hydrocarbons, the quantities  released to  the environ-
ment during both intentional  and  inadvertent  production appear to be
negligible compared  to  the quantity which Dow markets to other industries.
No  information  is available on  how these "low millions of  pounds" are
consumed; however, under  the  worst case  assumption that none  of  it is
destroyed through use as  a feedstock,  then  roughly 70-90%  might  be
expected to be  emitted  to  air,  10-30% disposed  on  land, and  a few percent
discharged  to water, based on disposal patterns of other chlorinated
ethanes  and  ethenes.  Obtaining an independent  estimate of environmental
releases by  comparing the  levels of  the 1,1,1- and 1,1,2-  isomers found
in urban air,  then  perhaps  10,000-20,000 MT/yr might be estimated to be
released to  the environment.

      1,1,1-Trichloroethane  is one of the most frequently detected organic
priority pollutants in  municipal and industrial wastewaters.   The Effluent
Guidelines  Division detected  it at least once in nearly  all industrial
 categories;  it  was  found particularly often in Mechanical  Products and
 Provided by Charles Delos, EPA Program Manager.
                                  xv

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Paint & Ink, as well as in the Electrical, Pharmaceutical, Photographic,
and Organics & Plastics industries.  1,1,2-Trichloroethane, on the other
hand, is detected with intermediate frequency relative to other priority
pollutants; it was most often found in Mechanical Products, Paint & Ink,
and Petroleum Refining industries.

     After discharge to surface water, both trichloroethanes tend to
partition toward the atmosphere.  The half-life for this process often
ranges from a few hours to a few days (corresponding to a distance of
perhaps a few miles to a few dozen miles).  In the lower atmosphere
1,1,1-trichloroethane is quite stable, with half-life estimates ranging
from one to several years.  Consequently, the substance has the opportun-
ity to diffuse to the stratosphere where it contributes to depletion of
ozone.  The half-life of 1,1,2-trichloroethane in the atmosphere is
shorter, measured in months; ozone depletion is not a concern for this
substance.

     Trichloroethanes do not bind particularly tightly to soils.
Consequently, in disposing of them as a solid waste, migration from the
dump site can be expected to occur by volatilization or percolation,
unless preventive measures are practiced.  In groundwater, 1,1,1-
trichloroethane might decompose (by hydrolysis) with a half-life of
perhaps 6 months or longer to hydrochloric and acetic acids.  Some
dichloroethylene, which itself decomposes at about the same rate, may be
formed.  1,1,2-Trichloroethane is expected to behave similarly in
groundwater.  It can be concluded that effective disposal of trichloro-
ethanes must result in containment of the substances within the site for
a time period long enough for decomposition to take place.  Adsorption
to a solid phase may or may not reduce decomposition with the same effec-
tiveness that it reduces migration.  If sorption were to slow both proc-
esses equally, then its overall effect would simply be to delay rather
than to prevent migration.

     The toxicity of 1,1,1-trichloroethane is somewhat less than most of
the similar solvents.  Animal tests have not shown it to be carcinogenic
or teratogenic; however, the results are not considered to be conclusive.
The National Cancer Institute was scheduled to complete further testing
in 1981.  It has been shown to be weakly mutagenic.  EPA's water quality
criterion for protection of human health is 18,400 ug/1.  Acute toxicity
to aquatic life has not been found at levels below several thousand yg/1.

     The toxicity of 1,1,2-trichloroethane, on the other hand, is more
substantial.  Of most concern is the carcinogenicity shown in animal
tests.  EPA's  water quality criterion for protection of human health is
6 wg/1 (10   risk).  In contrast to its toxicity to mammals, its toxicity
to aquatic life appears to be similar to the 1,1,1- isomer.

     Consistent with the trichloroethanes'  tendency to partition to the
atmosphere, where they are fairly stable to decomposition, most exposure
is found to result from air rather than water contamination.  For 1,1,1-
trichloroethane, urban air sampling has indicated a mean concentration of
                                 xvi

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3.3 ug/m .  Drinking water surveys have suggested a mean concentration
in the neighborhood of 0.1 ug/1.  Assuming inhalation of about 20 m /day
and ingestion of 2 I/day, the aggregate exposure to this compound is far
greater via air than via water.  Although the data on food contamination
is limited and unreliable, it suggests that exposure via food may be in-
termediate between air and drinking water.  Exposure through fish is very
small, however.

     Exposure to the more hazardous 1,1,2- isomer is substantially less
than for 1,1,1-trichloroethane., Observed levels of 1,1,2-trichloroethane
in urban air average  0.12 yg/m .  If the Cancer Assessment Group's extra-
polation from animal tests were accurate, long-term exposure to -such a
level would represent a cancer risk of slightly greater than 10  .  If
representative nationwide, such a risk would represent a cancer incidence
of 3-6 cases/year.  For comparison, the observed total cancer incidence
(from all causes) is over 800,000 cases/year.  Aggregate exposure and
risk via drinking water is difficult to quantify because the compound is
so rarely detected in surface and groundwater.

     Overall, it can be concluded from the findings that:

     (1) Trichloroethanes are primarily air pollutants.  Popu-
         lation aggregated exposure appears to be far greater via
         air than via surface and groundwater.

     (2) Unless continuing tests show 1,1,1-trichloroethane to be
         carcinogenic, the concentrations generally found in air,
         surface water, and groundwater are not directly hazardous.
         The total quantities released to the environment might
         contribute to stratospheric ozone depletion, however.

     (3) The levels of 1,1,2-trichloroethane observed in urban
         air might contribute very slightly to cancer risks.  Its
         detection in surface and groundwater is, on the other
         hand, rare.

     (4) Current levels of trichloroethanes in ambient surface
         waters are rarely expected to harm aquatic life.
                                 xvii

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                        1.0  TECHNICAL SUMMARY
     The Monitoring and Data Support Division, Office of Water Regulations
and Standards, the U.S. Environmental Protection Agency, is conducting
an ongoing program to identify the sources of, and evaluate the exposure
to, 129 priority pollutants.  This report assesses the exposure to and
risk associated with the two isomers of trichloroethane:  1,1,1-trichloro-
ethane and 1,1,2-trichloroethane.

1.1  MATERIALS BALANCE

     The compound  1,1,1-trichloroethane, also known as methyl chloroform,
is a high-vapor-pressure organic solvent, primarily used in degreasing
operations and as a component of other products.  The chemical has become
environmentally pervasive due to fugitive emissions during production,
use, and disposal.  The 1,1,2- isomer is also a high-vapor-pressure
organic solvent, but it is used mostly as a feedstock intermediate.
Environmental releases are relatively small compared with the 1,1,1- isomer,
                       i
1.1.1  1,1,1-Trichlorethane

     Approximately 322,000 kkg of 1,1,1-trichloroethane were produced
in 1979.  Production of 1,1,1-trichloroethane has remained relatively
stable since 1976, well below its 7-9% predicted growth rate.  Total
environmental release of the chemical from either the vinyl chloride
or ethane production process is estimated to be 480 kkg (see Table 3.1);
81% (~390 kkg) of the total releases were discharged to POTWs.  Approxi-
mately 80 kkg were emitted to air, and 9 kkg were discharged to land
in 1979.

     About 220,000 kkg (68% of the total produced) were consumed by
degreasing operations.  Such use results in 151,000 kkg of atmospheric
emissions; 24,000 kkg were disposed to land, and 10,000 kkg were sent
to POTWs.  The remaining uses—aerosol vapor depressant, adhesives,
paints, film cleaners, and leather tanning—result almost entirely in
atmospheric emissions.  Of the total 85,000 kkg consumed in such uses,
68,000 kkg (80% of the quantity used) were emitted to air.  Only 420 kkg
were disposed to land and 7 kkg were sent to POTWs.

1.1.2  1,1,2-Trichloroethane

     The 1,1,2- isomer is produced in the U.S. directly or in-
directly from ethylene and is also produced as a co-product in the
manufacture of other chlorinated hydrocarbons.  Its chief use is as a
feedstock intermediate in the production of 1,1-dichloroethylene.
Occasionally, it is used as a solvent for chlorinated rubber manufacture.

     According to the U.S. International Trade Commission, Dow Chemical
is the sole producer of 1,1,2-trichloroethane.  The quantity produced is
                                  1-1

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 proprietary information.  Approximately  180,000  kkg  of  1,1,2-trichloro-
 ethane is  estimated  to  be required  for 1,1-dichloroethylene production.
 This  estimate  represents the maximum  production  potential  and is  probably
 high.

      Environmental releases of  1,1,2-trichloroethane from  1,1-dichloro-
 ethylene manufacture are small.

      Dow Chemical does  sell some 1,1,2-trichloroethane  as  a consumer
 product but the quantity sold is considered proprietary information.
 A spokesperson from  Dow estimated that "low millions of pounds" are
 used  annually in various industries.  Release of 1,1,2-trichloroethane
 to  the environment also results from  the manufacture of other  chlorinated
 hydrocarbons.  Total environmental releases are estimated  to be 5 000
 kkg/yr (1979).

 1.2   FATE AND DISTRIBUTION IN THE ENVIRONMENT

 1.2.1  Concentrations in Environmental Media

      Trichloroethanes have been detected in all environmental  media,
 including food and drinking water, widely throughout  the United States.
 Data  on levels in food  are extremely limited but suggest that  concen-
 trations for the 1,1,1- isomer are in the low yg/kg  range.   Limited semi-
 quantitative data on levels of the 1,1,2- isomer in  fish indicate very
 low levels may be present in this food.   No other data  on levels of
 l»l»2-trichloroethane in foods were available, but,  given the much lower
 volume of environmental releases of 1,1,2-trichloroethane, it  is assumed
 that most foods would contain negligible amounts, if any.

     From semi-quantitative water concentration data, it has been esti-
mated  that about 20% of finished water supplies may contain >1 yg/1 of
 the 1,1,1-  isomer and only isolated instances of >10  yg/1 exist.  Data
on the concentrations of the 1,1,2- isomer in water supplies are extremely
 limited and no meaningful estimates of average concentrations can be
made;  however, on the basis  of a much lower volume of release of this
isomer to the environment,  it is thought that most drinking water supplies
have negligible amounts of the 1,1,2- isomer.

     Air monitoring data for the trichloroethanes Indicate that 1,1,1-
trichloroethane is ubiquitous.   Concentrations in renote areas average
about 0.5 yg/m3 and in urban areas  about 3.3 yg/m3,,  It  is  estimated
that the concentration of 1,1,2-trichloroethane in urban air is generally
about 0.12 yg/m3.

     Ninety percent,  or more,  of sediment concentrations reported in
STORET for both chemicals are less  than  10 ug/kg.

1.2.2   Environmental  Fate

     Because of their high vapor pressures,  trichloroethanes have  high
volatilization rates  relative to those of many other  organic chemicals,
despite the fact  that their  solubilities  are also  quite  high.  The

                                1-2

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 primary waterborne fate pathway for these chemicals is volatilization
 from surface water or soil,  followed by slow photo-oxidation in the
 atmosphere.   For both isomers,  the half-life for volatilization from
 a 1-m deep stream is  estimated  to be 4-5 hours.   Time to  90% loss is
 about 12 hours.   For  a 10-m deep stream, the estimated half-life increases
 to about 1 week  and the time to 90% depletion is about 3  weeks.  The
 distance for 90% to volatilize  is up to 1700 km  downstream from the
 discharge point.

      When 1,1,2-trichloroethane in water solution was applied to a sandy
 soil column in the laboratory,  about one-half volatilized and one-half
 percolated into  the soil column.   These results  indicate  that leaching
 and volatilization are the  important fate processes for 1,1,2-trichloro-
 ethane in soil.   No similar  information has  been found concerning 1,1,1-
 trichloroethane.

      In laboratory studies,  1,1,1-trichloroethane was found  to have a
 hydrolysis half-life  of 6-7  months.   In groundwater aquifers,  where
 other fate processes  do not  operate,  the compound may be  degraded by
 this  process.  If behavior in the environment is  similar  to  results of
 laboratory tests,  it  would take 1.5-2 years  to degrade 90% of the1
 original amount.

      Little  information was  found concerning  the  biodegradation of the
 trichloroethanes.   Biodegradability  studies  conducted in  flasks in the
 laboratory indicated  that both  compounds were degraded  by yeast extract
 and domestic wastewater inoculum.  However, many  other  chlorinated sol-
 vents are resistant to biodegradation,  even  though they exhibit some
 biodegradation in wastewater  treatment  or laboratory  studies.

      The atmospheric  lifetime of  the 1,1,1- isomer is on  the  order of
 6-10  years, long  enough for  global mixing and  transport to the  strato-
 sphere  to  occur.    (Stratospheric mixing  and inter-hemispherical mixing
 occur on a  time scale  on the order of a  year  or less.)  Ozone depletion
 up  to 1.3% of total ozone, depending on  continuing  release of the  chemi-
 cal,  may occur following Cl atom  release by photodecomposition.  The
 1»1»2-  isomer may  be photolyzed more rapidly  than  the 1,1,1- isomer based
 on results of laboratory tests, although little information concerning
 1,1,2-trichloroethane was found.

 1.3   RISKS TO HUMANS

 1.3.1  Human Effects

 1.3.1.1  1,1,1-Trichloroethane

     The compound 1,1,1-trichloroethane has a fairly low  toxicity via
 inhalation due to rapid and  almost total elimination of the compound,
 unchanged, via the  lungs.  The small amount that is metabolized  (less
 than 5% of an inhaled  dose)  is converted by the liver to  trichloroethanol
and trichloroacetic acid and excreted in urine.  Urinary clearance has
                                  1-3

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 an approximate half-life in man of 10-12 hours for trichloroethanol
 and 70-85 hours for trichloroacetic acid.  Although inhalation exposure
 is most common, percutaneous absorption of both liquid and vapor 1,1,1-
 trichloroethane, as well as exposure via ingestion, has been demonstrated
 in humans.

 „ n  In laboratory animals, acute LD5Q's range from 5,000 mg/kg to
 12,000 mg/kg via oral administration End 75-98 g/m3 for 3-7 hours via
 inhalation.   Principal effects of acute exposure in laboratory animals
 are depression of the central nervous system and disturbances in cardiac
 function,  including sensitization of the heart of epinephrine.   In sub-
 chronic inhalation studies,  monkeys,  dogs,  rabbits,  rats  and guinea
 pigs exposed to 15 g/m3,  8  hours  per day,  5 days per week for 6 weeks
 showed some  leukopenia (reduction in the number of white  blood  cells)
 body weight  reduction and nonspecific inflammatory changes.   The liver
 appeared to  be most susceptible to  histopathological changes in guinea
 pigs and mice.

      No adequate carcinogenicity  studies are available for the  determi-
 nation of  carcinogenic risks associated with exposure to  1,1 1-tri-
 chloroethane.   In three studies,  1,1,1-trichloroethane caused no
 significant  increase in tumor incidence in  B6C3F1  mice (4010 mg/kg/day
 by gavage),  Osborne-Mendel rats  (1071 mg/kg/day by  gavage)  or  Sprague-
 Dawley rats  (9.5 g/m3,  6  hours  per  day,  5 days per week for  12  months
 by inhalation);  however,  poor survival of test animals and insufficient
 duration of  study rendered these  data  inadequate for  use  in  an  assessment
 of carcinogenicity.  Further  data on carcinogenicity  and mutagenicity
 are extremely  limited;  weakly positive results were  reported  in one
 strain (TA100)  of  Salmonella  typhimurium and  in one mamalian  cell
 transformation assay.   No teratogenic  effects  associated with 111-
 trichloroethane  exposure were observed  in rats or  mice exposed  to
 4.8  g/m-5 1,1,1-trichloroethane  on days  6-15 of gestation.

     At low  inhalation  exposures of 1,1,1-trichloroethane  (< 5.5 g/m3)
 the  primary  effects  in  man are  psychophysiologic,  including~dose-related
 impairment of  perception and  coordination and  relatively little distur-
 bance  in body  functions.  At higher exposures  (> 44 g/m^)   functional
 depression of  the central nervous system leading to respiratory or
 cardiac failure are noted.  Acute exposures to high levels of the
 compound (> 5.5 to < 44 g/nr*) by accidental contact or abuse, may
 result in transient kidney and  liver dysfunction.  The effects of
 chronic low-level exposures are not known.

 1.3.1.2  1,1,2-Trichloroethang

     Data concerning the toxicity, carcinogenicity,, mutagenicity or
 teratogenicity of 1,1,2-trichloroethane are very limited or non-existent
particularly regarding adverse effects to man.  However, based on the
evidence available, 1,1,2-trichloroethane is considered much more toxic
than the 1,1,1- isomer of  trichloroethane.
                                 1-4

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     Absorption  of  1,1,2-trichloroethane  has been demonstrated  in both
 man  and  animals  following  inhalation  exposure  or  dermal  contact.  In
 laboratory  animals,  fairly rapid  excretion of  73-87%  of  an absorbed dose
 occurs via  the urine,  and  6-8%  of the absorbed dose is expired  unchanged.
 Major urinary metabolites  in mice are S-carboxymethyl cysteine, chloro-
 acetic acid, and thiodiacetic acid, and minor  amounts of trichloroethanol
 and  trichloroacetic  acid.

     The 1,1,2-  isomer has been shown to  cause central nervous  system
 depression  in mice and damage to  the  liver and kidney in mice and dogs
 following single intraperitoneal  injections of 0.07-0.4  ml/kg.  Acute
 exposure in man  appears  to be characterized by a  narcotic effect  on the
 central  nervous  system and eye  and skin irritation, while possible kidney,
 lung, and gastrointestinal damage may result from long-term exposure.

     Data from a study on  carcinogenic effects indicated  that 1,1,2-
 trichloroethane  caused hepatocellular carcinomas  and  pheochromocytomas
 in B6C3F1 mice of both sexes at time-weighted  doses of 195 and  390 mg/kg
 of body  weight/day,  5  days per  week,  administered by  gavage.  Carcino-
 genicity data from a similar study with Osborne-Mendel rats were
 inconclusive.  No adequate data regarding mutagenic or teratogenic
 effects  associated with  1,1,2-trichloroethane  exposure have been  reported.

 1.3.2  Exposure  of Humans

 1.3.2.1   1.1.1-Trichloroethane

     The chemical 1,1,1-trichloroethane is globally pervasive in  air and
 has been found in many samples  of  ground and surface  drinking water.
 It has been detected in  foods in  the  United Kingdom.  Except for  some
 limited  data on  levels in  fish  tissue, no data on  concentrations  in foods
 in the U.S. were  found.  Dermal absorption appears to be  of concern only
 for a relatively  small subpopulation  that handles  the chemical occupa-
 tionally.

     A typical daily urban exposure based on ingestion of contaminated
water and food and inhalation of urban air is  estimated to be about
 40 ug/day/person.  An  upper limit on  the population potentially exposed
 to these  levels is about 150,000,000  people per day.

     For rural dwellers, a  typical exposure is five times less,  9 ug/day/
person.   Some 53,000,000 people per day might be exposed at this level.

     Populations  living near user or manufacturing sites may have exposures
up to 2200 yg/day/person due to higher ambient air concentrations.  The
size of the exposed population cannot be estimated with reasonable
accuracy.

     Occupational absorption via inhalation and percutaneous routes  may
range up to 11,000 mg/day/person.   This  level may apply to some  of the
130,000 employees in degreasing operations.
                                  1-5

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 1.3.2.2   1,1.2-Trichloroethane

      The  compound  1,1,2-trichloroethane has been  found  in  drinking water
 supplies.   The  estimated  potential  intake  from  drinking water  ranges
 from  negligible to  <2 ug/day/person for the majority  of the  population,
 although  it is  possible that a very small  subpopulation may  ingest up
 to 600 ug/day/person.  Limited air  concentration  data for  1,1,2-trichloro-
 ethane in urban air have  been utilized to  estimate an average  absorption
 of about  1.3  ng/day/person via inhalation.

 1.3.3 Risk Considerations for Humans

 1.3.3.1   1,1,1-Trichloroethane

      Currently  available  data do not indicate that this compound  is
 carcinogenic.   No positive mammalian teratogenic  or mutagenic  effects
 have  been demonstrated.   An acceptable daily intake (ADI)  of 37.5 mg/day/
 person has  been derived.  Estimated urban and rural exposures  are more
 than  500  to 4,000 times less than the estimated AD]:.  No toxic effects
 are expected  from these exposures.  Occupational  exposures from 27 mg/day/
 person to 11,000 mg/day/person have been estimated;; consequently, an
 estimated 130,000 persons (involved in degreasing operations)  may be
 subject to  adverse  health effects.

 1.3.3.2  1,1.2-Trichloroethane

     An NCI study indicates that 1,1,2-trichloroethane is carcinogenic
 in mice but not  rats and  thus is a suspect carcinogen in humans.

      Four risk  extrapolation models were applied to the dose-reponse
 data  obtained in animal experiments to indicate the range -in the pre-
 dicted number of possible lifetime excess cases of cancer that might
 result from chronic human exposure to 1,1,2-trichloroethane.  The range
 of estimated risks  obtained for the human exposure levels of interest
 is indicative of the inherent uncertainty associated with the mathematical
models currently used for risk extrapolation purposes.  There  is presently
 no scientific concensus for selecting the most appropriate model for
 extrapolating high  exposure levels utilized in animal experimentation
 to the much lower levels experienced by the human population.  Each of
 the models  is formulated in such a way that the curves pass through the
 origin; that is, there is some finite response at any dose greater than
 zero.  This concept of no threshold is scientifically debatable, but it
has been the position of some scientists  and of government regulators
 that  thresholds to carcinogens do not exist.   The no-threshold theory
 tends to make the predicted risks obtained "conservative," meaning here,
 to overstate the risk.

      In addition to the uncertainty associated with the choice of the mathe-
matical model, there is large and unquantifiable uncertainty regarding
extrapolating from laboratory animals to humans.  The  guidelines
                                 1-6

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                                                                         -


  1.4  RISKS TO AQUATIC BIOTA

  1-4.1  Toxic Effects
                        7  me/1 for rtl i            ces tested is the
 1.4.2  Exposure of Aquatic Blo<-a
                              m^ritf'f "  ^f  thS C°™ionS  of
basins, and near producton anfuse SL   '"^  J  t3ken fr°m "^ river
The highest value for 11 1-SchlorM' T 6 in the 1<3W Ug/1 ranSe'
manufacturing site was 169 u»7?  ^   5  ne detected downstream of I
 manufacturing site was 169 u»
 concentrations? there is    fve;ianaK   UPOn repOr£ed amb±ent water
 and known effects  levels  liJ,    P between a(luatic exposure levels
 to  occur  at  lL ^ than 1 0 »g/l  "° ""^ " Chr°niC 6ffeCtS are
1'4'3  Risk Considerations  for  AT.a^  Biota
1.0
ambient concentration   rein the low a'  *°nitoring d^ indicate  that
for the two chemicals are not exceedL ?   *?**'  W*ter quality "ite
the U.S.  The risk to aqua?ic organist ^ am^ent °r e«l^nt waters in
negligible.                   organisms is, therefore, assumed to be
                                  1-7

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                          2.0  INTRODUCTION

     The Office of Water Regulations and Standards, Monitoring and
Data Support Division, the U.S. Environmental Protection Agency, is
conducting a program to evaluate the exposure to and risk of 129 priority
pollutants in the nation's environment.  The risks to be evaluated include
potential harm to human beings and deleterious effects on fish and
other biota.  The goal of the task under which this report has been
prepared is to integrate information on cultural ar-d environmental flows
of specific priority pollutants and estimate the ris.v based on recep-
tor exposure to these substances.  The results are intended to serve as
a basis for developing suitable regulatory strategy for reducing the risk,
if such action is indicated.

     This report provides a brief, but comprehensive, summary of the
production, use, distribution, fate, effects, exposure, and potential
risks of 1,1,1-trichloroethane and 1,1,2-trichloroethane.  The 1,1,1-
isomer is more commonly produced and hence detected more often in en-
vironmental media than the 1,1,2-isomer.  Consequently far more informa-
tion is available concerning 1,1,1-trichloroethane and it is dealt with
in far greater detail in each chapter.

     The report is organized as follows:

     Chapter 3.0 presents a materials balance for the trichloroethanes
     that considers quantities of the chemical consumed or produced
     in various processes, the form and amount of pollutant released
     to the environment, the environmental compartment initially
     receiving it, and, to the degree possible, the locations and
     timing of releases.

     Chapter 4.0 describes the distribution of trichloroethanes in the
     environment by presenting available monitoring data for various
     media and by considering the physicochemical and biological fate
     processes that transform or transport the chemicals.

     Chapter 5.0 describes the available data concerning the toxicity
     of trichloroethanes for humans and laboratory animals and quanti-
     fies the likely level of human exposure via major known exposure
     routes.

     Chapter 6.0 considers toxicological effects on and exposure to
     biota, predominantly aquatic biota.

     Chapter 7.0 compares exposure conditions for humans and other
     biota and with the available data on effects levels from
     Chapters 5.0 and 6.0 the risks presented by various exposures
     to the trichloroethanes are estimated.
                                 2-1

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Appendices A-C present more detailed information supporting
materials balance estimates in Chapter 3.0.  Appendix D dis-
cusses the procedure for estimating the volatilization rates of
the trichloroethanes and Appendix E discusses in detail the
atmospheric fate of the compounds.
                           2-2

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                          3.0  MATERIALS BALANCE

  3.1  INTRODUCTION
  tricho ^aPter S'fTJ" ^ environmental materials balance for 1,1,1-
  trichloroethane and 1,1, 2-trichloroethane.
  the to^T       f n!\ither cre«ed nor destroyed in chemical transformations,
  all m^-fT58,   J1   materials entering a system equals the total mass of
  all materials leaving that system, excluding those materials the system
  accumulates or retains.   From the perspective of risk analysis,  a Steals
  balance may be performed around any individual operation that placet a
  specific population at risk (e.g., process water discharges creating
  groundwater contamination).   An environmental materials  balance   therefore
  consists of a collection of  materials  balances,  each  of  which is  theref°re*
  to a specific source and sink within  the  environment.
       The materials balance  is based on a review of both published and
                                                               " -
                                         °c
              ^environmental distribution of 1,1,1-trichloroethane.


 production, use and environmental release'of 1,1,2-trichloroethane"

 3.2  SUMMARY


      Production of 1,1,1-trichloroethane in the  U.S.  has  remained
 relatively stable since  1976,  well  below its 7-9% predicteHrowth rat.
 and below the 12-13%  growth rate  exhibited  between^965 and ?"
 CnP fOmnnnnH  T.rao  •»-,.,,-,1 __ j	^_t_  _    .     .              «•»»«*
                               more hazardous trichloroethyl
the                                            x
capacity for that year was estimated to be 4.8 x 105 kkT 907 of which

"                                                °  k89"f
                               mae  to  e  .8 x 10  kk   907 of which
"l sJo^kfof^01111611 ^ ?Chiff 1979)«  In 1979° thke8U.S9?"profd:c eT


£££ SZ&^^T^^™^™
                     ^
                                  3-1

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  Inadvertent Sources
                             Production (Ug)
  Vinyl Chloride
   Manufacture
("balanced process")*1
Chlorlnatlon of   _
  Water Supplies *
                                                I Stockpiled I
                                                I    M40  J
                                                                      Ul*
Aerosol  Forw-
 latlon
     ?2.53U
Adheslvos and
Coatings
                                                                 ji^n!
                                                                  I     5.790     I
                                                                              IOIAI
                                     Environmental Release (kkg)
210



neg



120
  neg

22.300



22.527



 S.670



   306


   320
                        16,670     negf


                        42.737    28.219
                                    F!s«rs J.!   Mi'srli!- Sjlsscs:   !.!.! IrUfcioroithsr* !9?S


           a) See tot.  Section 3.3.1 for process  description, lablc 3.1 for envlioiwental release AM I, at Ion.

           b) See teal.  Se
-------
 sent to Publicly Owned Treatment Works (POTW's) (390 kkg); about 84 kkg were
 emitted to the atmosphere and 9 kkg were land-disposed.

      The 1,1,1- isomer is used in degreasing, aerosol formulation;  manufacture
 of adhesives, coatings, and paints; leather tanning, film cleaning and other
 miscellaneous solvent operations.  Figure 3-1 lists quantities of the com-
 pound consumed by each use in 1979, as well as the resulting environmental
 releases.  Of the total 282,810 kkg of 1,1,1-trichloroethane released to the
 environment from use of the compound, 86% (242,653 kkg) was emitted to the
 atmosphere, 10% (28,210 kkg) was land-disposed, and 4% (11,947 kkg) was
 sent to  POTWs.  Negligible amounts of 1,1,1-trichloroethane were discharged
 to surface-waters.

 3.3  MANUFACTURE OF 1,1,1-TRICHLOROETHANE1

      The bulk of 1,1,1-trichloroethane production  in the U.S.  is based
 upon the vinyl chloride process; only minor amounts (wlO%)  are made  by
 the ethane process.   In the vinyl chloride process,  vinyl chloride  reacts
 with hydrogen to form 1,1-dichloroethane,  which is then thermally chlorinated
 to produce 1,1,1-trichloroethane.  The yields,  based on vinyl  chloride,
 range from approximately  95% to 98%.   The 1,1,1- isomer is also
 produced by the noncatalytic chlorination of ethane.   Ethyl chloride,
 vinyl chloride,  vinylidene chloride,  and  1,1-dichloroethane are produced
 as by-products.

      The largest releases of 1,1,1-trichloroethane to the  environment
 during  its production,  by both processes,  are to aquatic media.  Nearly
 81% (356 kkg)  of the  total 437 kkg  of 1,1,1-trichloroethane released
 to the  environment during production  via  the vinyl chloride process was
 discharged to  water;  74%  (34 kkg) of  the  total  46  kkg of 1,1,1-trichloro-
 ethane  released  from  the  direct chlorination process  was discharged to
 water.   Atmospheric emissions  from  the vinyl chloride process totaled
 7  kkg while  emissions from the direct  chlorination process  were  10 kkg.
 Land destined  1,1,1-trichloroethane wastes totaled 76  kkg,  74 kkg of which
 were attributable to  the  vinyl chloride process; 2 kkg were released from
 the direct chlorination process.
                 »
 3.3.1  Vinyl Chloride Process

     Figure  3-2 outlines  a  simplified process for production of 1,1,1-
 trichloroethane via vinyl chloride  (see Appendix A, Note 5  and Figure B-l,
Appendix B for further details).  Vinyl chloride, hydrogen  chloride,
FeCl^ catalyst, ammonia, chlorine and stabilizer compounds are introduced
into the system to yield 1,1,1-trichloroethane.  Wastes are generated
from the following point and nonpoint sources: heavy and light end
distillation column vents; miscellaneous wastewater discharges; fugitive
emissions; spent catalyst filters; 1,1,1-trichloroethane column vents;
product storage vents and handling operations.  However, 1,1,1-trichloro-
ethane is released to the environment from only the last five of the above

 TJased on the process description of EPA (1979b).
                                   3-3

-------
OJ
I
•e-
FUGITIVE STORAGE COLUMN
EMISSIONS VENT VENTS
IIC1 TO A , A
. - , 1
^ OTHER [ 1
PROCESSES | 1
: i
VINYL CHLORIDE
IIC1
FeCl-j CATALYST
AMMONIA
CHLORINE
STABILIZER

->
.

PRODUCTION AND STORAGE
RELATING TO VINYL CHLORIDE
PROCESS
FEED TO
OTHER Hf
PROCESSES - SPENT v
/ ' CATALYST *
HANDLING
f
\

\
r^.
*-*
/ M I c r r
STORAGE
VENT
t
• ;> HANDLING
I I
1»1,1-TRICIILOROETHANE onnnnrT '
	 	 ,. .^T* fKUUUtl 	 v^ TRAN'TORTATinM
STORAGE OUT OF Pl ANT
f
^
X
1 1 AMCAlIC
        (1,1,2-TRICHLOROETHANE)
        WASTEWATER
COLUMN  SOURCES
WATER
  Figure 3.2   Waste Releases  from 1,1,1-TMchloroethane Production Via Vinyl Chloride Process*

  "~~]      :'
  a)  |=Air  emissions;«*= water  discharge; and I = land disposal.
  Source:  EPA,  1979a,b.

-------
sources.  Estimated environmental releases of 1,1,1-trichloroethane
from this process are shown in Table 3-1; derivations of these estimates
are given in Table B-l, Appendix B.

3.3.2  Environmental Releases from the Vinyl Chloride Process

     As shown in Table 3-1, nearly 81% (356 kkg) of the total quantity
of 1,1,1-trichloroethane released to the environment from its production
via the vinyl chloride process (437 kkg) was discharged to water, while
approximately 17% (74 kkg) was emitted to the atmosphere and 2% (7 kkg)
was land-disposed.

     The majority (90%) of the 1,1,1-trichloroethane wastes discharged
to water was contained in effluents from refrigerated vent condensers,
which were used to control emissions from product storage and handling
(EPA 1979b) ; liquid wastes generated from both of these sources were
sent to POTWs (EPA 1979b) .  The remaining 35 kkg of 1,1,1-trichloroethane
liquid wastes from the vinyl chloride process stem from the 1,1,1-trichloro-
ethane column (vent TC, Figure B-l, Appendix B) and were also discharged
to POTWs.

     Approximately 74 kkg of 1,1,1-trichloroethane were emitted to the
atmosphere during its production by the vinyl chloride process (Table 3-1) .
Nearly 80% (58 kkg) of these wastes came from product storage and handling.
The remaining atmospheric emissions (Tables 3-1 and B-l, Appendix B)
were a result of 1,1,1-trichloroethane column losses (4 kkg) and fugitive
emissions (12 kkg) .

     Only 7 kkg of 1,1,1-trichloroethane wastes (2% of the tota^l wastes)
were disposed to land.  This waste was a semisolid spent catalyst complex
(NH4'FeCl3-NH3) composed primarily of 1,1,1-trichloroethane (EPA 1979b) .

3.3.3  Chlorination of Ethane

     The compound 1,1,1-trichloroethane is also produced by direct Chlorination
of ethane; small amounts of 1,2-dichloroethane and 1,1,2-trichloroethane
are produced as by-products.  To maximize  1,1,1-trichloroethane production,
ethyl chloride and 1,1-dichloroe thane are recycled to the Chlorination
reactor; vinyl chloride and vinylidene chloride are catalytically
hydrochlorinated to 1,1,-dichloroethane and 1,1,1-trichloroethane,
respectively.

               HC - CHC1 + HC1
                            HC1      :? — > CH3CC13
                                   3-5

-------
 TABLE 3-1  ENVIRONMENTAL RELEASES OF 1,1,1-TRICHLOROETHANE DURING
            PRODUCTION BY THE VINYL CHLORIDE PROCESS, 1979 (kkg)
Producer Quantity Produced Estimated Environmental Releases3
(location) (103 kkg)b Mrc Landd Watere Tocal
Dow Chemical Co. 122
(Freeport, TX)
Dow Chemical Co. 80
(Plaquemine, LA)
PPG Industries, Inc. 95
(Lake Charles, LA)
Total 297
31 3 153 187
20 2 100 122
23 2 103 128
74 7 356 437
a)  Control devices and their removal efficiencies are: product storage
    and handling  (refrigerated vent condensers—85%); 1,1,1-trichloroethane
    vent  (aqueous scrubber/recycle—90%).  See Appendix A for emission
    factors used.

b)  Quantity of 1,1,1-trichloroethane produced from vinyl chloride process
    (297,000 kkg) = total quantity produced minus quantity produced by the
    direct chlorination of ethane (Harris 1980; Philips 1980).

c)  Product storage and handling account for >75%.

d)  Waste composed of spent catalyst complex.

e)  Product storage and handling account for >85%.
Source EPA (1979a,b).
                                  3-6

-------
  gnf^


  2^SL.^^S-tt-^^i.JS«SJSSr-K
  the process, wastes are generated from the following point  and  nonpoint
  sources:  fugitive emissions; distillation column vents;  recycle and
  product  storage vents; spent catalyst filters; handling  operations
  quench column vents; and miscellaneous wastewater sources!  Wastes'
  f* rtn fi*-fn^T»»  7 1 1	*••../_ t_ i —	^.« _
  ov«n                         release<* to the environment from

   £-«f  ^^^
  lu^mL^  hafdlin* °perf lons'  Table 3-2 (and Table B-2 in Appendix B)
  ~ this  roems"!1"'6' e°Vl— tal **-« of  1,1,1-tricSoro.ttai.
  3'3'4  E.n-vironmental Releases from the Direct  Chlorination



  (46 k£nSLtedV4^(3A kkg) °f ^ t0tal ^Ll-trichloan
  dJL^  J      f    ^he environment during its production by the
  direct Chlorination  of ethane was discharged to water, 21% (10 kk

                                                               k
                                                                  was
 nr A ^-     5hej1'1»1-trichloroethane  discharged to water during its
 production via direct Chlorination was contained in effluents ?fom

 stf«!!T ^ V6nt fndensers used to ^trol emissions from recycle
 storage vents, product storage vents and handling (EPA 1979b)   Liauid
 wastes from these sources were sent to POTWs (EPA 1979b)


      Approximately 10 kkg of 1,1,1-trichloroethane were emitted to the

 atmosphere during its production  via the direct chlorinaSHf Ithane

 (Table 3-2  see Table B-2,  Appendix B).  All of this waste came from the

 recycle storage vent, product  storage vent and  handling (EPA 1979b)


      Only  2 kkg of 1,1,1-trichloroethane were land-disposed.   This waste
 was  captured by the glycol  pot control devices  used on  the 1,1,1-trichloro-

 ethane column vents;  see  Figure B-2, Appendix B for vent location!I  (SJ 1979b)


 3'4   INADVERTENT  SOURCES  OF 1,1.1-TRlCHLOROETHANE


     Certain industrial processes not  directly  related to  '

 ethane production generate  1,1.1-trlchloroethane-containlng ,

 ""kkg"?  ^ releaS6d C°  the environment ^  small quantities  U.e.,



 3-4'1  Vinyl Chloride Manufacture



     Virtually  all vinyl capacity  in the United  States  fc95Z) is based

upon the "balanced process," which incorporates  direct  and oxy-chJorination
                                 3-7

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FUGITIVE
EMISSIONS
STORAGE
A VENT
' I
1 I
1 1
I 1



ETHANE
CHLORINE
AMMONIA ^
FeCl3 CATALYST "^

OJ



CHLORHIATION
AND

COLUMN
VENTS
A
[ STORAGE VENT
i A
1 1





SEPARATION
°° WASTES USED AS i / HANDLING
FEEDSTOCK V
ELSEWHERE . SPENT t /
^- " CATALYST Y
"••"-.
(1,1,2-TRICIILOROETHANE) 1
I
1
1
1
1,1,1-TRICHLOROETHANE PRODUCT
k *"TD
A " STORAGE
1 STABILIZER

i

MISCELLANEOUS
WASTEWATER
/ SOURCES
(AND 1.2-DICIILOROETHANE) '^
COLUMN
WASTES
                                                                                                       n>
                                                                                                          HANDLING
                                                                                                       I

                                                                                                       l'   TRANSPORTATION
                                                                                                          OUT OF PLANT
Figure 3.3  Waste Releases from 1,1,1-Trichloroethane Production Via Direct Chlorination of Ethane
a) | =  Air emissions;^ = water discharge-, and I »  land disposal.

Source:  EPA,  1979a,b.

-------
TABLE 3-2  ENVIRONMENTAL RELEASES OF 1,1,1-TRICHLOROETHANE DURING
           PRODUCTION BY THE ETHANE PROCESS, 1979 (kkg)
Producer       Quantity Produced     Estimated Environmental Releases
                    3     a
(location)       (10  kkg)             Air   Land    Water    Total
Vulcan              25                 10     2       34        46
(Geismar, LA)
a)  Philips (1980).

b)  Controlled releases, see Appendix A and Table B-2 in Appendix B for
    calculations and emission factors.  Wastes emitted to air stem from
    storage and handling operations and fugitive emissions; land releases
    result from control device wastes; water discharges are a result of
    handling and storage operations.
Source:  EPA (1979b).
                                  3-9

-------
 of ethene (Catalytic 1979).   A typical flow diagram, of the "balanced
 process" for vinyl chloride manufacture is shown in Figure B-3 in
 Appendix B.   Wastes containing 1,1,1-trichloroethane are generated by
 the three distinct aspects of the process: direct chlorination of ethene
 oxy-chlorination of ethene and dehydrochlorination of 1,2-dichloroethane'
 and are typically combined at any given facility for recovery, treat-
 ment and disposal.  Therefore, the specific point sources of aqueous and
 solid wastes at a manufacturing site are a function of the actual engineer-
 ing design and by-product production.   Wastewater streams from the
 direct chlorination and oxy-chlorination of ethene may include:  wash-
 water from vent gas scrubbers; dichloroethane  washwater;  drying  column
 wastewater;  the aqueous stream from the oxy-chlorination  quench  area
 and the aqueous stream from  the light-ends distillate decanter.   However,
 1,1,1-trichloroethane has not been detected in wastewater from these
 sources (EPA 1975a).

      Vent gases from  the direct-chlorination and  oxy-chlorination pro-
 cesses contain nitrogen,  small amounts  of  hydrogen chloride,  chlorine,
 unreacted ethene,  vinyl chloride,  methane,  ethane and carbon  monoxide',
 but do not contain 1,1,1-trichloroethane [see  Note 7,  Appendix A
 (EPA 1975a,  McPherson et al.  1979)].

      The  two sources  of solid  wastes from vinyl chloride monomer  pro-
 duction,  heavy ends from the  1,2-dichloroethane purification  column  and
 reactor tars (see  Figure  B-3,  Appendix  B for waste  source locations)
 both contain inadvertently-produced 1,1,1-trichloroethane.  Based  on
 1978 quantities  of vinyl  chloride  produced, approximately 20  to 1,140 kkg
 of  1,1,1-trichloroethane were  contained  in heavy ends wastes generated
 by  the  "balanced process"  (see Appendix A, Note 8  for calculations).
 However,  it  is  likely  that <1 kkg  of the compound  is released  to the
 environment  because the heavy  ends are either treated to recover organic
 compounds  for  in-house use or  incinerated with a 99,9% destruction
 efficiency (McPherson et al.  1979).

     Similarly, the tars generated by the  "balanced process"  contained
 approximately 24 kkg of 1,1,1-trichloroethane (see Appendix A, note 9
 for  calculations).  These nonrecoverable tars are either incinerated with
 99.9% destruction efficiency or disposed as solid waste to a landfill
 (EPA 1975a, Lunde 1965).

 3.4.2  Chlorination of Water

     Chlorination of municipal water supplies apparently is not an
 inadvertent source of 1,1,1-trichloroethane, as post-chlorination
effluent levels of the compound are not consistently higher than  those
prior to chlorination.  In fact, slightly lower concentrations were
found in treated effluent waters than untreated effluent waters (EPA
1977a, EPA 1977b, Sievers et_ al. 1977).
                                   3-10

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  3.5  USES OF 1.1,1-TRICHLOROETHANE

      Use of 1,1,1-trichloroethane, one of  the least toxic chlorinated
  hydrocarbons, had been expected to increase  (almost 10%) in the past
  ten years and replace the more hazardous trichloroethylene .   However  111-
  trichloroethane has captured only an estimated 25% of the vapor degreasing'
 market  (Mannsville Chemical Products 1979).  Table 3-3 lists consumption
 quantities and estimated environmental releases of 1,1,1-trichloroethane
 from its use in degreasing, aerosol formulation, adhesives manufacture,
 and other smaller volume uses.  Use quantities are based on the 1978 use
 distribution pattern and industry trends (EPA 1979a, Mannsville Chemical
 Products 1979).

 3.5.1  Degreasing Operations

      Degreasing is the removal of oils, fats, grease and wax from metals,
 glass,  plastics,  and textiles by an organic solvent.   The 1,1,1-isomer
 is particularly suitable for degreasing due to its nonflammability,
 relatively low toxicity and medium solvency.  The basic types  of  degreasing
 operations and estimated environmental releases of 1,1,1-trichloroethane
 from such operations are presented in Table 3-4.

      Of the total  220,130 kkg of 1,1,1-trichloroethane (virgin  solvent
 see Appendix C)  used in  degreasing,  53,010  kkg  were utilized in cold
 cleaning,  106,280  kkg  in open top  vapor degreasing,  57,600 in conveyorized
 degreasing and  3,260 kkg in fabric scouring.  Table B-4,  Appendix  B,
 lists various  industries  that  employ  some form  of  these operations.

 3.5.2   Cold  Cleaning

     Two types of  cold cleaning are performed: maintenance degreasing
 used primarily in  automotive and general plant cleaning,  and manufacturing
 cleaning, usually  associated with metal working.  About 137,400 facilities
 employ  1,1,1-trichloroethane in cold cleaning operations  (EPA 1979c)   The
 geographic distribution of cold cleaning operations is shown in Figure 3-4
 In both  maintenance and manufacturing cold  cleaning, the parts to be
 cleaned  are sprayed, soaked or brushed with solvent.  Depending upon the
 specific operation, the parts are loaded and unloaded manually or mechanically
 (conveyorized) into the degreaser  (see Table 3-4).  Environmental releases
ot 1,1,1-tnchloroethane from cold cleaning are delineated in Table 3-4
By far,  most of the 1,1,1-trichloroethane lost to the environment from
cold cleaning is emitted to the atmosphere;  in 1979, emissions  totaled
26,440 kkg.  Approximately 12,270 kkg were released to land,  and 5 260
kkg were sent to POTWs.  An estimated 15,770 kkg of the total 1,1,1-
trichloroethane were waste solvent load recycled (EPA 1979c).
                                  3-11

-------
             Table 3.3  Use of 1,1,1-Trich loroethane and Estimated Environmental Releases,  1979  (kkg)
Eat i rated Environmental Releases
e
greas ing (total )
-old cleaning (total)
Manufacturing
Maintenance
Open-top vapor degreasing
Conveyor i zed vapor degreasing
^onveyorized nonboiling degreastng
rabric scouring
•osol formulation
lesvies and coatings'"
ler
'aintsd
i Im cleaner
eather tanning
iscellaneous solvent use^
ortsh
ckpi led1
Tota 1
Quantity Consumed
220,130
53,010
23,310
29,700
106,280
45,530
12,070
3,260
22,530
22,530
23,170
5,790
320
390
16,670
27,030
6,440
321,830
Air
174,780
26,440
11,630
14,810
95,540
44,890
6,020
1,896
22,300
22,527

5,670
320
386
16,670


242,653
Land
27,860
12,270
4,730
7,540
51,710
2,770
2,450
660
230
neg

120


neg '


28,210
;
j ^
Wac»r . iOtal
11,940 214,580
5,260 43,970
2,030 13,390
3,230 25,580
4,160 i09,4!0
1,190 48,850
1,050 9,520
280 2,830
neg 22,530
3 22, 530

5,790
neg 320
4 390
neg 16,670


11,947 282,810
3ased on EPA emission factors and solvent waste and recovery factors.  Quantity consumed for degreasing  includ
only virgin solvent, environmental  releases include those from recycled solvent.  See Table 3.2 and Appendix C

3ased on 99? of solvent evaporating from product dispersion; the remaining 1 % is left in container and sent to
landfills (Anthony,  7980; Simmons,  1980).  Negligible is defined as 
-------
                                               Table 3.3 (concluded)
e                                       3" «-c««»nd.t.on Package for the Adheres and Sealants  Industry,

!'50n      '"^r1*  UnTrMted  diSCharge  °f  '.M-trichloroethane is projected to b. 2,920 kg  per  year.   0,
  500 kno-n adhes.ves and sealant  faculti
                                                                                               ,                .

                      .ves and sealant  faculties,  only  seven  are direct dischargers.  Therefore, the quantty of


                                                  •
  r a   I!;   TTtT? ^^.^^ ^^^  •-  -8"8,b,..   U..  «** 33?o  the indirect disch r ers  rov  e
 .reatment.  The total quantity discharged  is 3 kkg  per  year.   See Appendix A,  Note 10.


                                                evaporatin9
Based on  99?  lost  to  atmosphere,  see text dollar, I960, EPA, 1979a).
                                    f° r«Ult •^"••'y '» atTOSPher!c emissions, see text.  Miscellaneous  use<

                          traction  solvent and ,ubrlc.nt  in cutting oils or .eta. dri.Hng and taoping.


Harris, 1980.




Based on difference  In production  and  sales  in  1978,  extrapolated to 1979, USITC,  1979.




W*t«r discharges includ* both discharges  co ?OT
-------
             Table 3.4  Estimated Environmental Releases of 1,I,1-Trlchloroethane from Oogreasing Operations,  1979  (kkg)
Estimated Environmental Releases
Total Virgin
Doyroaslng Quantity Solvent % Solvent Wasted (average)
Operation Consumed Used3 and Total Waste Solvent Load^
Cold cleaning:
Manufacturing 27,040 23,310 40-60(50) 13,520
Maintenance 34,450 29,700 50-75(62.5) 21,530
Open-top vapor 123,280 106,280 20-25(22.5) 27,740
degroas Ing
*f* Conveyorlzed 52,810 45,530 10-20(15) 7,920
£ vapor degrees Ing
Conveyor! zed 14,000 12,070 40-60(50) 7,000
nonhol 1 Ing
decreasing
Fabric scouring 3,780 3,260 40-60(50) 1,890
g
Total 255,360 220,130 79,600
Quantity Alrd
Recycled

6,080 11,630
(8,140-15,120)
9,690 14,810
(10,370-19,250)
12,480 95,540
(66.880-124,200)
3,560 44,890
2,030 6,020
(4,210-7,830)
850 1,890
(1,320-2,460)
34,690 174,700
Watere
Land Surface POTW Total

4,730 2,030 18,390
7,540 3,230 25,580
9,710 4,160 109,410
2,770 1,|90 48,850
2,450 1,050 9,520
660 280 2,830
27,860 11,940 214,580
a)  Based on 1otal production of 321.830 kkg of 1,1,1-trlchloroothane (Harris, 1980) and a percentage use distribution  pattern
    similar to that of 1978 (EPA, I979b).  Virgin solvenr Is that which Is entering tho system for the  first  time; total
    quantity consumed  Is virgin solvent plus that which Is recycled from previous year (see Appendix C  for derivation).

b)  El'A. 1979c.  Waste solvent  Is that which contains Impurities from degreased parts and Is distinct from vapor emissions  (due
    1o evaporation from the dagreaser) or from carry-out of  solvent from degreased parts.

c)  Uased on 45* of the total  waste solvent load Iwlng reclaimed by distillation and recycled (EPA, 1977d).

-------
                                                              Table  3.4  (concluded)


        d)  Cased on  emission  of  430 g solventAg  solvent consumed for maintenance and manufacturing cold cleaners, 775 g so.ventAg
           so vent consumed  for  open-top  degreasers, 850 g solventAg solvent  consumed for conveyorHed vapor deceasing, 430 g
           so.ventAg solvent  consumed for  conveyor.zed nonboll.ng  degreasers.  and 500 g solvent Ag solvent consumed for fabric
           scourers.  The  range  shown represents  the ± 30* uncertainty  of  the  emission factor (EPA, 1979c).
H-
           or          ms,                                                                                    ™* —   ac
           or  In  landfills) and  I5J! to water  (dumped  In drains resulting  In  discharge  to POTWs).   Of  the remaining solvent  45* Is
           recycled  (often d.st.Hat.on) and  5% Is  Inc.nerated. generating  .nslgn.f leant atnospher.c  emissions.

       f)  Totals may not add due to rounding.

-------
 3.5.3  Open-top Vapor Degreasing

      In open-top vapor degreasing,  a vapor zone is created by heating
 the solvent; parts to be cleaned are immersed, the solvent vapor con-
 denses and impurities are washed away.   A solvent spray is sometimes
 employed to assist in removing heavy soil (EPA 1979c).   Open-top vapor
 degreasers are utilized in metal working plants for manufacturing cleaning
 and are also suited for degreasing  of intricate electrical parts where a
 high degree of cleanliness is required  (EPA 1977d).  Geographic distribu-
 tion of open-top (and conveyorized)  vapor degreasers is shown in Figure 3-5
 Approximately 4,000 establishments  utilize 1,1,1-trichloroethane in
 open-top vapor degreasing (EPA 1979c).

      Although the body of the open  top  vapor degreaser  is  extended to
 minimize the escape  of solvent vapors,  87% (95,540  kkg) of the total
 l»l»l-trichloroethane lost to the environment from such operations is
 in  the form of atmospheric emissions from solvent  diffusion and convection
 and carry-out on cleaned parts (Table 3-4).   As  noted in Table  3-4,
 9,710 kkg of 1,1,1-trichloroethane  are  disposed  to land from waste
 solvent disposal,  4,160 kkg are discharged to POTWs  and 12,480  kkg of
 the total waste  solvent load  are recycled.

 3.5.4  Conveyorized Vapor Degreasing

      Conveyorized  vapor degreasing employs  the same  process  technique
 as  open-top  vapor  degreasing  except  that work  to be  cleaned  is mechanically
 transported  to and from the degreaser.  About  600  facilities  employ
 l,l»l-trichloroethane  in  conveyorized vapor degreasing  (EPA  1979c);
 the geographic distribution of  conveyorized  (and open-top) vapor degreasers
 is  shown  in  Figure 3-5.

      Carry-out of  vapor and liquid solvent is usually the largest  source
 of  solvent loss  from  conveyorized vapor degreasers since the units are
 normally  enclosed  except  for  small areas for entry and exit of material
 to  be  cleaned.  Total  atmospheric loss of 1,1,1-trichloroethane from
 conveyorized vapor  degreasers, as shown in Table 3-4, is 44,890 kkg;
 approximately 2,770 kkg were released to land and 1,190 to POTWs.
 Approximately 3,560 kkg of the total 1,1,1-trichloroethane waste solvent
 load was  recycled.

 3.5.5  Fabric Scouring

     A relatively small amount of 1,1,1-trichloroethane, 3,260 kkg,
was consumed in fabric scouring, which is essentially conveyorized cold
 cleaning  (see Table 3-4).  The geographic distribution  of fabric scouring
 facilities is shown in Figure 3-6.

     Fabrics are scoured prior to dying  and finishing to remove waxes
 and sizings accumulated during production.  Material is  fed into the
 degreaser where it is sprayed with solvent; multilayer  treatment (several
                                  3-16

-------
                                           ! 0 to 5 000
                                       |i':i!illj| 5.000 tc 25.000
                                           j 25.000 to 50 000
                                            > 50 000
 FIGURE 3-4   GEOGRAPHIC  DISTRIBUTION OF COLD  CLEANING OPERATIONS
 Source:  EPA (1979c)
                                     NUMBES Of OPERATIONS
                                           0 to 100
                                           100 to 500
                                           500 to 1,000
                                           > 1.000
FIGURE 3-5  GEOGRAPHIC DISTRIBUTION OF VAPOR DECREASING OPERATIONS'
a) Includes open-top and conveyorized  degreasers
Source:   EPA (1979c)
                                3-17

-------
                                         0 te 50
                                         50 to 500
                                       i  50C to 1,000
                                         >  1.000
FIGURE 3-6   GEOGRAPHIC DISTRIBUTION OF FABRIC SCOURING OPERATIONS
Source:  EPA (1979c)
                               3-18

-------
layers of fabric are fed through the degreaser at once) is sometimes
performed to increase throughput (EPA 1979c).   Table 3-4 gives environ-
mental losses of 1,1,1-trichloroethane from fabric scouring operations;
1,890 kkg of the total 1,1,1-trichloroethane loss occurs as atmospheric
emissions.  Appoximately 660 kkg of 1,1,1-trichloroethane were land-
disposed, while 280 kkg were sent to POTWs (Table 3-4).

3.5.6  Aerosol Formulation

     The quantity of 1,1,1-trichloroethane used as a solvent and vapor
depressant in aerosols is not directly reported; based on SRI (1978)
estimates of 18,000 kkg of 1,1,1-trichloroethane used and an expected
increase in use due to the ban on chlorofluorocarbon use in aerosols,
approximately 22,530 kkg of 1,1,1-trichloroethane were utilized in
aerosol formulation in 1979  (Anonymous 1977;   SRI 1978,
EPA 1979a).  The compound 1,1,1-trichloroethane is a strong candidate
for replacing chlorofluorocarbons due to its flammability-suppressing
nature as well as its solvency (for hair spray resins), availability,
and relatively low toxicity (Anthony 1979).  The compound is found in
insecticide sprays, automotive cleaning products, household cleaners,
and personal care items  (Gordon and Hillman 1979, Hile 1977).

     Losses of 1,1,1-trichloroethane from manufacturing of aerosol
products occur during filling of the containers; such losses are
atmospheric and total no more than 1% of the total amount of solvent
consumed.  Thus, approximately 230 kkg of 1,1,1-trichloroethane are
emitted to the atmosphere from manufacture of aerosol products
(Anthony 1980, Simmons 1980)

     Approximately 22,070 kkg of 1,1,1-trichloroethane are emitted to
the atmosphere from use of aerosol products, since the solvent evaporates
as it is dispensed from  the container.  Only 1% (230 kkg) of the total
1,1,1-trichloroethane present remains in the "empty" container (Simmons
1980, Anthony 1980) and  is assumed to be landfilled  (Table 3-4).

3.5.7  Adhesives and Coatings

     The adhesives and sealant industry, consisting of about 1,500
establishments, utilized 22,530 kkg of 1,1,1-trichloroethane in 1979
in the production of water- and solvent-based adhesives, especially
contact cements (EPA 1979a, EPA 1979e, Miron 1980).  Geographic
distribution of the adhesive facilities is shown in Figure 3-7.

     Batch blending of adhesives occurs in enclosed vessels; emissions
of 1,1,1-trichloroethane are estimated to be 1% of the  total solvent
present, or 230 kkg  (Miron 1980).  The remaining emissions, 22,297
metric tons, are lost during preparation of adhesive material by
spraying and 1,1,1-trichloroethane evaporation from product use (see
Appendix A, Note 10).
                                   3-19

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FIGURE 3-7  GEOGRAPHIC DISTRIBUTION OF THE ADHESIVES INDUSTRIES

    Size of symbol ( X) proportional to number of facilities.
    -.e:  EPA (1979a)

-------
      Aqueous discharges of 1,1,1-trichloroethane are minimal; only
 8 kg of this solvent are discharged industrywide  per day (EPA 1979e).
 A maximum of 3 kkg of 1,1,1-trichloroethane would be discharged
 industrywide,  assuming a 365 day per year operation (see Table 3-4).
 Of the 1,500 adhesive and sealant facilities, only seven discharge
 directly to surface waters;  loss of 1,1,1-trichloroethane to surface
 waters appears to be negligible (EPA 1979e).

      Use of 1,1,1-trichloroethane in the adhesives industry is being
 phased out, perhaps due to regulations such as Los Angeles'  Rule 66.
 The solvent is,  however,  still an important component of water-based
 contact cements.

 3.5.8  Small Volume Uses  of  1.1.1-Trichloroethane

      The 1,1,1-isomer is  used,  to a small extent,  in paints,  as a film
 cleaner, in leather tanning  and other miscellaneous solvent  applications
 (see Table 3-4).   Such uses  result primarily in atmospheric  emissions,
 with less significant quantities being discharged  to water.   Table B-5,
 Appendix B lists  detection frequency of 1,1,1-trichloroethane in various
 industrial wastewaters.

 3.5.9  Paints

      In 1979,  approximately  5,790 kkg  of 1,1,1-trichloroethane  were
 utilized as a solvent in  traffic paint formulation  (EPA  1979a).
 Application of such paints is performed by  spray equipment with no
 emission control  devices,  therefore an estimated 98% (or 5,670  kkg)  of
 the  solvent evaporates  during product  dispersion.   The remaining  2%  is
 left  in paint  containers  or  contained  in machinery  cleaning residues
 (120  kkg);  both of  these  are disposed  to land.

 3.5.10   Film Cleaning

      An estimated 320 kkg  of 1,1,1-trichloroethane were  used  in 1979
 as motion  picture film cleaner;  this solvent  is especially suitable
 for this use due  to  its nonflammability.  Since such cleaning is a
manual  operation, all of the solvent so  used  evaporates,  resulting in
 320 kkg  of  1,1,1-trichloroethane being  emitted to the atmosphere.

 3.5.11  Leather Tanning

      In 1979, approximately 390 kkg of 1,1,1-trichloroethane were used
in the  tanning industry to waterproof leather.  The solvent-containing
waterproofing solution is applied with a flow coater, which provides
a "falling curtain" of solution over the hide as it is moved by a
conveyor belt  (Lollar 1980).   Such systems are usually equipped with
a canopy exhaust system, venting fumes to the atmosphere.  An estimated
99% of the total solvent present (386 kkg) is emitted to the atmosphere
as the solvent evaporates from the "falling curtain" of water proofing
                                 3-21

-------
 solution (Lcllar 1980).   The  remaining  4  kkg  are  seint  to  POTWs.   This
 estimate seems  high since 1,1,1-trichloroethane was  detected in  waste-
 waters  of only  3 out of  7 leather  finishing establishments  in quantities
 of £10  ug/1  (Lollar 1980, EPA L980b).

 3.5.12   Miscellaneous Small-volume Uses_

     Miscellaneous  uses  of 1,1,1-trichloroethane  in  pharmaceutical
 extraction solvents,  metal cutting, drilling  and  tapping  oils, and  other
 non-specified solvent applications consumed an estimated  16,670  kkg in
 1979.   Its use  as a drain and septic tank cleaner appears to have been
 discontinued.

     Although the FDA banned  the use of 1,1,1-trichloroethane in drug
 products in  1973  (Mannsville Chemical Products 1979),  the compound  has
 been detected in wastewaters from  this  industry in small  amounts.
 Based on EPA data (see Appendix A, Note 11) <1 kkg of  1,1,1-trichloro-
 ethane  is sent  to POTWs  annually (EPA 1980c).  These aqueous  discharges
 could stem from the use  of  1,1,1-trichloroethane  as an extraction
 solvent  or from its application in equipment  cleaning.

     Use of  1,1,1-trichloroethane  in lubricating  oils  for metal  cutting
 and the  unspecified solvent uses are assumed  to result in atmospheric
 emissions.   Approximately 16,670 kkg of 1,1,1-trichloroethane would
 be emitted to the atmosphere from miscellaneous solvent use.

     In  the  past, 1,1,1-trichloroethane has been  used as a component
 of drain and septic  tank  cleaners.  Several industrial spokespersons
 reported that,  to their knowledge, such use has been discontinued
 (Elliot   1980,  Ashland Chemical 1980).   The Consumer Product Safety
 Commission did  not  list 1,1,1-trichloroethane as  a componenet of drain
 or septic  tank  cleaners as of December 1979 (Consumer Product Safety
 Commission 1980).   Cleaning compounds containing  1,1,1-trichloroethane
 have, for  the most  part, been removed from the market (Anonymous
 1979), since they have extensively contaminated groundwater in areas
 of Nassau  County, New York.

 3.6  MUNICIPAL DISPOSAL OF 1.1., 1-TRICHLOROETHANE

     Loading of 1,1,1-trichloroethane to POTWs is largely dependent
 upon variations in  industrial discharges and the type of industry in a
 particular municipality.  A framework for calculating the total 1,1,1-
 trichloroethane flow through the nation's POTWs is provided by data
 from a recent EPA study (EPA 1980c).   A materials balance of 1,1,1-
 trichloroethane at the treatment plants can be constructed using a
 total nationwide POTW flow of  approximately 1011 I/day (EPA 1978b)  and
median values of 66 pg 1,1,1-trichloroethane/l (influent)  and 10.4 yg/1
 (effluent) (EPA 1980c).  It is assumed  for purposes  of these calculations
 that influent and effluent flow rates are equal,  i.e.,  water loss from
sludge removal and evaporation are small compared to influent flows
                                  3-22

-------
  (see Note 12, Appendix A).  Using these data, approximately 2,410 kkg
  ?f« ,7* 7trl2,loroethane are C0ntained in POTW influent nationwide and
  380 kkg in effluent.


       Approximately 4  kkg of 1,1,1-trichloroethane were contained in
  land-destined POTW sludge, based on a raw sludge concentration of

  ?rof yfwf  ^ 1!8°C):;  and 6 X 10  kkg dry Sludge Derated per year
  (EPA 1979f,  see Appendix A,  Note 12).
  POTU The TUnt  !f  1«1«1-'rlchloroethan€  emitted  to  the  atmosphere  from
  POTWs can be  estimated  by  the  difference  in  influent,  effluent  and  raw
  sludge waste  loadings.  Thus,  2026 kkg of 1,1,1-trichloroethane are
  emitted  to  the atmosphere  from POTWs per  year  (Note  12,  Appendix A)
  This  estimate seems reasonable due to the volatility of  the compound
  and aeration  practices  and the high temperature associated with waste-
  water  treatment.


       Some of  the 1,1,1-trichloroethane entering POTWs was possibly
  biodegraded,  but no specific data were found.

  3'7  PRODUCTION AND USE OF 1,1, 2 -TRICHLOROETHANE

      The compound 1,1,2-trichloroethane is a colorless, nonflammable
 liquid produced in the U.S. directly or indirectly from ethylene;  it
 T^M J C°pr?duCt ln,the ^nufacture of other chlorinated hydrocarbons.
 Its chief use is as a feedstock intermediate in the production of
 1,1-dichloroethylene.   Occasionally it is used  as a solvent for
 chlorinated  rubber manufacture (Archer 1979) .

      According to the  U.S.  International  Trade  Commission,  Dow Chemical
 «  v  JcJ     domestic Producer of  1,1,2-trichloroethane  (USITC  1979).
 (?arber Ssnf T 'H*"*  ^ 5Uantit? Produced as proprietary information
 reaction  1% V    !  ^ Yroduction of  "2,450 kkg  of 1,1-dichloroethylene,
 1S7 inn V   ? n10^eory'  3nd an  estimated  90%  yield (EPA 1978),  approximately
 187,100 kkg  of 1,1,2-trichloroethane would be required  to yield  the
 A^^?y  !?  i'J-fi^oroethylene  currently being produced (see Note  13,
 Appendix  A)    This estimate represents the maximum production  potential

 from !iS!r*?  ? 91§    ?C?T  D°W  Chemical  P^duces  1,1-dichloroethylene
 f^Tf   J  I   J§ §  ,°v  J^'^ttichloroethane,  depending upon economics
 and feedstock  availability  (EPA 1978).

     Environmental releases of  1,1,2-trichloroethane  from 1,1-dichloro-
ethylene manufacture are small; an EPA study found no 1,1,2-trichloro-

        ? PI°CeSS Vent 8aS  (EPA 1979b)"  Volatile organic compounds
v.vw t^sions ar cne Dow facility are controlled by incineration and
refrigerated condensers with removal efficiencies of 98 and 937
respectively (see Table 3-5); Hedley et a±_ (1975) report no l,°i,2-
trichloroethane in the 1,1-dichloroethylInT separation column wastewater.
                                 3-23

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    Table 3.5  Production, Use, and Estimated Environmental Dispersion of 1,1,2-Trichloroethane  in  1979  (kkg)



                                                                                          Estimated Environmental

                                                                                          	Releases	

           Production                                                Use                   Air     Land    Water
Chlorination of 1,2-dichloroetharie                     Production of 1,1-dichloroethylene  neqb            ,,nac
          187,100a                                               187.100                                     9

1,2-dichloroethane purification                                                            60d

1,1,1-trichloroethane production, vinyl chloride process                                   nege    negc    riege
         750

1,1,1-trichloroethane production, ethane process                                           riege    riege    nege
         1,640'
                                                       Miscellaneous                       4,000    900     100
                                                                   5,000
a)  IJased on 1,1-dichloroethylerie production of 122450 kkg (EPA, 1978), 90% yield (EPA, 1978) and reaction
    stoichiometry.

b)  Not detected in vent gas from reactors or distillation columns (EPA, 1979b).

c)  Not detected in waste water streams (nediey, et al., 1975).

d)  Based on 2 kg 1,1,2-trichloroethane discharged/kkg EDC produced by direct chlorination (Medley,  et al
    1975).   EDC production by direct chlorination 3.08 x 10^ kkg,  and 1% of waste escaping incineratTonT '

e)  All of  that which is produced (as a by-product) is recycled  within the plant (EPA, 1979b).

f)  See text.

g)  Order of magnitude estimate of  deposition  of "low  millions of pounds" which  Dow markets to other industries,
    jCC LCAL•

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       The dispersion of 1,1,2-trichloroethane to the environment also
  results from the manufacture of other chlorinated hydrocarbons (see
  Table 3-5).  From manufacture of 1,2-dichloroethane by direct and oxy-
  chlorination respectively, 0.039% and 0.453% (by weight) of the process
  effluent is 1,1,2-trichloroethane.  During purification of 1,2-dichloro-
  ethane, 2 kg of 1 1,2-trichloroethane produced by'direct chlorination
  (Hedley et al^ 1975).   Based on 1978 production of 3.08 x 10* kke
  (USITC 1979) of 1,2-dichloroethane by direct chlorination and thf above
  discharge factor, about 6,000 kkg of 1,1,2-trichloroethane would be
  contained in solid wastes (see Note 14,  Appendix A).   These wastes are
  recycled as feed materials for other processes (generating no waste)
  or incinerated  at approximately 99% efficiency.  If 1% of the total
  solid waste generated  escapes incineration,  approximately 60 kkg  of
  I,1,2-trichloroethane  would be emitted to the atmosphere (see Table 3-5)

       During manufacture of 1,1,1-trichloroethane  by the  vinyl chloride
  process,  2.6 kg  of  1,1,2-trichloroethane would  be emitted to the
  atmosphere  (see  Table  3-5).
 process
     During manufacture  of  1,1,1-trichloroethane  by  the vinyl  chloride
 .  _-_;ss,  2.6 kg of 1,1,2-trichloroethane are  produced  per kke  111-
 trichloroethane (Elkin 1969).  Based on a production of 289, 700 'kkg of
 7sn'iC    f J°f°f     by the Vinyl chloride Process  (USTIC 1980), about
 750 kkg of 1,1,2-trichloroethane would be produced; usually, these heavy
 n^/fFPr^o^   * materials for other chlorocarbons within the sam7
 plant (EPA 1979D).  Approximately 51 kkg of 1,1,2-trichloroethane are
 produced  per kkg of 1,1,1-trichloroethane manufactured by the chlorina-
 tion of ethane; again all of  that which is produced  is recycled
within the plant (EPA 1980).                           recycled

      Dow Chemical does sell some 1,1,2-trichloroethane as a consumer
product (Dow Chemical 1980)  but the quantity sold is considered pro-
prietary information.   A spokesperson from Dow estimated  that  "low
                                                               ™ "


                                      waastbeen detected
B-6, Appendix B (Epsb)   Ou  of   981 ^f* "
found only 58 times at concentrations g eat r tha'n'lO
concentration was 12 ug/i, the maximum 3,400 ug/1
                                  3-25

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      Very small  quantities  of  1,1,2-trichloroethane have been  found in
 POTWs Across  the country  (EPA   1980c).   Based  on  a nationwide  POTW flow
 of  10   I/day (EPA  1978b) and  influent  and effluent concentrations of
 1.9 and  0 ug/1,  respectively,  approximately  69 kkg of  1,1,2-trichloro-
 ethane is contained in  POTW influent and zero  in  the effluent.  The
 quantity of 1,1,2-trichloroethane contained  in POTW sludge  can be
 determined using a  raw  sludge  concentration  of 10.9 ug of 1,1,2-trichloro-
 ethane^l (EPA 1980c) and  the quantity of dry sludge generated  per  year,
 6 x 10  kkg.   Based on  these data, and  assuming that wet sludge is 95%
 water by weight,  approximately 1 kkg of 1,1,2-trichloroethane  is con-
 tained in POTW sludge each  year.  As ocean dumping of sludge is man-
 dated to cease by 1981, and increasing  stringent  air quality standards
 will  probably curb  sludge incineration, the  1  kkg of 1,1,2-trichloroethane
 is  assumed to be land-disposed.  The amount  of 1,1,2-trichloroethane
 emitted  to the atmosphere from POTWs can be  estimated by differences
 among  the quantities to the compound to influent, effluent  and sludge.
 Thus,  approximately  68 kkg  of  1,1,2-trichloroethane were emitted to the
 atmosphere from  POTW.  This seems reasonable in light of the compound's
 volatility, and  the  high temperatures and aeration techniques required
 for water treatment.  Biodegradation of the compound is a possible
 explanation for  the difference  in influent, effluent and sludge concen-
 trations;  however, no specific data were found.

     Chlorination of municipal water supplies is known to produce
 chlorinated hydrocarbons (Sievers et al. 1977); however,  it appears
 that such  inadvertent production of 1,1,2-trichloroethane does  not
 occur.  1,1,2-Trichloroethane was detected (but not quantified) in the
 drinking water supply in Miami, Florida (EPA 1975c),   Neither the National
Organics Monitoring Survey,  nor the National Organics  Reconnaissance
 Survey for Halogenated Organics (Symons et al.  1975) addressed  1,1,2-
 trichloroethane in drinking  water supplies.
                                   3-26

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                                REFERENCES

 Anonymous.   Profile -  1,1,1-trichloroethane,  Chemical Marketing Reporter, 1977,

 Anonymous.   New York seeks  to  curb  solvents in  groundwater.  Chem Week
 pp. 24-25; April 4, 1979.

 Anthony, T.  A frank look at aerosols. Chemtech 9(5):  292-3; 1979.

 Anthony, T.  Personal  Communication, Dow Chemical, 1980.

 Archer, W.   Chlorocarbons - hydrocarbons (In) Kir Othmer Encyclopedia
 of Chemical  Technology.  Vol. 5 pp. 732-3.  New York, NY: John Wiley
 and Sons; 1979.

 Ashland Chemical.   Personal Communication, 1980.

 Campbell, A.; Carruthers, R.A.   Production of 1,1,1-trichloroethane
 British Patent 1281541, July 12, 1972.  Assignee:   Imperial Chemical
 Industries,  Ltd.

 Catalytic,  Draft  Summary Report of BAT-308 Responses, 1979.

 Consumer Product  Safety Commission,  Personal  Communication,  1980.

 Crutzen, P.J.;  Isaksen, I.S.A.   Impact of  chlorocarbon industry on
 the ozone layer.  Geophys.  Res. (in press).

 Elkin,  L.M. Chlorinated solvents.  Report No.  48, Menlo Park, CA:
 Stanford Research Institute  (SRI); 1969.

 Elliot,  B.  Personal Communication,  Vulcan  Materials,  1980.

 Environmental Protection Agency.  Disposal  of  organo-chlorine wastes
 by  incineration at sea.   Report  No.  EPA 450/9-75-014;  1975a.

 Environmental Protection Agency.  Engineering  and cost  study of air
 pollution control for the petrochemical industry, vinyl  chloride
manufacture by the balanced process.  Vol.  8 , Report No. EPA 450/3-73-
006-h, 1975b.

Environmental Protection Agency.  Preliminary assessment of suspected
carcinogens in drinking water: Report to Congress.   PB 250961/OTIS.
Springfield, VA; 1975c.

Environmental  Protection Agency.  Chlorinated compounds found in waste-
                                 3-27

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 Environmental  Protection  Agency.  Multimedia  levels  - Methylchloroform.
 Report  No.  EPA-560/6-77-030.   Battelle  Columbus  Laboratories;  1977.

 Environmental  Protection  Agency. National  organics monitoring  survey,
 Washington, DC:   Office of Water Supply; 1977b.

 Environmental  Protection  Agency.  Environmental  monitoring near  industrial
 sites-methylchloroform.   Report No. EPA-560/6-77-025.   Battelle  Columbus
 Laboratories;  1977c.

 Environmental  Protection  Agency.  OAQPS Guidelines,,  Control of  Volatile
 Organic Emissions From Solvent Metal Cleaning.   Report  No. EPA-450/2-
 77-02;  1977.

 Environmental  Protection  Agency.  Air pollution  assessment of vinylidene
 chloride.  Report No. EPA-450/3-78-075. Washington, DC:  EPA; 1978.

 Environmental  Protection  Agency.  Level II materials balance: Methyl-
 chloroform. Draft Report, Contract No. 68-01-5793.  McLean, VA:  JRB
 Associates, Inc.; 1979a.

 Environmental  Protection Agency.  Emissions control options for  the
 synthetic organic chemicals manufacturing industry.  EPA Contract No.
 68-02-2577; July 1979b.

 Environmental  Protection Agency.  Source assessment::  Solvent evaporation-
 degreasing operations.  Report No.  EPA-600/2-79-019f; 1979c.

 Environmental  Protection Agency. Investigations of selected environmental
 pollutants: 1,2-Dichloroethane.  Report No. EPA-560/12-78-006;  1979.

 Environmental Protection Agency.  Paragraph 8 recommendation package
 for the adhesive and sealant industry; 1979e.

 Environmental Protection Agency.  Comprehensive sludge study relevant
 to Section 8002 (g) of the Resource Conservation and. Recovery Act of
 1976.  Report No. EPA-SW-02.   Washington,  D.C. Office of Solid  Waste; 1979f,

 Environmental Protection Agency.  Development document for effluent
 limitations guidelines and standards for the pharmaceutical industry.
Report No. EPA-440/l-80-084a.   Washington,  DC.  Effluent guidelines
 division; 1980a.

Environmental Protection Agency.  Priority pollutant  frequency  listing
 tabulations and descriptive statistics.  Washington,  DC:   Office of
Analytical Programs; 1980b.

Environmental Protection Agency.  Fate of  priority pollutants in
publicly-owned treatment works.   Interim Report No. EPA  440/1-80-301.
Washington, DC;  1980c.
                               3-28

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Farber, H.  Personal Communication, Dow Chemical, 1980.

Gordon, W. ; Hillman, M.  Formulation data for hydrocarbon-propelled
aerosol products under CPSC jurisdiction.  Battelle Columbus Division;
1979.

Grimsrud,  E.P.; Rasmussen, R.A.  Survey and analysis of halocarbons in
the atmosphere by gas chromatography-mass spectrometry.  Atmospheric
Environment.  9: 1014-1017; 1975.

Harris, M.  USITC.  Personal Communication, 1980.

Hedley, W.H.; Mehta, S.M.; Moscowitz, C.M.; Reznik, R.B.; Richardson, G.A.;
Zanders, D.L.  Potential pollutants from petrochemical processes.
Technomic  Publications; 1975.

Hile, J.P.  Trichloroethane: Status as a new drug in aerosolized drug
products intended for inhalation, Federal Register 42  (242); 1977.

Lillian, D.; Singh, H.B.; Appleby, A.; Lobban, L.; Arnts, R.; Gumpert, R.;
Haque, R.; Toomey, J.; Kazazis, J.; Antell, M.; Hansen, D.; Scott. B.
Atmospheric fates of halogenated compounds, Environ. Sci. Technol.
9(12):1042-1048.

Lillian, D.; Singh, D.; Appleby, A.  Gas chromatographic analysis of
ambient halogenated compounds.  J. Air Poll Control Assoc. 26(2):141-142; 1976.

Lollar, R.  Personal Communication, University of Cincinnati, 1980.

Lunde, K.E., Vinyl chloride. Report No. 5 Menlo Park, CA: Stanford
Research Institute; 1965.

Miron, J.  Personal Communication, Skeist Laboratory, Livingston, NJ; 1980.

National Institute for Occupational Safety and Health  (NIOSH).   Chloroethanes:
Review of  toxicity.  Current Intelligence Bulletin 27.  NIOSH 78-181.
Cincinnati, OH;  NIOSH:  1978.

Mannsville Chemical Products, 1979.  1,1,1-Trichloroethane chemical
product synopsis.  Cortland, NY: Mannsville Chemical Products;  1979.

McConnell, J.C.; Schiff, A.I.  Methyl chloroform: Impact on stratospheric
ozone.  Science 199(13); 1978.

McPherson, R.W.; Starks, R.W. Fryar, G.J.   Vinyl chloride monomer ...
what you should know.  Hydrocarbon Processing; March  1979.

Philips, Ed., Plant Manager, Vulcan Materials Company.  Personal
Communication,  August  1980.
                                  3-29

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 Rideout, W.H.; Mitchell, J.D.  Vapor phase chlorination of  1,1-dichloro-
 ethane.  U.S. Patent 4,192,823, March 11, 1980.  Assignee:  PPG  Industries,
 Inc.,  Pittsburgh, PA.

 Russell, J.W.; Shadoff, L.A.  The sampling and determination of halocarbons
 in ambient air using concentration on porous polymer.  J. Chromatog. 134:
 374-384; 1977.

 Sievers, R.E.; Barkely, R.M.; Eiceman, G.A.; Haack, L.P.; Shapiro, R.H.;
 Walton, H.F.  Generation of volatile organic compounds from nonvolatile
 precursors in water by treatment with chlorine or ozone. Water Chlorination:
 Environmental Health Effects, Proc. Conf. 78(2):615-24; 1977.

 Simmons, R.  Personal Communication, Dow Chemical, 1980.

 Singh, H.B.; Salas, L.; Shigeishi, H.; Crawford,  A.  Urban-nonurban
 relationships of halocarbons, SF , NO and other atmospheric trace
 constituents.  Atmospheric Environ:  819-828; 1977.

 Stanford Research Institute (SRI).Chemical economics handbook,  Menlo
 Park, CA:  SRI;  1978.

 Stanford Research Institute (SRI).   Chemical economics handbook.
Menlo Park, CA:   SRI; 1979.

 Symons, J.M.; Bellar, T.A.; Carswell, J.K.;  DeMarco,  J.;  Kropp,  K.L.;
Robeck, G.G.; Seeger, D.R.; Slocum,  C.J.; Smith,  B.L.; Stevens,  A.A.
The national organics reconnaisance survey for halogenated organics.
J. Amer. Water Works Assoc. 67:634-646;  1975.

United States International Trade Commission (USITC).   Synthetic organic
chemicals,  U.S.  production and sales, 1978.   Washington,  DC: USITC;  1979.
                                  3-30

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                     4.0  ENVIRONMENTAL DISTRIBUTION

  4.1   INTRODUCTION

       This  chapter contains  information concerning  environmental  dis-
  tribution  and environmental fate  for  the  trichloroethanes.  The  scient<-
  fic  literature and EPA's  STORET Water Quality  files were  searched  for
  information pertaining to ambient environmental levels of the chemicals
  and  concentrations  in  foods.  The environmental fate of the two  chemicals
  was  assessed.  In both cases, little  information was found for 112-
  trichloroethane.   The  1,1,1- isomer was well characterized with
  respect to both topics.

      Concentrations of  the  chemicals  in natural surface waters are gen-
  erally below 10 wg/1,  although, in a  small number of cases,  higher con-
  centrations have been  detected.  For  both trichloroethanes,  the princi-
  pal fate pathway  is volatilization from surface water followed by slow
 decomposition in the atmosphere.  The 1,1,1- isomer has an atmos-
 pheric lifetime of six to ten years, while 1,1,2-trichloroethane
 apparently decomposes more quickly.

      Section 4.2  presents monitoring data. Sections 4.3 and  4.4 discuss
 aspects of  environmental fate.

 4.2  MONITORING DATA

      Trichloroethanes  are found  in ambient air  and  water.  These  com-
 pounds have also been  detected  in  foods and in  aquatic  biota.
      v      ^  exhibits  concentrations  of  1,1,1- trichloroethane  reported
 in  published  literature  for  the U.S.  The  levels  reported  are  generally
 in  the  low yg/m range or  less<  Background  levels  of  this  isomer
 pervasive  on  a  global scale  are less  than  1  yg/m3 .   (Correia et  al.
 1978, Su and  Goldberg 1979).  Concentrations in foreign countrTe~in
 both  cities and rural_areas, are generally <10 yg/m3.  Average
 atmospheric concentrations of 1,1,2-trichloroethane found in seven
 cities were in  the 40-250 ng/mj range (Singh et al. 1979, 1980).  No other
 data were  found for the 1,1,2-isomer in air.

     Table 4-2  displays concentrations reported in  the literature for
 drinking water  (surface and groundwater supplies), ambient surface
 water and  wastewater.   Most reported data are for  the 1,1,1-  isomer
 Though reported values range up to 16,500 wg/1 near a production site
most levels are in the low yg/1 range.  Indeed, these published values
 are consistent with trichloroethane concentrations in ambient and
effluent waters reported from the STORET data base.

     Ambient and effluent concentrations of 1,1,1- and 1,1,2-trichloro-
o-S3^ af6 usua11? less than or e
-------
TABLK 4-1 a. CONCENTRATIONS OF 1 , 1 ,1-TKICHI.OROETHANE DETECTED IN THE ATMOSPHERE
Sample Date
BACKGROUND

9/16- 19/74
11/24- 30/75
12/02- 12/75
March, 1976
March 10,1976
May, 19/6
November, 1976
' Hay, 1977
UKRAN AREAS
6/27- 28/74
8/78- 12/73
7/08- 10/74
7/11 - 12/74
May, 1976
August, 1978
7/17/74 1228
7/17/74 1203
Location


White Face Mountains, NY
Lower end, San Francisco Bay
Point Keyes, CA
Pullman. UA (rural)
Western Montana
Badger Pass, CA
St. Francis National Forest
Helena, AK
Point Arena, CA

New York City, 45th & Lexington
Uayonne , NJ
Delaware City Del. Rte. 448 &
Rt. 72 Int.
Baltimore, MD Fort Holabird Area
Kiverside, CA Airport, 610 m
Claremont, CA
Wilmington, Oil, 5000 ft. .above
inversion
Wilmington, OH, 1500 ft. , Inversion
layer
Concentration

Max. Min. Mean
0.71 0.17 0.37 pg/rn3
Avg. 423 ng/m3
o 34 ng/m3
Avg. 492 ng/m3
o 58 ng/m3
Mean 515 ng/m3 a 47 ni5/mj
26 samples
530 ng/ro3
Mean 533 ng/m3
Std. Dev. 52 ng/m3
£1.7 ,,g/ra3
Mean 598 ng/m3
Std. Dev. 97.7 ng/m3

Max. M_in. Mean
8.7 0.55 3.3 ng/m3
78.5 0.41 8.7 ,,g/m3
1.6 0.16 0.55 ug/m3
1.14 0.24 0.65 |ig/m3
5.9 pg/ra3
27 ,JR/m3
0.14 t'g/m3
0.35 ug/m3
Comment


Concentration varies with
urban plume passage.
75 samples
100% detection
Avg. 458 ng/m3
100% detection
CH3CC13 0-14.6 km altitude
Concentration decreases with
Intrusion into stratosphere
At tropopause height, 11.4 km
MSL
Troposphere average
12% increase over May 76 -
May 77
Background Site
12% increase over May 76 -
May 77









Rel erence


Ml Man i^t aK (1975)
Singh ^t jjl. (1977)
Cronn e£ a^. (1977)
Croiui & ll,u :it: h (1979)
Si ngli L.£ al . 1978
Bat tell i- (1977)
Singh et al. (1978)

Li 11 Ian et al . (1975)
II
>.
II
Cronn (1980)
II
Lill ian £t a_l. (1975)
••

-------
TABLE 4-la.  CONCENTRATIONS  OF  ],1,1-TRICHLOROETHANE  DETECTED TN  THE ATMOSPHERE (Continued)
— •-•—-- 	 • •- 1 .
Sample Date
1/74- 10/75
1/29/74 0800
4/6/74 1130
4/6/74 1400
4/16/74 0830
1200
1700
4/19/74 0730
3/15/75
Urban Arpfis
5/15-5/25. 1980
5/29-6/9, 1980
6/15-6/28, 1980
7/1-7/J3. 1980
5-6/79
5-6/79
7/79
MAJUNE
October, J978
1974
May 9. 1974
May 9, 1974
May 9, 1974
May 8, 1974
May 24, 1974

~ ' — • — •• » 	 . 	 , , 	
Location
LaJolla, CA
Washington, DC
— 	 	 	 _ 	
Los Angeles, Chinatown, CA
Santa Monica Residential Area.CA
Orange County.CA
Chicago, Downtown Loop, I L
Chicago Airport, IL
Houston, TX
St. Louis MO
Denver, CO
Riverside, CA
Los Angeles, CA
Phoenix, AZ
Oakland, CA
Atlantic Ocean, average
Southern California
Oaborn Bank Basin, CA
Santa Cruz Basis-., CA
San Pedro, CA
Santa Barbara Basin, CA
San Diego Trough, CA


Concent rat Ion
<0.32- 5.9 pg/m3
2.7 pg/mj
1.8 ug/m3
7.0 pg/m3
2.2 Mg/m3
1.5 inj/m3
2.5 pg/m3
1.1 Mg/m3
	 	 	 *~ 	 -' • 	 	 . „.-—— -
1.7 pg/m*
Average Standard Deviation
B/m^
1.9 1.5
1-3 0.7
3.9 3.0
4-1 1.4
5.6 3.6
4.5 3.3
!•<> 0.9
0.4 pR/m3
l.Oi 0.3 pg/m3
0.76 pg/n.3
0.76
1.6
1.3 pg/ni3
0.76 g/,q3

Commen t
Continental U.S.

pg/day (23 in /day)
42 13
1 28 7
9? 11
-
93 18
133 45
116 39
38 I J
Marine Air
Marine Air
Marine Air, off California
Coast



Reference
Su & Goldberg (1976)
it
M
ii
ii
*i
Singh at ill. (1980)
	 ...


1
Su and Coldbcrg (1976)
II
II
1*
II


-------
                                          TABLE 4~la.  CONCENTRATIONS OF 1,1,1-TRICHLOROETHANE DETECTED IN THE ATMOSPHERE (Continued)
Sample Date
NEAR PRODUCERS
November, 1976
December, 1976
November, 197fc
December, 1976
January, 1977
Urban Areas
May, 1980
May- June, 1980
June, 1980
June, 1980
May-June, 1980
May-June. 1980
July, 1980

Location
Dow Plant A; Freeport, TX
Vulcan Materials Co.; Gelamar, LA
Ethyl Corporation; Baton Rouge, LA
PPG Industries; Lake Charles, LA
Hoeing; Auburn, UA
TABLE 4-lb. CONCENTRE
Houston, TX
St. Lout a, MO
Denver, CO
Riverside, CA
Los Angeles, CA
Phoenix, AZ
Oakland. CA

Concentration
<1.7-64 pg/m3
£1.7-860 ug/m3
<1.7- 22 ug/m3
<1.7-47 ug/m3
2.2-5.5 ug/m3
iTIONS OF 1,1,2-TRICHLOROETII
Average Standard Deviation
ng/mj
180 130
80 30
150 60
230 120
50 30
90 60
40 20

Comment
1,1,1-Producer, distance £ 3.2
km,f (direction, distance, time)
1,1,1-Producer, distance <1 km
1 ,1,1-Producer , distance, -:.3kin
1,1,1-Product Site, distance
<4 km
User site, Distance <3 km
ANE DETECTED IN THE ATMOSPHERE
Dally Dose ug/day
Average Standard Deviation
3.1 1.8
1.9 0.4
3.4 0.6
5.0 2.1
1 0
1 1
1 0

Reference
Battelle (1977)
It
II
It
II
Singh et al . J 980
ti
it
it
Singh et al . 1979
II
II

r

-------
TABLE 4-
            CONCENTRATIONS OF TRICHLOROETHANES DETECTED IN WATER
Sample Type/Date
DRINK inn WATER—
SURFACE WATER



8-78/6/79
6/12/1978
2/76-2/78
DRINKING WATER—
GROUNDWATER



	 	 ,
Location



All over U.S.
Nlngiira Falls, NY
Poughkeepsle, NY
Waterford, NY




— 	 • 	 	 	 	 	 _____
Concentration
1,1.1- 1.1,2-
Detected In ~T7lO~ I/ 10
Hi eh Concentration 8,5 iie/K <1.0 iig/
Raw Finished
No. Samples 105 103
t Positive 12.4 21.8
Mean 0-32 pg/« 0.56 pg/t
Median 0.2 0.4
RanBe 0.1-1.2 0.1-3.3
Detected 9.92 of finished surface
water samples.
Mean of all samples » 0.12 lie/I
Max. 2,250 pg/t
1.1.1- 1.1.2-
Detected in 15/330 Not
Average of 2.2 ng/« Analyzed
Positives
Range <0 5-650 Mg/£
<0.33, l.l ug/
4 samples, all <5 |ig/t
0.1 I'g/t, ND, 6 samples <2 pg/t

Kaw Finished
No. Samples 13 23
% Positive 23.1 21.7
Mean 4-8 |ig/t 2.13 |ig/t
Median 1.1 2.1
Range 0.3-13.0 1.3-3.0
Oetecte.l in 22. 2* of finished ground
water samples.
23% of 1611 wells tested in three
states were positive.

	 — 	 — 	 _
Comment
NORS
-
NOMS 	
| of positive samples
CWSS Data
,1,1- Finished Drinking Water
Supplies

NOMS ,
> of positive samples

	 " 	 "1
Reference
EPA (1975)

'OnJgllo £t aK (1980)
Brass (1981)
Kim and Stone (1979)





-------
TABLE 4-2.  CONCKNTRATIONS OK TRICIII.OROETHANES  DKTECTKD IN WATER (Continued)
Sample Type/Date



4/28/78

Location
i
Alabama
Connecticut
Florida
Idaho
Kentucky
Maine
Massachusetts
New Hampshire
New Jersey
New York
Norlh Carolina
Rhode Island
South Carolina
Tennessee
Washington
New Jersey
Nassau County, L.I., NY
All Over U.S.
Concentration
No. Wells Tested % Positive
80 10
1200 ?
329 15
9 11
22 0
89 18
163 21
6 0
All 48
372 9
44 2
88 ?
4 0
50 26
32 69
iil«lz 1.1.2-
No. Samples 394 399
K, Positive 10 66
<1.0 M8/1 376 203
1-10 |.B/» 17 141
10-1000 ng/l 1 55
>100 |ig/l - ]
yi.l- 1,1.2-
No. Tested 372 372
No. Positive 33 50
% Positive 9 13
Maximum 310 ng/l 300 ng/t
1 ,1,1- 1,1,2-
Detected In 3/106 Not
Average of 2.8 ug/H Analyzed
Positives For
Range <0.5-7 |ig/l
Comment Reference
* ~ " '— — - -
1 ,1,1-Trlchloroethane Conlgllo et al. (1980
i
i
i
n
•i
CWSS , Brass (1981)
1

-------
                                    TABLE 4-2.   CONCENTRATIONS OF TRICIII.OROETHANES DETECTED IN WATER  (Continued)
Sample Type/Date
AMBIENT SURFACE
WATER	

   11/76- 1/77
WASTEWATER
  1977
  l're-1977
      location
Near Production Plants
                   Chicago
                   Illinois
                   Pennsylvania

                   New York City Area
                   Hudson River Area
                   Upper & Mid-Mississippi R
                   Lower Mississippi River
                   Houston Area
                   OliJo River Basin
                   Oreat Lakes
                   Tennessee River Basin
                                                         Concentration
                                                                    0.5-8 (3)
                                            0.05  ng/t- 16,500 |ig/t
                                                                  Concentration
                                            No. Samples          Range (Mean)
                              11
                              12

                              14
                               I
                               3
                               1
                               3
                               3
                               6
                               2
                          Detected 2-300   ug/t
1-2
                                                                      and 4  (<2)
                          Not Detected


                          Maximum  8 |ig/t


                                   1 Mg/l
                                   4 Hg/e
                                                                                           Commen t
                                                                Sediment ND - 6.1  ug/kg
              Lake Michigan,  sewage  plant
               effluent,  fllltratlon plant,
               channels
              Illinois River
              Delaware, Schuylklll,  Lehlgh
               Rivers
              Hudson River and Bays
              Calveston Bay and Channels
               6/129 Raw Waste Samples from
                Textile Plants
               0/129 Secondary Effluent
                Samples

               3/4 Sewage Treatment Plant
                Effluents
               2/18 Finished Waters
               25/182 Ambient Samples
                                                                                                                        Reference
                                             Battelle  (1977)
                                                                                                                  Battelle (1977)
                                                                                                                  Raw] Ings and  Sanflcltl
                                                                                                                   (1978)
                                                                                                                  U.S. EPA  (1977)

-------
     As Table 4-3 exhibits, the majority of STORE! data values  for
 trichloroethanes have associated remark codes: ambient data—1,1,1-
 trichloroethane  (85%), 1,1,2-trichloroethane  (94%); effluent  data —
 1,1,1-trichloroethane (76%), 1,1,2-trichloroethane (97%).  The  remark
 codes include:J — estimated value; K—actual value is known  to be less
 than value given; and U— material analyzed for but: not detected.

     A detection limit (K remark) of 10 yg/1 appears most frequently
 in association with observations from sampling in a.mbient waters — for
 1,1,1-trichloroethane,34% of the time and for 1,1,2-trichloroethane,
 36% of the time.  Sampling in effluent waters reflects several  frequently
 used detection limits:  0.01, 1.0, 5 and 10 yg/1.   These limits  combined
 account for 52% of the values recorded for 1,1,1-trichloroethane and
 81% for 1,1,2-trichloroethane.  Levels might therefore be less  than or
 equal to the reported value.

     The distribution of unremarked STORET observations is presented
 in Table 4-4.  The majority of ambient and effluent values range between
 1 yg/1 and 10 yg/1, inclusively; the exception is ambient values recorded
 for 1,1,2-trichloroethane for which 60% are less than 1 yg/1.

     As of October 2, 1980, 80 observations of 1,1,1-trichloroethane
 in sediment and 79 observations of 1,1,2-trichloroethane were recorded
 in STORET.  The observations reflect regional conditions for the
 South, Southwest, and West, for sampling has occurred in only ten states:
Alabama, Arizona, California, Idaho, Louisiana, Nevada, New Mexico,
Oregon, Texas,  and Washington.  Table 4-5 shows the ranges for unremarked
and remarked values and the number of observations within each category.

     Dickson and Riley (1976) reported concentrations of trichloroethanes
 (1,1,1 and 1,1,2-isomers  were not distinguished)  between 16 ng/g and 2  ng/g
in aquatic biota in the United Kingdom.

     STORET system also contains observations in fish tissue.  Sampling
has been conducted in the ambient waters of nine states:   Alaska,
California, Idaho, Kansas,  Louisiana, Nevada,  Oregon,  Texas,  and
Washington.  The concentration ranges of unremarked and remarked data
are presented in Table 4-6.

     Only one study (McConnell e_t al. 1975)  provides  data concerning
1.1.1-trichloroethane in  foods.   The sampling was  done in the United
Kingdom.  No data are available concerning concentrations of  the
1,1,2- isomer in food.   Table 4-7 shows the concentrations of  1,1,1-
trichloroethane ranging from 1 yg/kg to  10 yg/kg.   PVC used in food
storage containers was found to contain  the 1,1,1-isomer,  but none was
found to have contaminated  cooking oils  purchased  in  these containers
 (Gilbert et al.  1978).   Subsequent to the study,  the  manufacturer of
the bottles disclosed that  1,1,1-trichloroethane was  no longer present
in food packaging grades  of PVC.
                                 4-8

-------
         TABLE 4-3.   STATUS OF STORET DATA FOP. CONCENTRATIONS OF
                     1,1,1- AND 1,1,2-TRICHLOROETHANE IN AMBIENT
                     WATER AND EFFLUENT
   Status
   Observations
                       Number   % in Range     Range in Values (ug/1)
 Ambient Data:
 l>l»l-trichloroethane
    unremarked          54
    remarked K         213
    remarked U          99
                       366

 1,1,2-trichloroethane
    unremarked          20
    remarked K         214
    remarked U         123
                       357

 Effluent  Data:
 1,1,1-trichloroethane
    unremarked         126
    remarked J            2
    remarked K         360
    remarked U          43
                       531
1,1,2-trichloroethane
   unremarked
   remarked J
   remarked K
   remarked U
 13
  2
411
 43
469
           24
                         0.3  -  1600.0
                         0.3K - 50.OK
                         O.OU - 10.OU
                        0.5 - 58.0
                        0.5K - 50.OK
                        O.OU - 10.OU
0.2 - 7100.0
2.0J - 7.0J
O.OK - 20.OK
O.OU - 5.0U
1.1 - 3000.0
3.0J - 6.0J
O.OK - 20.OK
O.OU - 5.0U
Source:  U.S. EPA STORET Water Quality System, as of September 24, 1980,
KEY:  J - estimated value; K - actual value less than value given;
U - analyzed for but not detected.
                                 4-9

-------
              TABLE 4-4.  DISTRIBUTION OF UNREMARKED VALUES
                          IN STORET FOR CONCENTRATIONS OF
                          1,1,1- AND 1,1,2-TRICHLOROETHANE
                          IN AMBIENT WATER AND EFFLUENTS
                    1,1,1-Trichloroethane   1,1.2-Trichloroethane
                    Ambient
Effluent
Ambient
Effluent
Concentration
(Vig/l)
<1
1-10
11-100
101-500
501-1000
>1000

No.
Obs.
13
22
14
3
1
1
54

%
24
41
26
6
2
2

No.
Obs.
11
76
28
9
0
2
126

%
9
60
22
7
-
2

No.
Obs.
12
7
1
-
-
-
20
No.
% Obs.
60 0
35 6
5 2
4
0
1
13

%
^
46
15
31
—
8

Source:  U.S.  EPA STORET Water Quality  System,  as  of  September  24,  1980,
                                  4-10

-------
           TABLE 4-5.  CONCENTRATIONS OF TRICHLOROETHANES  IN
                       SEDIMENT REPORTED IN STORET
Compound/Status of Observation            Concentration

                          No.              Range
                      Observations        (yg/kg)

1,1,1-trichloroethane

   unremarked             15              0.1-16.6
   remarked K             49              5.OK - 15000.OK
   remarked U             16              O.OU - 5U
                          80

1,1,2-trichloroethane

   unremarked              7              0.3-7.0
   remarked K             56              5.OK - 580.OK
   remarked U             16.              O.OU - 15000.OU
                          79


Source:   U.S. EPA STORET Water Quality System, as of September 24,  1980,
                                4-11

-------
            TABLE 4-6.   STORE! DATA CONCERNING LEVELS
                         OF TRICHLOROETHANES  IN FISH
                         TISSUE
Compound/Status Observations
                                          Concentrations
                           No . •
                      Observations
1,1, 1- trichloroethane
   unremarked
   remarked K
   remarked U
                          19
                          47
                          _7_
                          73
                                           Range
                                          (ug/kg)
                                          0.002 - 0.97
                                          0.005K - 20. OK
                                          O.OU
1,1, 2-Trichloroethane
   unremarked
   remarked K
   remarked U
                          64
                          _7_
                          71
                                          0.005K - 20. OK
                                          O.OU
Source:  U.S. EPA STORET Water Quality System.
                                4-12

-------
           TABLE  4-7.   LEVELS  OF  1,1,1-TRICHLORETHANE
                       DETECTED IN  FOODS  IN THE  UK
                                             Concentration
Food Type                                       (ug/kg)

 Meats

   English beef, steak                            3
   English beef, fat                              6
   Pig's Liver                                    4

 Oils and Fats

   Olive Oil (Spanish)                           10
   Cod Liver Oil                                  5
   Castor Oil                                     6

 Fruits and Vegetables

   Potatoes (S. Wales)                            4
            (NW England)                          1
   Apples                                         3
   Pears                                          2

 Packet Tea                                       7

 Fresh Bread                                      2
Source:  McConnell et al. (1975).
                                  4-13

-------
4.3  ENVIRONMENTAL FATE

4.3.1  Overview

     The trichloroethanes have high volatilization rates relative to
many other organic chemicals due to their high vapor pressures, even
though their solubilities are high also (Table 4-8).  The primary fate
pathway for these chemicals is volatilization from surface water or
soil, followed by slow  photooxidation in the atmosphere.  Atmospheric
lifetime due to  photooxidation for 1,1,1-trichloroethane is on the
order of six to ten years, long enough for global mixing and transport
to the stratosphere to occur.  (Hemispheric and stratospheric mixing
occur on a time scale on the order of a half year to a year.)  Decom-
position in the stratosphere can release Cl atoms, which may cause
ozone depletion.  Estimated ozone depletion due to the 1,1,1- isomer
are about 1.3% of the total ozone or less,  depending on assumptions of
continuing release rates.  Little information on the amospheric fate
was found of the 1,1,2-isomer although it may photooxidize more rapidly
than the 1,1,1-isomer.

     The following three sections summarize aquatic fate processes, soil
transport and volatilization, and atmospheric fate processes.

4.3.2  Aquatic Fate Processes

4.3.2.1  Hydrolysis

     Dilling et al. (1975) found that 1,1,1-trichloroethane in sealed
tubes had a 6.9-month half-life for hydrolysis at 25°C.  Decomposition
products were acetic and hydrochloric acids, along with a minor amount
of vinylidene chloride.  In aerated water in a closed system decomposition
occurred with a half-life of about 6 months in either dark or in sun-
light.  This time is similar to the 6.9 months for hydrolysis.

     McConnell et al. (1975) reported that the 1,1,1-isomer is subject
to dehydrochlorination at a rate dependent upon pH.  Chemical half-life
in seawater is estimated to be 9 months at pH 8 and 10°C.  The decom-
position product is vinylidene chloride, with a minor amount of acetic
acid arising by hydrolysis.  In aqueous systems, metallic iron was
found to accelerate decomposition, but degradation products were not
known.

     Dilling et al. (1975) inferred from their experiments that 1,1,1-
trichloroethane is chemically stable in water.  This is probably a
reasonable assumption for surface waters particularly in contrast to the
much more rapid volatilization rate.  However, for 1,,1,1-trichloroethane
in groundwater, where volatilization is not possible, hydrolysis may be
an active fate mechanism.  The 6-9 month half-life for hydrolysis
indicates that about 90% of 1,1,1-trichloroethane in an aquifer would be
decomposed in about 2 years.


                                  4-14

-------
    Property

    Synonyms
 1,1,l-Trichloroethanea

Alpha-trichloroethane
Methyl chloroform
1,1,2-Trichloroethaneb

vinyl trichloride
    Molecular formula

    Formula weight

    Boiling point


    Melting point

    Vapor density

    Specific gravity


    Solubility



    Density of saturated air

    Concentration of  saturated air


    Vapor pressure
   Conversion factors-Air

   (25C 760 mm Hg)
 N10SII 1976
133.41

74.0 C  (165.2 F)
(760 mm Hg)

-32.62 C  (-26.7 F)

4.6 (air = 1)

1.339 at 20 C (water -
1.000 at 4 C)

4400 mg/1 water at 25 C
soluble in ethyl ether,
ethyl alcohol

1.6 (air = 1)

16.7% by volume at 25 C


 62 mm Hg at 10°C
100 mm Hg at 20°C
127 mm Hg at 25°C
150 mm Hg at 30°C
240 mm Hg at 40°C
     3
1 g/m  = 183 ppm
                 3(b)
1 ppm = 5.54 mg/m
133.41

113.7°C


-35, -36.7 C

4.63 (air - 1)

1.44 at 20°C  (Water = 1.00
at 4°C)

4500 mg/1 water at 20°C
136 g/m  at 20°C
225 g/m  at 30°C

19 mm Hg at 20°C
32 mm Hg at 30°C
40 mm Hg at 35°C
      3
     i

1 ppm =
      3
1 mg/m  =0.18 ppm

        5.55 mg/m
b
 Verse luioren 1977

-------
4.3.2.2  Sorption onto Sediments

     No information has been found concerning the sorption of trichloro-
ethanes, although the organic carbon partition coeffficient (K  ) for
the 1,1,1- isomeris reported to be 180 (Karickhoff et al. 1979*??  The
Koc for 1,1,2- isomer is estimated by the method of Chiou _et al. (1979)
to be 57.  These Koc values indicate that the trichloroethanes will
sorb to a high degree onto organic matter in soils or sediments.

4.3.2.3  Volatilization from Water

     Billing (1977) found that 1,1,1-trichloroethane volatilized with a
half-life of 15.3 - 28.2 minutes from a stirred (200 rpm) 250-ml beaker
holding 200 ml of a 1 ug/1 solution, 6.5 cm deep.  Under similar con-
ditions Dilling et al. (1975) found a half-life of about 20 minutes for
the same isomer.  90%  volatilized in 60-80 minutes.  For 1,1,2-trichloro-
ethane, the half-life was 21 minutes and the time to 90% loss was
reported to be 102 minutes.

     The Dow Chemical Company (Battelle 1977) has reported the following
evaporation rates from a similar experiment:

     ..  ,.                                           T, ,„ minutes
     Medium                                          1/2	

Tap Water at 25 °C                                       22
Tap Water at 1-2°C                                      33

3% Salt Solution                                        25

Water with ^500 mg/kg peat moss                         20
Water with ^500 mg/kg wet bentonite clay                20

Water with 2.2 mph wind                                 17

     These laboratory measured rates are not directly indicative of
volatilization rates from natural water bodies.  When compared with
volatilization rates found in a similar manner for other organic
chemicals, the trichloroethanes will apparently volatilize relatively
quickly.  Thus, the trichloroethanes will probably volatilize rapidly
from natural water bodies when compared with the other organic chemicals.

     Appendix D details estimations of volatilization rates from natural
water bodies.  The half-life for 1,1,1-trichloroethane from aim deep
stream  flowing at 1 m/sec with a 3 m/sec wind speed is about 4 or 5
hours.  For a 10 m deep stream, the half-life increases to about 6.7 days.
Time to 90% loss is about three half-lives, or 12 hours to 20 days.  For
the 1 m/sec current speed, the distance to 90% loss is 43 to 1700 km
downstream.  These estimates may represent upper limits since other
conditions, such as high wind speed or turbulence in the water, would
increase the volatilization rate.  Estimated volatilization rates for
1,1,2-trichloroethane are similar, but about 20% slower.


                                 4-16

-------
 A.3.2.4  Biodegradation

      Tabak £t a]L_ (1980) conducted static culture flask tests to
 determine the susceptability of the trichloroethanes to microbial
 degradation.   Wastewater microbiota and a yeast extract were used
 to inoculate 5 mg/1 and 10 mg/1 solutions of the 1,1,1- and 112-
 isomers. Figure 4-1 shows that 15-25% of the 1,1,1- isomer and 55-60%
 of the 1,1,2-isomer remained after 21 days.  Though these results may
 not be totally representative of susceptability to biodegradation in
 the environment, they are indicative of the potential for these com-
 pounds to biodegrade in the environment and in waste treatment processes,

 4.3.3    Soil Transport and Volatilization

 .     Wilson |t al.. (1980)  studied  the transport and  fate of chemicals
 including 1,1,2-trichloroethane applied to a sandy soil composed of
 92/.  sand; 5.9* silt,  2.1%  clay  and 0.08% organic carbon.  The  results
 are  somewhat ambiguous  since more  compound was  recovered than  was
 applied.  More than half of  the 1,1,2-trichloroethane in a  water
 solution apparently volatilized, although more  than  one-half apparently
 percolated  through the  140-cm soil column (Table 4-9).   None  was
 degraded.   Soil  columns were not saturated.

     When Wilson et aT._ (1980)  compared  volatilization  from the  soil
 column to volatilization from water, they found  that volatilization
 from soil was inhibited by the  soil by about a factor of ten or more
 (forna,502)  of 1,1,2- isomerapplied to soil  may
       volatilize.

     •  A large part  (>50%) may  percolate through the soil column.
       The  chemical is  minimally retarded by sandy soil.

     •  Volatilization from the  soil  column will  occur at a  rate  ten
       or more  times slower  than from a  water column of similar  depth.
                                4-17

-------
                                                          % Remaining from Original

                                                                 Concentration
                                                                                  % Remaining from Original

                                                                                       Concentration
-O
 I
M
OO
                   w

                   J>
                                5?  Z
                                2  o
                                c  ••*
                                o>   Ol
                                o"  3
                                51-  1
\°L  w


~  I

CO  oi
00  r*
O  ^J

~  6.
    Ol
    <

    5'

    o>
    -1
    <
                    M

-------
        TABLE  4-9.   FATE OF 1,1,2-TRICHLOROETHANE APPLIED TO
                    A SOIL COLUMN IN THE LABORATORY
                                        Fate (%)
                                                              Degraded or
Concentration Applied.(mg/I)  Volatilized  Column Effluent  not Accounted for

       1.000                  56 ±16       65 ± 12            -21 ± 10

       0.16                   95+13       61 ±  5            -56 +  7



Source:  Wilson et al. (1980).
                                  4-19

-------
      In soils in which a large organic matter component is present
 volatilization and transport rates will probably be slower than those
 described here, due to sorption onto the organic matter.

   .   No comparable information has been found for 1,1,2-trichloroethane.

 4.3.4   Atmospheric Fate Processes

      Appendix E discusses the atmospheric fate of the trichloroethanes
 in detail.   A summary is reported here.   Most of the information found
 related to  1,1,1-trichloroethane  with relatively little information
 found concerning the  fate of 1,1,2-trichloroethane in the  atmosphere.

      The 1,1,1-isomer is long lived in the atmosphere.  The residence
 time based on destruction by photooxidation is estimated to be  6-10
 years or longer.  Consequently, 12-25% of global emissions will  reach
 the stratosphere to be distributed globally.  Actual concentrations
 vary according to location, latitude, hemisphere, and altitude.  Higher
 concentrations are found in the northern troposphere than in the strato-
 sphere or Southern Hemisphere.  Atmospheric concentration, in general,
 have increased with time due to increasing use of the chemical.
      Final disposition of 1,1,1-trichloroethane is in  the atmosphere
 due to photooxidation in  both the  troposphere  and  the  stratosphere.
 Chlorine  atoms may be released to  attack  and  deplete ozone.  Estimates
 of ozone  depletion due to the 1,1,1-isomer are 0.2%  to  1.2% of  total
 ozone.  In comparison, the total  depletion due to  chloroflurocarbons
 released  in 1973  is estimated to be about 7% of total steady-state ozone.

      The  compound 1,1,2-trichloroethane was found  to be  30-50 times
 more  reactive than the 1,1,1-isomer when  studied in a laboratory
 photochemical apparatus  (see Appendix E).  The 1,1,2- isomer photolyzed
 "rather rapidly"  forming  formyl chloride, phosgene, and  chloroacetyl
 chloride  as decomposition products.  The  environmental significance
 of this test was not established; however, the results can be reasonably
 assumed to indicate that  the atmospheric  lifetime of 1,1,2-trichloro-
 ethane is about a factor  of ten less than the lifetime of 1,1,1-
trichloroethane, i.e., about 1 year.

 4.4  MODELING OF ENVIRONMENTAL DISTRIBUTION
4.4.1  Ambient Concentrations

     Fugacity models can be used to estimate ambient environmental
 concentrations for some chemicals; however,  these models are inappropriate
 for 1,1,1-trichloroethane due to the long lifetime of the chemical,
 its pervasiveness, and global distribution.   Distributions  and releases
 of 1,1,2-trichloroethane appear to be so limited  that  an equilibrium
modeling approach is not appropriate.   The model environments  and
 compartments for these chemicals are not clearly defined.  The
 fugacity models were not applied for these reasons.
                                4-20

-------
   .4.2  EXAMS Model Results
  i  i  o    .*?? purpose of estimating the potential  fate of 1,1,1- and
  1,1,2-tnchloroethane in various aquatic environments under conditions
  mfdein^?n?U? dlSChar?e' the f^5 (E^osure Assessment Modeling Syste
                38
                                                           nons
              dlSChar?e' the f^5  (E^osure Assessment Modeling System)
               38 lmPlemented^.S.  EPA 1980).  The physical-chemical
      i   /  a    ^action rate constants used as inputs are listed
tL nuino    f    arb*trary loadinS r"e of 1.0 kg/hr was chosen for
the purpose of  comparing the compound's fate in different systems -
a pond,  oligotrophic lake,  eutrophic lake, average river, turbid river
and coastal plain river.  The simulated systems represent "average"
US  water  bodies.  Their properties (i.e., biomass,  sediment concen-

     °
                                                  ,
  rn r°Si laanf10  conditions> «re described in the model  output

            -   '      "** ^ ^^  ^ depth are
  for
      Tables 4-11  through 4-15 present the output of the EXAMS simulations

 in vartr" S**',  ^^ are  ™™** concentrations af equStt
 due to dif'f^f ^  fWf "' Sediment« biota' «c.)  and percentage loss
 aue to different  fate processes.
 volatitin 8l8?lf±5
-------
             TABLE 4-10.  PARAMETERS FOR TRICHLOROETKANES
                          USED  IN EXAMS ANALYSIS3
Property

Molecular Weight

Solubility

Liquid Phase Transport
   Resistance

Henry's Law Coefficient

Vapor Pressure

Partition Coefficient:
   • Biomass/Water

   • Sediment/Water

   • Octanol/Water

Chemical Oxidation Rate

   • Water

   • Sediment

Hydrolysis Rate
Isomer
1,1,1-
133.4
4400
0.53
3.9 x 10~3
100
81
152
320
1
1
1.7 x 10~4
1,1,2-
133.4
4500
0.53
7.4 x 10"4
19
33
56
117
1
1
1.2 x 10~7
Unit
g/mole
mg/1
unitless
m /mole
torr
Ug/g
mg/1
mg/kg
mg/1
mg/1
mg/1
mole/1/hr
mole/1/hr
mole/1/hr
 •Source:  SRI (1980).
                                  4-22

-------
              TABLE 4-11.   FLOW AND DEPTH OF EXAMS SIMULATED SYSTEMS'
                                      Depth (m)




.p-
1
N)
U)



System
Pond
Eu trophic Lake
Oligotrophic Lake
River
Turbid River
Coastal Plain River

Water Flow
(m /day)
0.643
4.1x5b
5b
4.1x10
2.4xlO?
2.4xlO?
2.4xl06

Water
Column
2
20 C
20°
3
3
3

Sediment
0.05
0.05
0.05
0.05
0.05
0.05
Sediment Mass
in Water
Column (kg)
600
2695(3)
525(3)
6xl04
3xl05
6000

Length (m)
NA
NA
NA
3
3
3
All data from EXAMS (1980)  output.
Average flow for littoral zone, epylimnion and hypolimnion.
Includes epylimnion and hypolimnion (deepest part of lake).

-------
                       TABLE 4-12.  STEADY-STATE CONCENTRATION IN VARIOUS CENTRALIZED AQUATIC SYSTEMS
                                    RESULTING FROM CONTINUOUS 1,1.l-TRICHLOROETUANKS DISCHARGE AT
                                    1.0 lqj/lird
                                                             Maximum Concentrations
     Pond

*•    Eutrophic
NJ    Lake

     01igotrophlc
     Lake

     R i ve r

     Turbid  River

     Coastal  Plain
     River
Loading

1.0 kg/hr

Water
Total
i»fi/l)
2.6
0.13
0.14
9.9 x 10~4
9.9 x 10~*
9.3 x 10~3

Bottom
Sediment
(mg/1)
2.1
1.2 x 10~2
2.8 x 10~3
2.5 x 10~A
5.4 x 10~A
2.8 x 10~3
Maximum in
Sediment
Deposits
(ing/kg)
32
7.1 x 10~2
2 x 10~2
2.6 y 10~3
1.9 x 10~3
4.3 x 10~2


Plankton Benthos
(t'g/g) (UR/jO
210 170
10 0.9
11 0.23
8 x 10~2 2 x 10~'
8 x 10~2 4 x 10~'
0.75 0.22
                                                                                                               Total  Steady-
                                                                                                               State  Accumulation
                                                                                            74

                                                                                           310


                                                                                           340


                                                                                            0.91

                                                                                            0.90

                                                                                            8.4
    a
     All data simulated by  EXAMS model  (see text for further  information).

-------
           TABLE 4-1).  THE FATE OF 1,1 ,1-TRICHLOROETHANE IN VARIOUS CENKKALIZED AQUATIC SYSTEMS*





J^
KJ
Cn
System
Pond
Eu trophic
Lake
Oligotrophlc
Lake
Kiver1'

Turbid
i> i vu _ d
Water at Steady-
state
71
99
>99
97

98

K, teaming in
Sediment at
Steady-state
29
1
«


2

A I rans termed
by Chemical
Processes
1
5
6




% Transformed
by Biological
Processes
0
0
0

0


% Volatll-
i zed
92
91
90

2

2
% Lost
by other
Proccessi's
7
4
4

98

98
Time for
System Sei 1 -
Purl f icat i in
2700 hours
56 days
64 days

39 hours

21 hours
Coast ;il  Plain
                  93
                                                   0
                                                                  0
                                                                               14
                                                                                          86
                                                                                                       180 hours
'All data  simulated by the EXAMS model (see text  for  further information).





 Including loss through physical transport out of system.

                                                    s-sre


-------
                  TABLE 4-14.  STEADY-STATE CONCENTRATIONS IN VARIOUS GENERALIZED AQUATIC SYSTEMS
Maximum Concentrations



System Loading
Pond 1.0 kg/hr-1
Eutrophl c
Lake
Oil go trophic
Lake
T River
to
Turbid River
Coastal Plain
River

Water
Total
(mg/1)
3.4
0.14

0.15

9.9 x 10~4
9.9 x 10~4
9.4 x 10~3


Bottom
Sediment
(mg/1)
2.0
0.007

2.1 x 10~3

3 x 10~4
6.2 x 10~4
3 x 10~3

Maximum in
Sediment
Deposits
(mg/kg)
12
0.017

5.3 x 10~3

1.2 x 10~3
9.2 x 10~4
1.8 x 10~2


Total Steady-
Plankton Benthos slate Accumulation
(MB/B) (ng/g) (kg)
110 67 76
4.6 0.2 380

4.8 0.007 410

3.3 x 10~2 9.8 x 10~3 0.9
3.3 x 10~2 2 x 10~2 0.9
0.31 0.1 8.2

:l
 All  data  simulated  by  EXAMS model  (see text for further information).

-------
                TABLE 4-15.  THE  KATE OF  1,1,2-TRICHLOROETIIANE IN VARIOUS GENERALIZED AQUATIC SYSTEMS1
% Residing in % Residing in
Water at Steady- Sediment at
System slate Steady-state
I'ond 89 11
En trophic 99 1
Lake
Oligotrophlc >99 <1
Lake
RlviTd 99 1
Turbid 99 1
J^~ , , .1
1 IUverd
ts>
Coasial Plain 98 2
H i vi- r d
% Transformed Z Transformed X Lost Time for
by Chemical by Biological % Volatil- by other System Scl
Processes Processes ized Processes1' Purlflcatii
0 0 91 9 1030 hours
0 0 95 5 71 days
0 0 94 6 76 days
0 0 1 99 17 hours
0 0 1 99 12 hours


0 0 12 88 64 hours
 AH  data  simulated by the EXAMS model (see text for further information).


 Including loss through physical transport out of system.
"Estimate for removal of ca.  75% of  the  toxicant  accumulated  in system.   Estimated from the results of the half-lives
 for the toxicant In bottom sediment and water  columns,  with  overall cleansing time weighted according to the toxicant's
 initial distribution.
d
 All river systems are 3 km In length  so  that  physical  transport  out of  the nodeled system is dominant loss process.
 The "river" system was extended  to  various  lengths  up  to 1000 km from the source to determine the significance of
 other fate processes (see text).

-------
N>
OO
                                1,1.1 — Trichloroethane
                                1,1.2 — Trichloroethane
                                                                                 300
                                                                                                                  3000
                                                                  Km
                               FIGURE 4-2.   PERCENTAGE OF TRICHLOROETHANE LOSS DUE TO VOLATILIZATION
                                             AS FUNCTION OF DISTANCE FORM POINT SOURCE

-------
 concentrations were usually two orders of magnitude greater than water
 levels.  The 1,1,1-isomer had a slightly greater affinity for bio-
 accumulation and adsorption onto sediment than did  the  1,1,2- isomer.  This
 behavior would be expected based on their respective partition coefficients,
 shown in Table 4-10.  The following conclusions can be  drawn from the
 EXAMS analysis about the potential environmental fate of the trichloro-
 ethanes in aquatic systems.  Persistence depends primarily on volatilization
 since chemical degradation is minimal.  The estimated half-lives (under
 conditions of continuous discharge) are listed in Table 4-16.  The
 half-lives for the other rivers are not included because the lengths
 modeled were so short that physical export of the chemical out of the
 segment was responsible for over 85% of removal.  Persistence would
 be greater in the coastal plain river than in the average river due to
 the higher biomass retaining some fraction of the chemical.  Since
volatilization is so important in all systems, conditions of high
 temperatures, high wind velocity, water and air turbulence, and low
biomass would all increase the rate of trichloroethanes to the atmos-
 phere in real systems.  This assumes negligible transformation of the
 compound in both liquid and vapor form.  For the 1,1,1- isomer,  hydrolysis
was detectable as a mechanism of removal in static systems; however,
it was never competitive with the process of removal in static systems
and it was never competitive with the  process  of volatilization.
In the pond system, a half-life of 5700 hours was estimated for
 chemical loss alone as compared with a significantly shorter half-life
of 60 hours due to volatilization only.  As can be seen on Table 4-16,
the total system half-life for 1,1,1-trichloroethane was 50 hours,
which is quite close to the volatilization half-life.
                                4-29

-------
       TABLE 4-16.  HALF-LIVES FOR TRICHLOROETHAMES
                    PERSISTENCE IN GENERALIZED
                    AQUATIC SYSTEMS
System

Oligotrophic Lake

Eutrophic Lake

Pond

River
    Persistence Chrs)

1*1.1-             1,1,2-
 230

 210

  50

  40
280

260

 50

 40
Source:  U.S.  EPA (1980c).
                              4-30

-------
                              REFERENCES

Battelle Columbus Laboratories.  Multi-media levels-methyl chloroform.
EPA 560/6-77-030.  Columbus, OH:  Battelle Columbus Laboratories, U.S.
Environmental Protection Agency; 1977d.

Battelle Columbus Laboratories.  Environmental monitoring near industrial
sites.  Methyl chloroform.  Columbus, OH:  Battelle Columbus Laboratories,
1977b.

 Brass,  H.   Final community water supply survey.  (CWSS).   Cincinatti,  OH:
 Office  of  Drinking Water,  U.S.  Environmental Protection  Agency;  1981.

Chiou, C.T.; Peters,  L.J.; Freid,  V.H.  A physical concept of soil-water
equilibria for nonionic organic compounds.  Science 206  (4420): 831-832;
1979.

Coniglio, V.A.; Miller, K.; Mackeever, D.  The occurrence of volatile
organics in drinking water.  Briefing.  Washington, DC:    Criteria and
Standards Division,  U.S. Environmental Protection Agency, 1980.

Correia, Y.; Martens, G.J.; Van Mensh, F.H.; Whim, B.P.  The occurrence
of trichlorethylene,  tetrachloroethylene, and 1,1,1-trichloroethane in
Western Europe in air and water.  Atmos. Environ. 11(11): 1113-1116;
1977.

Cox, R.A.;  Derwent,  R.G., Eggleton, A.E.J.; Lovelock, J.E.  Photochemical
oxidation of halocarbons in the troposphere.  Atmos. Environ. 10: 305-308;
1976.

Cronn,  D.R.; Rasmussen, R.A.; Robinson, E.  Measurement of tropospheric
halocarbons by gas chromatography,  mass spectrometry.  Report for Phase
II.  Research Triangle Park, NC:  U.S. Environmental Protection Agency;
1977a.

Cronn,  D.R.; Harsh,  D.E.  Determination of atmospheric halocarbon
concentrations by gas chromatography-mass spectrometry.  Anal. Lett.
12(B14): 1489-1496;1979.

Cronn,  D.R.  Measurements of atmospheric methyl chloroform by Washington
State University. In Proceedings of the conference on methyl chloroform
and other halocarbon pollutants.  Research Triangle Park, NC:  U.S.
Environmental Protection Agency; 1980b.

Dickson, A.G.; Riley, J.P.  The distribution of short-chain halogenated
aliphatic hydrocarbons in some marine organisms.  Marine Pollution
Bulletin 7(9): 167-169; 1976.

Dilling, W.L.; Tefertiller, N.B.;  Kallos, G.J.   Evaporation rates of
methylene chloride,  chloroform, 1,1,1-trichloroethane, trichloroethylene,
tetrachloroethylene,  and other chlorinated compounds in dilute aqueous
solutions.   Environ.  Sci. Technol.  9(9):833-838; 1975.
                                  4-31

-------
 Billing, W.L.  Interphase transfer process.  II. Evaporation rates of
 chlorome thanes, ethanes, ethylenes, propanes, and propylene from dilute
 aqueous solutions.  Comparisons with the sketical predictions.  Environ.
 Sci. Tecnnol. 11: 405-409; 1977.

 Karickhoff,  S.W. ; Brown  D S •
 pollute. on
 Lillian, D.;  Singh, H.B.; Kopleby, A.; Lobban, L. ; Arnts, R.;  Gumpert,
 R.; Hague, J. ; Toomey, J.; Kazazis, J. ; Antel, M. ; Hansen, D.;  Scott,
 B.  Atmospheric  fates of halogenated compounds.   Environ. Sci.  Technol
 9:1042-1048;  1975.

 McConnell, G. , Ferguson, D.M., Pearson, C.R.  Chlorinated hydrocarbons
 and the environment.  Endeavor. 34:13-18; 1975.

 Rawlings, G.D.;  Sanfield, M.  Toxicity removal of secondary effluents
 from textile plants.  EPA- 600/7- 78- 168.  Washington, DC.  U.S.
 Environmental Protection Agency, Symp. Proc. Process. Measurement
 Environ.  Assess 331:153-169; 1979.

 Singh, H.B.;  Salos, L.J.; Cavanaugh,  L.A.  Distribution sources and
 sinks of atmospheric halogenated compounds.   J. Air Pollut.  Cont
Assoc. 27:332-336; 1977.

Singh, H.B.;  Salas, L. J. ; Sheigeishi, H. ;  Smith, A.H.  Fate of halogenated
compounds in the atmosphere.   Menlo Park, CA;   Stanford Research Institute-
1978 Available from NTIS  PB 278198.

 Singh, H.B.; Salas, L.J.; Smith, A.;  Shigeish, H.   Atmospheric measure-
ments of selected toxic organic chemicals, First Year Interim Report.
 Research Triangle Park, NC:  Environmental Sciences Research Laboratory,
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 Singh, H.B. ; Salas, L.J.; Smith, A.;  Shigeish, H.  Selected hazardous
 organic chemicals, Draft Second Year Interim Report; 1980.

 Symons, J.M. ; Bellar,  T.A. ; Caldwell, J.K. ;  Kropp, K.L.; Robeck, G.G.;
 Seeger, D.R.; Slocum,  C.J.; Smith, B.L.;  Stevens, A. A.  National
 Organics Monitoring Survey for halogenated organics.  J. Am. Water Works
 Ass. 67:634-636;  1975.

 Su, C. ; Goldberg, E.D.   Environmental concentrations of some halocarbons .
 Windom, L. ; Duce, R.A.  eds. Marine pollutant transfer.  Lexington, MA:
 Lexington Books; 1976.

 Stanford Research Institute  (SRI).  Estimates of physical-chemical
 properties of organic priority pollutants.  Preliminary draft.
 Washington, DC:  Monitoring and Data Support Division, U.S.  Environmental
 Protection Agency; 1980.
                                  4-32

-------
 Tabak,  H.H.;  Aqave,  S.A.;  J.  Mashni,  C.I.;  Barth,  E.F.   Biodegradation
 studies with  priority pollutant  organic compounds.   Cincinnati,  OH:
 Water Research  Division, U.S.  Environmental Protection  Agency;  1980.

U.S.  Environmental Protection Agency  (U.S.EPA).  Monitoring to detect
previously unrecognized pollutants in surface water.  Washington, DC:
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U.S. Environmental Protection Agency  (U.S.EPA). Data Sheet for results
of Phase I of special monitoring regulations (NOMS) finished drinking
water in 113 U.S. cities.  Washington, D.C.:  Monitoring Data Support
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 Verschueren,  K.  Handbook  of  environmental  data  on  organic chemicals.
 New York, NY:  Van Nostrand Reinhold; 1977.

Wilson,  J.T.; Enkrel, C.G.; Dunlap, W.J.; Cosby, R.L.;  Foster, O.K.;
 Baskxn,  L.B.  Transport and rate of selected organic pollutants  in
a sandy  soil.  Undated manuscript received as personal  communication
from  R.S. Kerr Env. Res. Lab, Ada, OK, U.S. Environmental Protection
Agency;  1980.

-------
                     5.0   EFFECTS AND  EXPOSURES— HUMANS

  5.1  HUMAN TOXICITY

  5.1.1   1 , 1, 1-Trlchloroethane

  5.1.1.1   Introduction

      The  principal  human exposure route  to 1,1, 1-trichloroethane, a vola-
  tile halogenated hydrocarbon, is by  inhalation.  It is also readily ab-
  sorbed from the gastrointestinal tract and via dermal contact.  Although
  anesthetic concentrations of 1,1, 1-tr ichloroethane are capable of depres-
  sing the  central nervous system, this compound has a fairly low toxicity
  due to its rapid and almost total elimination as unchanged 1,1, 1-trichloro-
  ethane.

      Commercial samples of 1,1, 1-tr ichloroethane available in the United
 States contain 3 to 8% by volume of added stabilizers such as p-dioxane,
 nitromethane,  N-methylpyrrole,  butylene oxide,  1,3-dioxolane and secondary
 butyl alcohols (IARC 1979).   The following discussion states,  whenever possible
 whether or not the pure or technical (i.e.,  stabilized)  product was  tested.

  5.1.1.2  Metabolism and  Bioaccumulation

      Absorption and Distribution

      In both man and rodents, 1,1, 1-trichloroethane  is rapidly absorbed
 through the lungs  and gastrointestinal  tract,  and somewhat slower through
 skin  (Stewart  1968,  Tsurata  1975).

     Studies with humans  have demonstrated that between 60-90% of inhaled
 1,1, 1-tr ichloroethane is  rapidly expired  unchanged (Monster 1979, Monster
 £tfll.  1979, Humbert and  Fernandez 1977).  Monster et al.  (1979) reported
 recoveries of  80% and 74% respectively,  following ix"po7ure of human vol-
 unteers  to 382 or 792 mg/m3 1,1, 1-trichloroethane for 4 hours.  Total in-
 dividual uptake was  2.2 times greater with the higher concentration over
 the 4-hour period.   The addition of two 30-minute work periods during the
 4-hour exposure increased uptake 2-fold above that noted with  exposures
 at rest, resulting in elimination of 62% of the inhaled dose.

     Due to a low blood/gas partition coefficient, retention of 1,1,1-tri-
 chloroe thane decreases with exposure time, as a steady state is reached.
 Several _ studies have noted that pulmonary excretion of 1,1, 1-trichloro-
 ethane is a function of both exposure duration and concentration.  Ex-
posures ranged from a single breath inhalation of the compound to an  8-

  Ue        *" ^ "*'* '   ^ reSUltS °f  theSe Studie* are summarized
                °f b°th li£Iuid LI, 1-trichloroethane and its vapor through
             1SQ77SO,^en tem°nstrated ^Stewart and Dodd 1964,  Fukabori   §
           ,  1977, Riihimaki and Pfaffli 1978).   Stewart and  Dodd  (1964)
                                    5-1

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                               TABLE  5-1

             PULMONARY  ELIMINATION OF 1,1,1-TRICHLOROETHANE
                               IN HUMANS
        Exposure
382 or 1163 mg/m  for
  8 hr

382 or 792 mg/m3 for
  4 hr

775 mg/m  for 4 hr with
  two 30 mln. work
  periods      ,

1910 mg/m3 for 1 hr
1910 mg/m  for 7.5 hr
single breath
 Amount of 1,1,1-Tri-
    chloroethane
  Expired  Unchanged
 98% by 8  days
 70-80% by 8 days


 62% by 8 days
820 mg/m- immediately
5.4 mg/m  at 24 hr
         3
1365 mg/m  immediately
44 mg/m3 at 16 hr

44% within 1 hr
                                                         Reference
 Humbert and Fer-
 nandez (1977)

 Monster et_ al.
 (1979)

 Monster et_ al.
 (1979)
Stewart et al,
(1975)

Stewart et al
(1975)     ~~

Morgan et al.
(1972)
                                5-2

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  observed rather slow absorption of 1,1,1-trichloroethane during immersion

  lll^r- ™ V1 thUfS ir° the S°1Vent °r t0piCal -PPlicatlon to the hand,
  ? /   I 30 minutes duration.  Average peak breath concentrations were 117
  5.4 and 3.5 mg/m^, respectively (only 14% of an estimated 820 mg/m3 ex-  '

  posure)  while average, breath concentrations 2 hours post-exposure were

  ii «^J!nJ 1'7*8/m  resPe"^ely,  indicating that amount of absorption
  is related to skin area and duration of contact.   Continuous 30-minute

  ST?77nn  i 3°C* handS VaS estimated to equal a  30-minute exposure to
  fntv I ?-m?^ t  ^compound.   Skin absorption would thus present
  only a limited health hazard according to these results.
  ethan10^* C°TkerS (1976'  197?)  3pplied    (*u       .-trichlo
  ethane (15 ml)  dxrectly to the forearm skin of  human volunteers for 2


  airrr;a.Mf a?f ^1>1/13tJiC!:10r0et:hane W3S quickly detected in exPi"d
  air reaching 16-38 mg/m3 by 2 hours.   Repetition of this procedure for

  l  !T A?,   /I   aT ag? alveolar  air  concentrations of 27 mg/m3 on day

  L^t f ^8!T  °ni  y A*   In an°ther  exPerim*nt, repeated dipping of both
  hands into the  solvent,  7 times per day for 4 days  resulted in blood

  levels of  6-9 ug 1,1,1-trichloroethane/ml by the fifth day.


       Riihimaki and Pf af fli (1978)  examined the absorption of 1,1,1-tri-

                              intact human skin.  Two human volunteers with
1 1 1 trilnr                  exPosed  »  3276 mg/m3 laboratory-grade

     "
                                                                y-gr
 c                        an exposure chamber (15 m3) for 3.5 hours.
 Steady and quantitatively increasing blood concentrations of 1,1,1-tri-

 auink°rf ^ r" nf 6d dUring Percu^neous exposure in contr.it to the

 ?±laM       rSPld a"a,lnment of a stead^ state in blood subsequent to
 inhalation exposure..  Peak blood concentration at 3.5 hours was ^90 ug/1-
                           identical exposures  to  thes    sove«   ncen-



      Pharmacokinetic  studies by various routes of exposure with rats
   brain, kidney  muscle, lung and blood (Stahl et al  1969)  '

          ^-"•s^^s^^
brain at a given exposure concentration, while concentrations in  the
liver were much higher.   Tissue concentrations (especially  in the  Uvert
were much greater (nearly 10 times)  when animals  were exposed to a high
                                  5-3

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air concentration for a short exposure time compared to either a low air
concentration for a short exposure time or a low air concentration for
a long exposure  time  even though total exposures (mg/m^ x hr.)  were the
same.   Exposures ranged from 55 to 54,600 mg/m3 1,1,1-trichloroethane for
durations of 0.5 to 24 hours.  The biological half-life of 1,1,1-trichloro-
ethane in the blood, liver,  kidney and brain was approximately 20 minutes
(Holmberg _et al. 1977).

     Larsby and coworkers (1978)  reported crossing of the blood-brain
barrier by 1,1,1-trichloroethane in rabbits.  The animals were contin-
uously infused at a rate of 7-19 mg/min  intravenously.  A near equili-
brium between blood and cerebrospinal fluid was achieved very quickly.
The rate of elimination after cessation of infusion was rapid during the
first 20 minutes, with the concentration of solvent in the cerebrospinal
fluid appearing to follow the arterial concentration, but at a lower
level.

     Biotransformation and Excretion
                                                         i
     In controlled human studies, approximately 3.5% of the total uptake
is metabolized and excreted in the urine as trichloroethanol or tri-
chloroacetic acid.  Monster (1979) suggests that metabolism takes place
in the liver by hydroxylation to trichloroethanol followed by subsequent
partial oxidation to trichloroacetic acid.  The maximum concentration of
trichloroethanol in the blood and exhaled air after a 4-hour exposure
to 382 or 792 mg/nr* 1,1,1-trichloroethane appeared to occur at about
2 hours post-exposure, and declined rapidly  thereafter with a half-life
of 10-12 hours.  In the post-exposure period, the concentration of tri-
chloroethanol in the blood was approximately 14,000 times greater than
that in mixed exhaled air.  The maximum concentration of trichloroacetic
acid was reached at 20-40 hours after exposure, and decreased exponen-
tially after 60 hours with a half-life of 70-85 hours.  Urinary excretion
of the major portion of trichloroethanol occurred during the first 24
hours, while only about 30% of the trichloroacetic acid was excreted in
the urine by 70 hours.  Some 70 hours after exposure, the amount of tri-
chloroethanol and trichloroacetic acid excreted in the urine represented
only about 2.0% and 0.5%, respectively, of the uptake; of 1,1,1-trichloro-
ethane (Monster 1979, Monster _et^ al. 1979).  Humbert and Fernandez (1977)
observed that urinary excretion of the metabolites continued for up to
12 days following an 8-hour exposure to similar concentrations (382 or
1162 mg/m^) of 1,1,1-trichloroethane.

     Similar findings were reported by Ikeda and Ohtsuji (1972)  for Wistar
rats exposed to 1092 mg/kg 1^C-labelled 1,1,1-trichloroethane for 8 hours.
Urine samples collected for 48 hours from initiation of treatment con-
tained 0.5 mg/kg body weight trichloroacetic acid and 3.1 mg/kg trichloro-
ethanol.  Rats intraperitoneally injected with an equimolar dose of 1,1,1-
trichloroethane excreted essentially the same levels of both metabolites.
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      In summary, absorption of 1,1,1-trichloroethane occurs in both
 humans and animals through inhalation and dermal contact.  However,
 most of the absorbed dose is rapidly eliminated unchanged via the lungs.
 The small percentage retained and metabolized is converted to trichloro-
 ethanol with subsequent conversion to trichloroacetic acid, and excreted
 in urine.  Absorption by the inhalation route appears to be a function
 of duration as well as concentration.  Percutaneous absorption of both
 liquid and vapor 1,1,1-trichloroethane has been demonstrated in humans
 but relative to inhalation exposure,  dermal contact presents a limited
 risk.

 5.1.1.3  Human and Animal Studies

      Carcinogenicity

      Three studies have examined the carcinogenicity of 1,1,1-trichloro-
 ethane — by inhalation in rats and by gavage in both rats and mice
 (Rampy _et al.  1977,  Quast et al.  1979,  NCI 1977).  Poor survival or in-
 adequate duration of study,  however,  render the data from these studies
 inadequate for the assessment of human carcinogenic risk.

      Technical grade 1,1,1-trichloroethane (95%)  stabilized with 3%
 p-dioxane and containing 2% impurities, was administered in corn oil by
 gavage to Osborne-Mendel rats (50 per sex per group)  at dosages  of 750
 or 1500 mg/kg,  5 days/wk for 78 weeks and to  B6C3F1 mice (50  per sex per
 group)  at time-weighted doses of  2807 or 5615 mg/kg,  5  days/wk for 78
 weeks.   Rats were observed through 110  weeks,  mice  through 90  weeks.   A
 slight decrease in average body weight  gain was noted for all  treated
 animals of each species.   Although no statistically significant  increase in
 either the total number of neoplasms  or any specific  type of neoplasm
 was observed in either  group of treated rats  or mice, an abnormally  high
 early mortality,  most probably  from chronic murine  pneumonia,  was  such
 that the number of survivors (3%  treated  rats, 31%  treated  mice were
 alive at termination) render suspect  any  assessment of  carcinogenic
 risk (NCI  1977).                                               6

      Rampy et al.  (1977) and  Quast  et al.  (1979) reported no appreciable
 increase in  tumor incidence  in  Sprague-Dawley  rats  (90-96 per  sex per
 group)  exposed  by inhalation  to 4.7 or  9.5  g/m3 1,1,1-trichloroethane
 6 hours/day, 5  days/wk  for 12 months, followed by an additional 18 months
 of  observation.   No differences in  body weight, terminal organ weight or mor-
 tality were observed. The only reported sign of toxicity was an increased
 incidence  of focal hepatocellular alterations  in female rats at the higher
 dose.  No  appreciable difference in tumor incidence between treated and
 control rats was  evident.  However, the length of treatment was less than
 lifetime  (12 months) and there is a .question as to whether or not the
maximum tolerated dose was used.  These studies,  therefore, do not pro-
vide adequate data on which to base assessment of carcinogenic risk.
                                  5-5

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       Mutagenicity

      _The 1,1,1- isomer was weakly  inutagenic  in Salmonella  typhimurium
  strain TA-100  in an Ames  test, with  or without microsomal  activation
  (.binnnon et  al.  1977) .

      Price  et  al.  (1978)  reported  in vitro transformation  of  F1706
  Fischer rat embryo  cells  to  tumor  producing  cells following exposure to
  1,1,1-trichloroethane.  ^differentiated fibrosarcomas were produced
  at  the  site of  inoculation in newborn Fischer  rats injected subcutan-
  eously  with transformed cells.

      Adverse Reproductive Effects

      No embryotoxic or teratogenic effects were noted in offspring of
 Sprague-Dawley rats or Swiss Webster mice exposed by inhalation to 4.7
 g/m  1,1,1-trichloroethane,  7 hours/day on days 6-15 of gestation.  The
 average number of implantation sites per litter, litter size,  incidence
 °f fp'a1 ""	  fetal  sex ratio,  fetal  body measurements, and the
      Elovarra and coworkers (1979)  noted embryotoxic effects in chick
 embryos subsequent to direct injection of 0.6  to 13.3 ug 1,1,1-tri-
 chloroethane/egg on day 3  or 6 of incubation.   Weight and growth measure-

                    '     ^ ** **      ^ d°SS Whl
 wer   i       °J f T?^'* LD5°  °f  6'7-13'3  yg/e^'  Malformations
 were  increased fourfold  above control  values but  the  lack of  anatomic
 and physiologic maternal-fetal  relationships and  the  ultras ens itivity
 ?Lo  I*  tSSv S?St?m  render  iC UTlsuitab1^  for assessing potential  tera-
 togenic  risks in  humans, particularly  in  view of  negative results  in
 two species  that  possess placentae.

      Other lexicological Effects

      Several comprehensive  reviews are available on the acute and chronic
 aT 1976  ^SH^QT^^r11 1'1'1-trichi— thane exposure  (Aviado et
Jl. 1976, NIOSH 1976a, Walter et al. 1976, Kover 1975,  MRI 1979).  We

   r°rr;w°?iyeliShliSht th°Se —that «
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      Liver and kidney damage have been reported in man but only with
 very high exposures to 1,1,1-trichloroethane.  Unlike the CNS effects,
 however, these changes are irreversible, consisting of actual cellular
 or biochemical damage including increases in weight accompanied by fatty
 changes and hemorrhagic necrosis (NIOSH 1976).  Dornette and Jones (1960)
 found no liver damage (measured as serum transaminase) in subjects anes-
 thetized with 32,760-141,960 mg/m3 1,1,1-trichloroethane for up to 2
 hours, while Aviado j£t al. (1976) report clinically detectable effects
 on the liver with inhalation of approximately 142,000 mg/m3 for 15 min-
 utes.  Exposures of 2730 mg/m3 for 78 minutes caused some signs of ad-
 verse kidney effects,  4900 mg/m3 for 20 minutes produced elevated uri-
 nary urobilinogen and increasing levels from 0-14,500 mg/m3 over 15
 minutes produced red blood cells in the urine and/or a positive urinary
 urobilinogen (Stewart e^ al.  1961).

      Inhalation of 54 to 3000 mg/m  elicited effects on the cardiovascular
 system in humans including bradycardia and hypotension within the first
 few minutes of exposure;  in addition to these effects, various altera-
 tions in electrocardiogram patterns  such as premature ventricular con-
 traction,  depressed S-T  segments and changes in nodal rhythm were pro-
 duced with anesthetic  levels  of 32,760-141,960  mg/m3 for  up to 2 hours
 (Dornette and Jones 1960).

      At least 30 deaths  have  been attributed to 1,1,1-trichloroethane
 from deliberate  or occupational inhalation exposure,  most of  which re-
 sulted from suffocation with  acute edema  and congestion of  the lungs,
 liver,  brain,  kidney and/or spleen  (Stahl et al. 1969,  Caplan et  al.
 1976,  Bass  1970,  Hall  and Hine  1966).   Tissue concentrations  oFTTT,!-
 trichloroethane  were highest  in the  liver followed by brain,  kidney,
 muscle,  lung  and  blood.  Bass  (1970) reported 29 cases of sudden  death
 attributed  to  cardiac  sensitization  to  endogenous catecholamines,  while
 Travers  (1974) noted a death  from cardiac  arrest, all  following inhala-
 tion of  1,1,1-trichloroethane.   Garriott  and Petty (1980) reported three
 fatalities following inhalations of liquid paper solvent  containing 0.4-
 0.7 mg/100 ml 1,1,1-trichloroethane.

     A case of accidental ingestion of 600 mg/kg 1,1,1-trichloroethane
 resulted in initial  signs of CNS depression  and gastrointestinal effects.
 Clinical tests showed no adverse effects on  CNS, ECG, SGPT,  blood urea
 nitrogen, SCOT, hematocrit and hemoglobin, while some kidney and liver
 pathology was suggested by red blood cells and protein in the urine and
 increased serum bilirubin (Stewart and Andrews 1966).

     Limited quantitative data are available concerning any toxic effects
 specifically related to long-term exposure to 1,1,1-trichloroethane by
any route of administration.  Stewart et al.  (1969)  reported normal
clinical chemistry tests  for 11 males after inhalation exposure of 2730
mg/mJ 1,1,1-trichloroethane for 6.5-7 hr/day for 5  days.  Subjective
reports listed some signs or irritation and slight  central nervous ef-
fects resulting from exposure.
                                 5-7

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       No clinically pertinent findings (primarily regarding cardiovascu-
  lar and hepatic effects)  were recorded in an epidemiologic study involv-
  ing  two  adjacent textile plants,  one of which utilized stabilized 1,1,1-
  trichloroethane as a general cleaning solvent.  A total of 151 matched
  pairs of employees were examined.   Employees from the exposed group had
  occupational exposures  to 1,1,1-trichloroethane ranging from 5.5 to 1360
  mg/m^ for up to 6 years (Kramer _et al.  1978).   A study of  health effects
  associated with air concentrations of 30-1660  mg/m3  1,1,1-trichloroethane
  to  170 factory  employees  also  revealed  no existing hazard  (Hervin and
  Lucas 1973).  Maroni et al.  (1977)  reported  no signs  attributed to cen-
  tral  or peripheral nervous system  impairment in 22 factory workers ex-
  posed to air concentrations  between 600 and  5400 mg/m3 for up to 6 years.

       Animal   studies reflect the same general  toxic responses noted in
  humans.   Exposure by various routes, of  administration  to high concentra-
  tions of  1,1,1-trichloroethane in various  species of animals  induces toxic
  effects  on the  central  nervous system,  the cardiovascular  and pulmonary
  systems  and  in  renal and  hepatic tissues  (Parker  e£ al. 1979,  Horiguchi
  and Horiguchi 1971,  Tsapko and Rappoport 1972, Herd et al.  1974, Torkel-
  son et al. 1958,  MacEwen  and Vernot 1974).  In general, the LD50ls  for
  1,1,1-trichloroethane in most species are  in the range of  5,000-12,000
 mg/kg  bw via  oral  intake, and 76,450-98,300 mg/m3 for 3-7 hours via in-
  halation  (MRI 1979) .

      Torkelson  et al. (1958)  found slight  liver and lung pathologv in
 guinea pigs exposed  to 5,460 or 11,000 mg/m3 1,1,1-trichloroethane for
  90 or  30 min/day-  (respectively) for 3 months.  Lung irritation was ob-
 served in guinea pigs exposed to  5,460 mg/m3 for 72 min/day or 11,000
 mg/m  for 12 min/day, both for 69 exposures-  No irritation was evident
.with exposure to the lower concentration for 36 min/day for 69 exposures.

      MacEwen and Vernot  (1974) reported no pathology,  no hematological
 effects, normal  clinical chemistry tests and no liver lesions in dogs
 monkeys, mice and rats with continuous inhalation of 1,365  or 5>460 mg/m3
     i"^1CJ10!0ethanxe f°r  14  Weeks'  Lun8 chan§es (slight congestion in
 one half of the  rats) was observed at both dose levels,  while fatty livers
 and  elevated levels of liver  triglycerides in mice were found only at the
 higher dose.   in addition to these effects seen in the mice,  McNutt et
 al.  (1975) observed microscopic pathology indicated by centrilobular —
 nepatocyte hypertrophy,  focal necrosis and inflammation at  week 10  and
 vacuolization at week 12 with continuous inhalation of  5,460 mg/m3  for
 14 weeks;  these  effects  were  not  apparent at  1,365 mg/m3.

     In similar  studies, Prendergast et  al.  (1967) found no microscopic
 pathology,  some  body weight loss, some leukopenia, normal clinical  chem-
 istry  tests and  some non-specific inflammatory  changes  in the  lungs of
 monkeys,  dogs, rabbits,  rats  and guinea  pigs  exposed to  900-2,457 mg/m3
 1,1,1-trichloroethane continuously  for 90 days  or  14,742 mg/m5 8  hr/day
 5 days/wk for 6  weeks.   Adams  et al.   (1950) reported similar  results for
 these  species  with  exposures  up to 27,300 mg/m3,  7 hr/day,  5 days/wk for
 31-32  exposures.
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 5.1.2   1,1,2-Trichloroethane

 5,1.2.1  Introduction

     Although  very  little  data are  available  concerning toxic,  carcin-
 ogenic, mutagenic or teratogenic  effects  in animals  or humans,  the
 evidence  suggests that  1,1,2-trichloroethane  is  more toxic that its
 isomer, 1,1,1-trichloroethane.

 5.1.2.2   Metabolism and Bioaccumulation

     Available pharmacokinetic data on 1,1,2-trichloroethane  indicate
 that it is  readily  absorbed  from  injection sites,  skin and via  the
 lungs.  Yllner (1971) found  that  greater  than 90%  of an intraperitone-
 al dose of  100-200  mg/kg bw  11+C-labelled  1,1,2-trichlorethane in mice
 was eliminated within 24 hours.   Expiration accounted for  16-20% of
 the administered dose (40% of  which was excreted unchanged, 60% as
 C02), and urinary excretion, for  73-87% of the dose.   Major urinary
 metabolites were S-carboxymethyl  cysteine (29-46%  free,  3-10% bound),
 chloroacetic acid (6-31%)  and  thiodiacetic acid  (38-42%).  Minor met-
 abolites  included oxalic acid,  glycolic acid,  2,2-dichloroethanol,
 2,2,2-trichloroethanol,  and  trichloroacetic acid,  suggesting  metabol-
 ism via formation of chloracetalydehyde.   Only 1-3%  remained  in the
 animal after 3 days; 0.1-2.0% was in the  feces.

     Intraperitoneal injection  of guinea  pigs with 50 yl of pure
 1,1,2-trichloroethane resulted  in rapidly increasing  blood levels  of
 the solvent, reaching a  maximum of  nearly 15 yg/ml at  2  hours,  then
 declining over the  next  10 hours.   Intracutaneous or  subcutaneous  in-
 jection of 50  yl resulted  in a  slower, more even uptake  of the  solvent
 from a depot in or  under the skin,  and a  subsequent slow disappearance
 from blood  (Jakobson et^  al. 1977).

     Rapid dermal absorption of 1,1,2-trichloroethane has been  docu-
 mented for guinea pigs  (Jakobson et_ al.. 1977) and rats  (Tsurata  1975,
 1977).  The compound was detected in the  blood of guinea pigs five
 minutes after  application  of 1 ml of pure  1,1,2-trichloroethane  to the
 skin.  Blood concentrations increased during the first 30 minutes
 post-dosing, peaking at  approximately 3.7 mg/ml.   Blood  levels dropped
 to a minimum value  (^2.5 mg/ml) at  one hour, but  then increased
 steadily  thereafter reaching a concentration of ^5 mg/ml at 12 hours
 (length of observation).  No indications  of blood saturation were
noted during this period.  A second  application at another skin depot,
at the point when blood levels were  at the minimum from the first ex-
posure,  resulted in a distinct short second maximum followed by a sec-
ond minimum and increase (Jakobson e_t al.  1977).   The complex toxi-
cokinetics characteristic of percutaneous application are most likely
due to a local effect on and/or within the skin and not to a systemic
effect.   Jakobson speculates that an increased barrier function of the
skin during the first 1-2 hours post-treatment results in a decreased
                                 5-9

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 uptake  of the  solvent  into  the blood.   With  time,  this  barrier is  over-
 come (presumably  due  to  progressive  skin  damage),  leading to a gradual
 increase  in the blood  concentration  of  1,1,2-trichloroethane.

     Another investigator (Tsurata 1975) calculated an in vivo dermal
penetration rate for 1,1,2-trichloroethane in rats  of 5.6 mg/min/cm2
skin and a percutaneous absorption rate of 17.4 mg/min/cm2 skin.  In an
in vitro, study (Tsurata 1977),  with application of  1 ml solvent to
excised rat skin (3.7 cm2 area),  0.53,  1.56 and 3.04 milligrams of sol-
vent had penetrated the skin by 1, 2, and 3 hours,  respectively.  The
penetration curve  of 1,1,2-trichloroethane consisted of a lag phase
(time period required to establish a steady state diffusion, 0.64 hr)
followed by a steady state phase.

      The  1,1,2- isomer of trichloroethane is also  absorbed via the lungs,
 Wistar  rats exposed by inhalation to 1092  mg/m3  1,1,2-trichloroethane
 for 8 hours excreted 0.3 mg/kg bw each  of  trichloroacetic acid and tri-
 chlorethanol in their  urine during,  and up to  40 hours  after exposure
 (Ikeda  and Ohtsuji 1972).   An equimolar dose given by intraperitoneal
 injection (370 mg/kg bw) resulted in similar urinary levels (0.4 mg/kg
 bw TCA  and 0.2 mg/kg bw  trichloroethanol)  (Ikeda and Ohtsuji 1972).

      Van  Dyke  (1977) reported 9.3% enzymatic dechlorination of 1,1,2-
 trichloroethane in vitro by rat  Liver microsomes.   Dechlorination  was
 maximal in the presence  of  02 and required NADPH;  in a nitrogen
 atmosphere, dechlorination  was reduced  to approximately 1/3 - 1/2  the
 rate under aerobic conditions.

      In summation, ready absorption  of  1,1,2-trichloroethane from  skin,
 lung and  injection site  has been  demonstrated  in laboratory animals.
 An in vivo dermal absorption rate of 17.4  mg/min/cm2 had  been  calculated
 for the rat.   Prolonged  dermal contact  results in  a complex pharmaco-
 kinetic pattern in guinea pigs which may  reflect increased absorption
 over time resulting from progressive skin  damage.   Once absorbed,  1,1,2-
 trichloroethane appears  to  be rapidly cleared  in the urine of  rats and
 mice.  Major urinary metabolites  identified  in mouse urine include S-
 carboxymethyl  cysteine,  chloroacetic acid  and  thiodiacetic acid.   Small
 amounts of trichloroethanol and  trichloroacetic  acid are  also  present.

 5.1.2.3  Human and Animal Studies

      Carcinogenicity

      Osborne-Mendel rats (50 per  sex per  group) were fed  technical grade
 1,1,2-trichloroethane  via stomach tube  at  time-weighted doses  of 46  or
 92 mg/kg, 5 days/wk for  78  weeks,  followed by observation until
 week 113.  No  increased  incidence of tumors  or appreciable differences
 in weight gain patterns, appearance  or  behavior were observed.  Survi-
 val was such that adequate  numbers of rats in  all  groups  were  at risk
 from late-developing  tumors (NCI  1978).
                                  5-10

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      In  a separate  experiment,  B6C3F1 mice  (50  per sex per group)  were
 fed  technical  grade 1,1,2-trichloroethane via stomach tube at  time-
 weighted doses of 195  or  390 mg/kg,  5 days/wk for  78  weeks with
 observation  until week 91.  A highly  significant increased incidence
 of hepatocellular carcinoma  was  observed in  all mice treated  with
 1,1,2-trichloroethane  (see data below).  A  positive association between
 the  incidence  of pheochromocytoma of  the adrenal gland and 1,1,2-tri-
 chloroethane exposure  was  also  noted.  Adrenal  pheochromocytomas were
 found in 17% (8/48)  of high dose  males and  28%  (12/43)  high dose fe-
 males, but not in low  dose groups or  controls (NCI 1978).
          TABLE  5-2    INCIDENCE OF HEPATOCELLULAR  CARCINOMA
                       IN B6C3F1 MICE FED  1,1,2-TRICHLORO-
                       ETHANE FOR  78 WEEKS
         Group                       Male                  Female
Vehicle Control                2/10  (10%)             0/20  (0%)
Low Dose  (195 mg/kg/5 days/   18/49  (37%) p=.022     16/48  (33%) p-.002
          wk)
High Dose (390 mg/kg/5 days/  37/49  (76%) p<.001     40/45  (89%) p<.001
           wk)

Source:  NCI  (1978)


     Mutagenicity

     A negative mutagenic response was noted with 1,1,2-trichloroethane
(8 mg/plate) in a plate assay with Salmonella typhimurium strain TA1535
in the presence or absence of a microsomal activation system (Rannug
et_ al. 1978).  No other data were found concerning possible mutagenic
effects of 1,1,2-trichloroethane.

     Adverse  Reproductive  Effects

     The embryotoxic effects of 1,1,2-trichloroethane on chick embryos
was studied by Elovarra and coworkers (1979).  Concentrations of 0.6
to 13.3 ug of 1,1,2-trichloroethane/egg were injected directly in the
air sac on day 3 or 6 of incubation.  A clear dose-response relation-
ship with respect to survival of the embryos at day 14 was noted re-
gardless of the day of treatment.  An approximate LDso value of 6.7-
13.3 wg/egg was obtained.  Measured weight and growth for live  em-
bryos,  however, were affected only at the highest dose (13.3 yg/egg).
Macroscopic malformations including exteriorization of visera,  skeletal
and eye abnormalities and profound edema were increased twofold above
controls at doses of 0.6 to 13.3 ug/egg.  The lack of anatomic and
physiologic maternal-fetal relationships and the resultant ultrasensi-
tivity of this system, however,  render it unsuitable for assessing  po-
tential teratogenic risks to humans.

                                 5-11

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       No additional information was available concerning potential ad-

       oIthane?CtiVS ^^ aSS°ciate

       Other lexicological Effectjs
    _   Reports  in  the  literature  have  linked  acute  exposure  to  1  1  2-
  trichloroethane  with central nervous  system effects  in mice,  kidney
  necrosis  in mice (0.17 ml/kg ip) and  dogs  (0.4 ml/kg ip) and  liver
  necrosis  in both mice and dogs  following intraperitoneal injection  of

                   8       " 3nd Plaal966> 1967> Plaa an
 skin ofi applicati°n °f °'5 to 2 ^ of 1,1,2-trichloroethane to the
 SKin of guinea pigs resulted in the death of 30 to 75% of the animals
 within one week  (Wahlberg and Boman 1979).  In another study, dermal
 application of 1 ml of the solvent to the skin of guinea pigi produced
 effects within 15 minutes (pyknotic nuclei in epidermal cells with
 perinuclear edema in basal cells).  After 30 minutes, epidermal sep-
 aration from the cerium and vesicle formation was evident, while with-
 in 1-12 hours all layers of epidermis showed cellular degeneration.
 Damage was localized exclusively to the epidermis (Kronevi et al.  1977)

     In humans, a narcotic action and irritant effects of eyes and
mucous membranes of the respiratory tract are noted following exposure
to  low  concentrations of 1,1,2-trichloroethane.   It  produced cracking
and erythema when in contact with the skin.   Long-ter^exposure to the
   t,                 gaStric S^P<^,  ^t deposition
   the kidneys and damage to the lungs (Hardie 1964).   The lowest
reported oral lethal dose in man is 50 mg/kg (RTECS 1980).

      No case reports  or  epidemiological  studies were available with
 regard to  human  exposure to 1,1,2-trichloroethane.
 5.1.3   Overview
 5.1.3.1  Ambient Water  Quality Criteria — Human Health

     The  U.S. EPA  (1980a) has established a water quality criterion for
 1,1,1-trichloroethane of 18.4 mg/l for the maximum protection of human
 health.   The criterion  is based on reduced survival noted in Osborne-
 Mendel  rats administered 750 mg/kg of this compound by gavage, 5 days
 per week  for 78 weeks (i.e. 536 mg/kg/day) (NCI 1977) .  Assuming a 70 kg
 body weight and a  safety factor of 1000, an acceptable daily intake
 UDI) of  37.5 mg/day was calculated.  The criterion level of 1 1 1-
 trichloroethane for drinking water, corresponding to  this ADI,'is 18 4
 m/l.
                                 5-12

-------
       For  the maximum protection of human health from potential carcino-
  genic effects of  exposure  to  1,1,2-trichloroethane  through ingestion of
  water and contaminated aquatic organisms,  the U.S.  EPA  (1980a) has  set
  the ambient water concentration at zero.   The concentration of 1,1,2-
  trichloroethane calculated  to keep lifetime cancer  risk below 10~5  is
  6 ug/1.   The criterion is based on the induction of hepatocellular  car-
  cinoma in male B6C3F1 mice  given time-weighted average oral doses of
  195 or 390 mg/kg, 5 days per week for 78 weeks (i.e., 139 and 279 me/
  kg/day, respectively) (NCI  1978).

  5.1.3.2   Other Human Effects Considerations

       The widely used industrial solvent 1,1,1-trichloroethane has a
  fairly low toxicity due to rapid and almost total elimination of the
  compound,  unchanged, via the lungs.  Pulmonary elimination appears to
  be a  function of both concentration and exposure duration, with reten-
  tion  increasing with concentration but decreasing with increased expos-
 ure time.   The small amount that is metabolized (^3.5% of an inhaled
 dose)  is converted by the liver to trichloroethanol and trichloroacetic
 acid and excreted in urine.  Urinary clearance has an approximate half-
 life in man of 10-12 hours for trichloroethanol and 70-85 hours for tri-
 chloroacetic acid.  Although inhalation exposure  is most common,  percu-
 taneous absorption of both liquid  and vapor 1,1,1-trichloroethane,  as
 well as exposure via ingestion,  has been demonstrated in humans.

     In laboratory animals,  acute  LD5()'s  range  from 5,000-12,000  mg/kg
 via  oral administration and 75,450-987300 mg/m3 for 3-7  hours via in-
 halation exposure.   Principal  effects of  acute  exposure  in laboratory
 animals are  depression of  the  central nervous system and  disturbances
 in pulmonary and cardiac function,  including sensitization of the heart
                     Subchronic ^halation studies, monkeys, dogs, rabbits,
                                                  ,
v                 14'75° mg/m  8 hours ?er d*y> 5 days per
                                                             >
            7    showed some leukopenia, body weight reduction and non-
 irS iC ±"?1rajto?r changes.  The liver appeared to be most susceptible
 to histopathological changes in guinea pigs and mice.

     No adequate carcinogenicity studies are available for the determi-
nation of carcinogenic risks associated with exposure to 1,1,1-trichloro-
ethane.  In three studies, 1,1,1-trichloroethane caused no significant
increase in tumor incidence in B6C3F1 mice (4010 mg/kg/day by gavage)
           d1 Hra/,S (1°^/kg/day * S-age)  - * P» ue-Dawley ra§t '
             6 hr/day'  5 days Per week for I2 months);  however/poor
             T      I5 Snd lnsufficlent ^ration of study rendered
  er d    n     q     ^ USe ln an assessment  of carcinogenicity.   Fur-
ther data on carcinogenicity and mutagenicity are extremely limited-
           'fd6 I"1*"  ™*™^** ** -entrain (TA^ oTslltnell*
            and in  one mammalian cell transformation assay.  No  terato-
            S  a               l.l.l-trlchloro.th«e expos^e were ob-
                                                                   on
                                 5-13

-------
      At low exposures of 1,1,1-trichloroethane (_< 5460 mg/m3) the primary
 effects in man are psychophysiological, including dose-related impairment
 of perception and coordination and relatively little disturbance in body
 functions.  At anesthetic levels (>43,700 mg/m3), functional depression
 of the central nervous system leading to respiratory or cardiac failure
 are noted.  Acute exposures to high levels of the compound (>5460 mg/m3)
 by accidental contact or abuse, may result in transient kidney and "
 liver dysfunction.  The effects of chronic low-level exposures are not
 Known.

      Data concerning the toxicity,  carcinogenicity,  mutagenicity or
 teratogenicity of 1,1,2-trichloroethane are very limited or non-existent
 particularly regarding adverse effects to man.   However, based on the
 evidence available,  1,1,2-trichloroethane is considered much more toxic
 than its isomer,  1,1,1-trichloroethane.   The greater toxicity of the
 1,1,2-isomer may be  due to  its greater rate of  absorption and slower
 excretion than 1,1,1-trichloroethane.

      Absorption of 1,1,2-trichloroethane has been demonstrated in labor-
 atory animals following inhalation  exposure or  dermal contact.   An in
 vivo  dermal  absorption rate  of 17.4 mg/min/cm 2  has been calculated  fo~r
 the rat.   Prolonged  dermal contact  results  in a complex pharmacokinetic
 pattern in guinea pigs  which may  reflect increased absorption over  time
 SN^s??38*6331^ skin damage.   Once  absorbed, fairly  rapid  excretion
 or  ii-*i7.  of  an absorbed dose  occurs via the  urine,  and 6-8%  of  the ab-
 sorbed  dose  is  expired  unchanged.   Major urinary metabolites  in mice
 are S-carboxymethyl cysteine,  chloroacetic  acid, and thiodiacetic acid,
 and minor  amounts of  trichloroethanol  and trichloroacetic acid.

      Exposure  to  1,1,2-trichloroethane has'been shown to cause central
 nervous system  depression in mice and  damage  to the  liver and kidnev
 in mice and dogs  following single intraperitoneal injections of 0.07-
    c pff' /°Ute  exP°sure in man appears to be characterized by a nar-
         o,^ "n the central nervous system and eye and skin irritation,
               Kidney, lung and gastrointestinal damage may result from
           exposure.
     Data from a study on carcinogenic effects indicated that 1,1,2-tri-
BFl^    fT^ hePatocellular carcinomas and pheochromocytomas in
B6C3F1 mice of both sexes at time-weighted doses of 139 and 279 mg/kg
bw/day administered by gavage.   Carcinogenicity data from a similar
study with Osborne-Mendel rats  were inconclusive.  No adequate data re-
garding mutagenic or teratogenic effects  associated with 1,1,2-trichloro-
ethane exposure have been reported.
                                  5-14

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 5.1.4  Estimates of Human Dose-Response Relationships

 5.1.4.1  1,1,1-Trichloroethane

      Poor  survival  or  inadequate  exposure  duration  render  the  three
 carcinogenicity  studies  conducted with  1,1,1-trichloroethane inadequate
 for  the determination  of carcinogenic risks.   Extremely  limited  teratogenic
 and  mutagenic data  suggest no  teratogenic  effects in  either mice or rats
 exposed to 4780  mg/m3  on days  6-15 of gestation and a weakly positive
 mutagenic response  in  an _in vitro neoplastic transformation assay and a
 single bacterial strain.  The  sole lifetime exposure  data  available for
 estimation of noncarcinogenic  risk are  the NCI (1977) findings of reduced
 survival, most probably  from chronic murine pneumonia, in  Osborne
 Mendel rats administered 750 mg 1,1,1-trichloroethane/kg by gavage,
 5 days/week for  78 weeks  (i.e., 750 mg/kg x 5/7 days  - 536 mg/kg/day).
 An acceptable daily intake (ADI)  can'be calculated  from these data for
 an average 70 kg human adult.  An uncertainty factor  of 1000 was  included
 due  to the limited chronic toxicity data available  for this compound.
 From  these data, an ADI  of 37.5 mg/day was obtained.
    An,    /750 mg/kg  '5/7 days\ /_„ ,  \
           I       innn/ I 70 k§ J     = 37.5 mg/day
           \       J.UUU         / \      /

 5.1.4.2  1,1,2-Trichloroethane

      Introduction

      The potential  carcinogenic risk to humans due  to 1,1,2-trichloroethane
 exposure is estimated  below.

      Ideally, this problem would  be dealt with in two ways:

      1) Various  extrapolation models would be applied to occupational
        vs. ambient* human exposure data (from retrospective studies)
        in order to obtain an approximate dose/response relationship.

      2) These same models would be applied to data from controlled
        experiments on laboratory animals, and the animal dose/
        response relationship would be converted to an estimated
        human dose/response.

      In the first approach, the overriding uncertainty is in the data
 themselves; usually the exposure levels, lengths  of exposure,  and even
 response rates (responses per number exposed)  are "best estimates,"
 and,  furthermore, unknown factors (background effects, etc.)  may bias
 the data.   In the second approach, the data are usually more accurate,
but the relationship between animal and human response rates  must be
 questioned, and at present there is no universally accepted solution to
 this problem.   (In short, in the former case relevant data are  of
 questionable  accuracy, whereas in the latter accurate data are  of question-
 able  relevance.)  If it is possible to perform both analyses and the results
*(or ambient, location A vs.  ambient, location B)
                                  5-15

-------
 corroborate each other, confidence is gained in these results.  If, on
 the other hand, data are not available for one of the analyses and some
 result   is assumed to be better than no result, the analysis must be
 performed based  upon the available data.

     Further complicating the issue is that at present there is no basis
 for judging the relative merits of the various extrapolation models.
 It is impossible to say which, if any, of them is correct.  However, the
models as applied here are believed to be conservative, i.e., tend to
 overestimate the true risk.

     The available data concerning human and other mammalian effects were
discussed in Section 5.1.2.  For 1,1,2-trichloroethane, the only quan-
 titative carcinogenicity data currently available are from an NCI study
on Osborne-Mendel rats and B6C3F1 mice.   The data selected for extrapolation
are listed in Table 5-2.

     Data from a study on carcinogenic effects indicated that 1,1,2-
trichloroethane caused hepatocellular carcinoma in B6C3F1 mice of both
sexes at time-weighted doses of 139 and 279 mg/kg bw/day administered by
gavage.   A relatively minor incidence of pheochromocytomas of the adrenal
gland in the high-dose males and females has not been included.   The test
performed on Osborne-Mendel rats,  also with 1,1,2-trichloroethane by
stomach tube,  yielded negative results (U.S.  EPA 1930a).

     To deal with the uncertainties inherent in extrapolation,  three
commonly used dose/response models have  been applied to the data  in Table 5-3
to establish a range  of potential  human  risk.   The assessment of  potential
human risk based on these models is subject to  important  qualifications:

    •   Though  positive  carcinogenic findings exist,, there  have also
        been negative findings  in  tests with other species  (see above).
        In view of possible  species differences in susceptability,
        phannaco-kinetics, and repair mechanisms,  the carcinogenicity
        of 1,1,2-trichloroethane to humans  is far  from certain.

    •  Assuming that the positive  findings indeed provide  a basis for
        extrapolation to humans, the estimation of equivalent human
        doses involves considerable uncertainty.   Scaling factors may
        be based on a number of variables, including relative body
       weights, body surface areas, and life spans.

    •  The large difference between the typically high experimental
       data and the actual human exposure levels introduce uncertainty
        into the extrapolation from animals to humans.  Due to inadequate
       understanding of the mechanisms of carcinogenesis,  there is no
        scientific basis for selecting among several alternate dose/
       response models, which yield differing results.
                                 5-16

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       TABLE 5-3.  CONVERSION OF CARCINOCENICITY DATA FOR 1,1,2-TRICHLOROETHANE  IN THE
                   MOUSE INTO EQUIVALENT HUMAN DOSES

                                                                                  Percent








V
M
^J

Animal Dose3
(mg/kg/day)
Male 390
Mice 195
0
(vehicle
control)
0
Female 390
Mice 195
0
(vehicle
control)
0
Equivalent
Human Dose^
(mg/day)
1120
560
0


0
1120
560

0
0
Response
37/49
18/49
2/20


2/17
40/45
16/48

0/20
2/20
Percent
76
37
10


12
89
33

0
10
Excess
Over Averaged
Controls
65
26
—


—
84
28

—
—
Source:  NCI (1977)
5 days per week for 78 weeks of a 96-week lifetime.


Human Dose - Animal Dose x Animal Weight  x ( HiHlaJL WelBht
                                                            2/3
(mg/day)     (mg/kg/day)
                                (kg)
Animal Weight'
days
                                                                        ) x
                                                                        ' X
                                                                             96 wks
                                      )

-------
     Calculations of Human Equivalent Doses





                                                    '     "
£c:ss.:f.r£ 1:1; %^s?z> % h™ ^ -1*-  ««

       £ -sas.2: s?s.£ v. ::-
           -.         .      .
introduces an uncertainty of a factor of ten at least.
70 L f'"et      ^A  J10"1 thlS ln'°^«on and assumed body weight! of
From this, a dose of 1 intr/kg/day for a mouse is calculated to be
equivalent to 2.9 mg/day for a human.           -u.uj.ated to be


    Estimation of Response per Unit of Exposure
    P (response at dose x) » 1 -
                           function'  The log-probit model assumes
                  ^^
                           5-18

-------
       For the linear one-hit model,  the equation


            P(x) - 1 -e~Bx,


  where P(x) is the probability of response  to dose x, is solved for the
  parameter B.


       It may be shown that for a  test group subjected to dose x:



                           1 - P
                 1
            B  - - log
     ^e?? *! ^ aVerTage c°ntrol group response and P (x)  is  the  response
     the test group.  We assume that B is given by
            B"  (B*i'  \
                   1      2
  the geometric mean of the BX  from experimental  data, and determine that
             a.       —3
           B - 1 x 10   per mg/day.
                                           ">"«<" <".rc.pt A results
           POO  - * (A + log
 where $ is the cumulative  normal distribution function,  and P(x)  is  the

 -^
      This equation makes  the assumption that the log-probit  dose/

           ^^  ^ U^  Sl°pe With respect to the log-dose.  From
    -      i?V     rd ^T1 distributi°n,  A (the geometric mean of
 individually determined A ) is found to be approximately  equal to

 Tr.L/        e W3S USe* t0 detennine the probability of a response
 at  various concentrations according to the above equation.


     The multistage model with a quadratic hazard  rate function,
                   2
          h(x) » ax  -I- bx + c,
was also fit to the data.   For estimating  the parameters  a  b  and c
a maxamum likelihood method was used, aided by a computer program ^hat

r^TlVTOTx0 foea5rCh f°r C£eabeSt  f2iC-  Zt ~ Su^fS
a - x x iu  ,  b * 1 x 10 Jt  and c 4 8 x 10-2.  Th  probabilitv of
response attributable to dose x is then given by   pr°bablllty of
          P(x)  - 1  -  e"(ax  + bx)
52 2T4S-J1.1S?
                                    5-19

-------
 roughly 1 mg/day.  Further, since P(x) depends heavily on the quadratic
 term in the high dose region, the excess risk predicted by the multi-
 stage model in the low dose (linear) region is significantly below
 the risk predicted by the linear one-hit model.

      No attempt was made to determine statistical confidence bounds for
 any of the three models.  The uncertainties inherent (a)  in choosing a
 dose/response model and (b) in determining a human equivalent dose make
 suspect any further purely statistical analyses  of the data.

      Table 5-4 summarizes the probability (risk)  estimates obtained from
 these three models.   Also included in .the table  are probability (risk)
 estimates  based on the findings  of the CAG (U.S.  EPA 1980a).   The CAG deter-
 mined an upper bound on excess  lifetime probability (risk)  due to
 1>1»2-trichloroethane ingestion  of 5.73 x 10~2 per mg/kg/day  - 819 x
 10-6  per mg/day (assuming a human  mass of 70 kg).   (Table  5-3 shows
 only  one significant digit.)  The  discrepancies  between the CAG proba-
 bility predictions and those derived here arise  from differing assumptions
 about the  data and about human equivalent dose,  from mathematical differ-
 ences in the dose/response models,  and from the  fact that  the CAG uses  a
 95% upper  confidence bound in calculating its  predicted probability.
 Predicted  excess  lifetime probability per capita  is  shown  in  Table 5-4
 for doses  ranging from 1 ug/day  to  100 mg/day.

      According to the  U.S.  EPA's Water Quality Criteria Document  for
 Chlorinated  Ethanes  (U.S.  EPA 1980a),  the maximum  allowable concentra-
 tion  of  1,1,2-trichloroethane in water  to keep lifetime cancer probability
 below 10-3 is  6.0 yg/r,  or about 0.01  mg/day,  assuming a daily water
 consumption  of 2  I/day for  humans.   (Note  that the 6.0 ug/1 figure  is
 based on assumptions about  indirect as well as direct exposure, particu-
 larly on average  ingestion by humans  of fish inhabiting waters at  this
 concentration,  and on  the  concentration in fish arising from  this  con-
 centration in  the water.)   The four dose/response models predict an
 upper bound  for probability foe this concentration and intake between
 roughly  10~7 and  10~5.

     The estimates in Table 5-4 represent probable upper bounds on the
 true probability, since the dose/response models  are believed to be
 conservative, and the estimation of human equivalent dose  is believed
 to be conservative as well.  Note,  however, that  the gap between the
 estimates is large in the low-dose region, so there is a substantial
 range of uncertainty concerning the actual carcinogenic effects of
 1,1,2-trichloroethane.  However,  present scientific methods do not
permit a more accurate or definitive assessment of human risk.
                                  5-20

-------
                     TABLE 5-4.  ESTIMATED LIFETIME EXCESS PROBABILITY OF CANCER IN HUMANS DUE TO
                                 1,1,2-TRlCULOROETllANE ABSORPTION AT VARIOUS DAILY DOSE LEVELS
                                 BASED ON FOUR EXTRAPOLATION MODELS3
I
N)
Extrapolation F.*P««,,r.M,««l ~ 	 	 :-.u ^.. U/._OU.K^. UL inuicateu Exposure Levels
Model (mg/day): 0.001 0.01 0.1 1 in inn
Linear
Log-Probit
Multistage
CAG
1 x 10~6 1 x 10 5 1 x 10~4 1 x 10~3 1 x 10~2 1 x 10'1
<1 x 10~8 1 x 10~6 7 x- 10~5 3 x 10~3 4 x 10~2 2 x 10~X
1 x 10"8 1 x 10~7 1 x 10~6 1 x 10"5 2 x 10~4 1 x 10~2
8 x 10~ 8 x 10~6 8 x 10~5 8 x 10~4 8 x 10~3 8 x 10~2
       A range of probability  is given, based on four different dose-response extrapolation models.  The
       lifetime excess probability of cancer represents the increase in probability of cancer over  the
       normal background incidence, assuming that an individual is continuously exposed  to 1 1 2-trichloro-
       ethane at the  indicated daily intake over their lifetime.  There is considerable  variation In the
       estimated risk due to uncertainty introduced by the use of laboratory rodent data, by the conversion
       to equivalent  human dosage, and by the application of hypothetical dose-response  curves.  In view or"
       several conservative assumptions that were utilized (see Section 5.1.4.2), it Is  likely that these
       predictions overestimate the actual risk to humans.                               AiKeiy that these

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5.2  HL7MAN EXPOSURE

5.2.1  Introduction

      Monitoring data presented previously in Chapter 4 indicate that
trichloroethanes are widely detectable in environmental media, including
drinking water and foods.   The fate analysis also demonstrated that the
trichloroethanes may occur in all environmental media — air, water,
soil, and sediment.  As discussed earlier in this chapter, absorption
of trichloroethanes can occur via all exposure routes — ingestion,
inhalation, and dermal contact.,   Therefore, the potential absorption
of the trichloroethanes by these three routes was considered in the
human exposure analysis.  Both the human effects considerations and
the monitoring data indicate that the assessment of risk for the
trichloroethanes should be conducted for each isomer separately.  There-
fore, exposure routes were considered separately for 1,1,1-trichloro-
ethane and the 1,1,2- isomer.

5.2.2  Exposure through Ingestion

     Data presented previously in Table 4-2 indicate that both isomers
of trichloroethane have been detected in some surface and ground sources
of drinking water.  It is difficult, however, to estimate the level
of exposure to trichloroethanes via drinking water on the basis of the
available data.  In most cases, the concentrations reported were below
the detection limits for the analytic procedures used.  As will be
discussed below, the relative contribution from drinking water to the
total human exposure to trichloroethanes appears to be quite small in
most cases.

5.2.2.1  1,1,1-Trichloroethane

     Coniglio and coworkers (1980) summarized the data on 1,1,1-trichloro-
ethane from federally sponsored surveys of finished drinking water from
surface and ground sources (see Table 4-2).  Their compilations indicated
that approximately 22% of all finished water supplies (both surface
and ground sources) contained detectable levels of 1,1,1-trichloroethane.
The mean concentration in  finished surface-water supply samples where
it was detected was 0.56 yg/1; positive samples from finished ground
water supplies had a mean concentration of 2.1 yg/1,  although the data
base for groundwater is much less extensive than for surface water.
The EPA STORET data presented previously in Table 4-4 indicate that most
quantified samples (14% were quantified) from ambient U.S. water supplies
were in the 1-10 yg/1 interval.  From these data (Coniglio et jd. 1980,
U.S. EPA 1980b), one can make a rough approximation that about 20% of
the population may be exposed to 1,1,1-trichloroethane in their drinking
water at levels greater than 1 as/l, and in isolated cases subpopulations
may be exposed to levels greater than 10 yg/1.  It should be noted that
this estimate of the size of the exposed population is at best a very
rough approximation since there is wide variation in the size of water
supplies, and it is not likely that the available monitoring data for

-------
 trichloroethanes constitute a representative sample, by size, of the
 total U.S.  water supply.

      The above estimation would also indicate that  the major portion of the
 U.S. population, i.e., about 80%, might be exposed  to 1,1,1-trichloro-
 ethane In drinking water at levels below detection limits.   Detection
 limits vary considerably depending upon the survey, but it is inferred
 from the data of Coniglio and coworkers (1980),  the STORE! data (U.S.
 EPA 1980b)  and Brass (1981) that the detection limits range between
 0.1 yg/1 and 1 yg/1 for most surveys.

      Thus,  for purposes of this study,  it is estimated that some 20%
 of the U.S.  population may ingest greater than 2 yg/day of 1,1,1-
 trichloroethane via drinking water,  assuming ingestion of 2 liters  of
 drinking water per day (ICRP 1974).   The remaining 80% of the population
 would, therefore,  ingest less than 2 yg/day in drinking water.   These
 values are  given in Table 5-4.

      A single study by McConnell e_t  al. (1975)  reported levels  of
 1,1,1-trichloroethane  measured  in various foods  (see Table  4-7).  These
 data are from Great Britain and may  not be representative of  levels in
 food in the  U.S.   Nevertheless,  these data were  utilized to estimate
 the potential exposure to 1,1,1-trichloroethane  from food.  The quantity
 of each food or food group  normally  consumed,  as  cited by the USDA  (1980),
 was used to  estimate daily  intake as shown in Table 5-4,   The estimated
 amount of 1,1,1-trichloroethane ingested  in food  could be perhaps
 2.8 yg/day.

 5.2.2.2  1,1.2-Trichloroethane

      The  monitoring  data  for  the  trichloroethanes in water  distinguish
 in some cases between  the two isomers,  but  the data  showing positive  and
 quantifiable  amounts of 1,1,2-trichloroethane are few.  Results of
 available studies indicate  that  the  isomer is not pervasive at  concen-
 trations  above  detection  limits (VL.5  yg/1).

      Coniglio et al. (1980) reported  on findings for ground water supplies
 in  New  Jersey, which indicated that median levels for both isomers
were  less than 1 ig/1;  the maximum level of 1,1,2-trichloroethane, however,
was over 100 yg/1 (actual values not  given).  Levels of the 1,1,2- isomer
in well water from Long Island's Nassau County were  as high as  310 ug/1.
These maxima are thought to be very  atypical  of U.S. water  supplies because
there is limited use of the 1,1,2- isomer, much of it in captive processes.
The materials balance for 1,1,2-trichloroethane also indicates that
relatively little is released into the environment (see Chapter 3.0).

     No data are available concerning levels of 1,1,2,-trichloroethane
in food.
                                   5-23

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 5-2.3  Exposure  through Inhalation

 5.2.3.1  1,1, 1-Trichlo roe thane

      Atmospheric monitoring data, provided in detail in Table 4-la,
 indicate the ubiquitous presence of 1,1,1-trichloroethane in air.
 Urban air clearly contains higher concentrations than most rural and
 remote areas that have been monitored.  Concentrations in air near
 producers and users of 1,1,1-trichloroethane tend, to be higher than
 in urban areas and show wide fluctuations.

      In order to estimate inhalation absorption of trichloroethanes
 a respiratory retention of 50% was assumed (Riihimaki and Pfaffli
 1^78, Lapp etal.  1979).   The breathing rate was taken to be 22.4
 m /day (1.2 mj/hr  for 16  hours falling to 0.4 m3/hr while asleep.)
 (ICRP 1974).  In the following discussion it will become evident that
 inhalation absorption contributes the majority of the total daily dose
 of 1,1,1-trichloroethane and thus proximity to major sources  of air
 emissions have  been taken  as a basis for depicting four comprehensive
 exposure  scenarios  as follows:

 1)  Rural Remote -  air concentration data for seven  areas  of  the
     United States considered to represent "background"  (see Table 4-la)
     average about 0.5 yg/m3.   There  is little variation,  ranging  from
     a mean of 0.37  ug/mj for White Face Mountain,  N.Y.  to  0.598 ug/m3
     for Point Arena,  CA.   The.  coefficient of  variation  (- - x  100)
     for all of  these  remote  areas was  only about  10%.   Tout?  the
     average inhalation absorption in rural/remote areas of the  U.S.
     is estimated to be about 6  ug/day  and  may range  from an average
     of 4.1  ug/day to  6.7 ug/day  depending  upon local  conditions.

 2}   Urban -  air  concentration data presented  in Table 4-la indicated
     that most urban air concentrations are considerably higher than
     rural axr concentrations.  The data  for seven cities from the
     survey by Singh et al. (1979,1980) is  the most: recent - averaging
     3.3 ug/m->.  This value was taken as a representative mean urban
     air concentration.  The range of mean urban air concentrations of
     J J    .r-oroethane atsor near ground level from various U.S.
    cities is from 0.55 ug/mj for Delaware City, DE  to highs of
    27 ug/mJ for Claremont, CA.  A wide range of potential exposure
              *              by the high coeffi'ient °f variation of
    about 60% for the air concentration data.

       _  Thus,  the typical inhalation absorption of urban dwellers is
    estimated to be 37 ug/day and may range  from 6 ug/day to 300 ug/day
    depending upon the urban area.                                     y

3)   Near  Producers and Users - air concentrations  show extremely wide
    fluctuations,  probably caused by variations  in emission  rates and
    local meteorological  conditions.   A representative mean  could not
    be estimated from the available  data.  As an approximation  of a
                                5-24

-------
       level  to which  this  subpopulation  could  be  exposed  on  a
       continuous basis,  the mean  of  the  high values  and mean of
       the  low values  were  taken,  i.e., 1.8-200 ug/m3,  giving an
       estimated range of potential inhalation  absorption  of  20-
       2200 ug/day.  Estimates of  inhalation absorption given by
       Lapp et al.(1979)  for persons  living near user/manufacturing
       sites  generally fall within the range calculated here.

  4)   Occupational -  a fourth scenario is presented  for contrast,
       Occupational exposures to 1,1,1-trichloroethane  were analyzed
       at the OSHA standard and over  a range of  observed concentra-
       tions in the workplace in order to provide a basis  for
       comparison with the environmental exposure scenarios.  The
       standard set by OSHA for the 1,1,1-isomer is 350 ppm (1900
      mg/m3) as a time-wighted-average (TWA) for the 40-hour
      work week (NIOSH 1976).  NIOSH (1976) reports that  the air
      levels in occupational settings range from 5.4 mg/m3 to
      2200 mg/m3.   The estimated absorbed dose via inhalation
      at the TWA is 9,100 mg per 8-hr,  work day.

      One of the uses of 1,1,1-trichloroethane is as part of the
 propellant gas in aerosol cans,  especially those for paint products.
 About 5,670 kkg/yr were estimated as actual atmospheric releases
 from this application (Chapter 3.0).  There are,  at present, no
 data to indicate  levels of 1,1,1-trichloroethane in the air in the
 immediate vicinity during or after the use of such aerosol cans.
 Without such data,  it is not possible  to estimate actual exposure
 levels.  These exposures would presumably be  short-term and  would
 affect only small  non-occupational subpopulations.

      The results  of the calculations of exposure for each of the four
 scenarios are summarized in Table 5-5.


5.2.3.2  1.1.2-Trichloroethane

     Available monitoring data for 1,1,2-trichloroethane, which are
detailed in Table 4-lb,  indicate  that an average air concentration
in an  urban environment  is about 0.12 ug/m3.  The highest value reported
was a mean of 0.23 ug/m3 in Riverside,  CA. and  the lowest reported 0.04
Ug/m   for Oakland,  CA.   It is unclear how representative  these cities
are for all U.S. cities  since no other data  were available.   On
the basis of these data, the inhalation absorption of 1,1,2-trichloro-
ethane for urban inhabitants is estimated to average 1.3 ug/day and may
range from 0.45 ug/day to 2.6 ug/day.  These results are presented in
Table 5-6.
                                  5-25

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                        TABLE 5-5.  ESTIMATED DATLY HUMAN EXPOSURE TO 1,1,1,-TRICIILOROETHANE
ROUTE

INGESTTON
  Drinking Water

  20% U.S. population
  80% U.S. population

  Food Stuffsb
Observed Concentration
Mean     	Range
  Meat
  Oils and Fats
  Fruits and Vegetables
  Bread
  Teac

INHALATION**
  Rural/Remote
  Urban
  Near User/Producer

  Occupational
  Percutaneous (Occupational)

  Liquid (both hands)
  Vapor
                                                                Exposure Rate or Intake
                                    (fc/day)
    Exposure
Typ Leal    Range
_
-

^
_
—
—
-
(
0.5
3.3
-

1900

j_f
—
	 	 . — .---. .....i. — J.. ** — -^-
<1
(Mg/kg)
3-6
5-10
1-4
2
7
,m/m3)
0.37-0.60
0.55-27
1.8-200
(mg/m )
5-2200

_
5-2200
2
2
(g/day)
207
8
343
62
28
(m3/day)
22.4
22.4
22.4

9.6
hrs./day
0.08-0.2
8
                                                                     >2
                                                                     <2
                                                             0.6-1.2
                                                             0.04-0.08
                                                             0.3-1.4
                                                             0.1
                                                             0.0006
                                                            (p g/day)
                                                           6  4.1-6.7
                                                          37     6-300
                                                               20-2200

                                                           (mg/day )

                                                          9100  24-10600
                                                               13-460
                                                               0.03-13
a) Based on selected data from Table 4-2.
b) Based on data from McConnell ejt al. 1975 (Table 4-7) and food consumption data from USDA  (1980)
c) 20 grams tea leaves per 227 g tea was assumed.
d) Based on selected data from Table 4-la.  A respiratory retention of about 50% was assumed  (see  text).
e) Based on findings of Riihimaki and Pfaffli (1978) and Stewart and Dodd (1964).  Calculations discussed in text.

-------
                  TABLE 5-6.  ESTIMATED DAILY HUMAN EXPOSURE TO 1,1,2-TRICHLOROETHANE



Exposure Rontie           Observed Concentrations




01
N>
Mean Range
Ingestion Mg/1
Drinking Water
- Ground <1.0 <1-300 *a>
Foodstuff No data
3
Inhalation Mg/m
Urban Areas 0.12 0.04-0.23
Rural Areas No data

Typical Range
2 I/day - ND(<3)
2 I/day <2 <2-600
No data
22.4 m3/day 1.3 0.45-2.6

 Data from New Jersey  and Nassau  County  wells  only.   These data are not believed to be representative
 of widespread conditions although  no other data were found.

-------
5.2.4  Percutaneous_Exposure

5.2.4.1  1,1,1-Trichloroethane

     Human experimental data demonstrated that percutaneous absorption
of both vapor and liquid 1,1,1-trichloroethane can occur,  (see Section
5.1.1.2), although these exposures would occur primarily in occupa-
tional settings.   The data of Riihimaki and Pfaffli (1978)  indicate that
absorption of 1,1,1-trichloroethane vapor would be slow, even at high
concentrations.   These authors found that at a concentration of 3,263 mg/m3,
an absorption rate of 2.1 mg/hr was observed for 1,1,1-trichloroethane
vapor across the total body surface (1.8 m^) of human volunteers.  Utiliz-
ing the Riihimaki and Pfaffli (1978) data, a permeability factor of
0.0004 m3/(m2xhr) was calculated for human skin with 1,1,1-trichloro-
ethane vapor.  [Absorption rate (mg/hr) » concentration (mg/m^) x surface
area (m2) x permeability (m^/m^ •  hr)].  Utilizing this factor, the
absorption rate across the unprotected  total body surface area at the
time-weighted average occupational standard of 1900 mg/m^ would be approxi-
mately 1.4 mg/hr or 11 mg/work day.

     Dermal absorption of liquid 1,1,1-trichloroethane can be very
rapid because it dissolves the fat out of the skin aiaking the skin very
permeable.  The experiments of Stewart and Dodd (1964) indicated that
immersion of both hands in 1,1,1-trichloroethane for 0.5 hour was
approximately equivalent in terms of absorbed dose to inhalation of
vapors at concentrations between 546 pg/m3 and  7730 ug/m3.  Assuming a 50%
respiratory retention (Riihimaki and Pfaffli 1978, Lapp e_t al. 1980)
and a respiratory rate of 0.6 m3/hr (sedentary rate) (ICRP 1974), the
initial absorption rate from both hands is estimated to be between
160-2300 mg/hr.   If dermal absorption occurs in certain occupations,
it is thought to be short duration, sporadic, and to occur to a small
subpopulation of workers.  Table 5-5 presents an estimate of potential
absorption of the 1,1,1- isomer in the occupational setting for compara-
tive purposes.

5.2.4.2  1,1,2-Trichloroethane

     Percutaneous absorption of either vapor or liquid 1,1,2-trichloro-
ethane presumably could occur to approximately the ssame extent as for
the 1,1,1- isomer.  More limited use of the 1,1,2- Isomer and a much
lower TWA (10 ppm or 54 mg/m3) imply that occupational absorption
via the  dermal route is not likely to occur to a significant degree.
                                 5-28

-------
  5.2.5   Total  Exposure  Scenarios

  5.2.5.1  1,1, 1-Trichloroe thane

      Table  5-7 estimates  total absorption  of 1,1,1-trichloroethane for
  three  general  population scenarios  and  for an occupational  scenario.
  For  the urban  scenario, inhalation  is the  major  route  of  exposure  to
  1,1,1-trichloroethane.  As  indicated in Tables 4-la  and 5-5,  the range
  of concentrations and, therefore, of estimated daily absorbed dose, is
  from 10 yg/day  to 300  yg/day via inhalation alone.   Approximately  74%
  of the  U.S. population (150,000,000 based  on the 1970  census)  is
  estimated to be exposed at  these levels  (U.S. Bureau of the Census  1979).

      For the rural scenario, inhalation  is  still the major exposure route,
  although ingestion is  estimated to contribute about  one-third  of the
  total estimated exposure of 9 yg/day.   This  level of exposure  is
  estimated to apply to  26% of the U.S. population or  54 million people.

      For the scenario  considering persons who live and work near sites
 where 1,1,1-trichloroethane is manufactured or used, the range of
 potential total absorption was estimated to be between 20 yg/day and
 2200 yg/day.  Inhalation was again the predominant exposure route.
 The size of this subpopulation was not estimated, although it could be
 quite large given the widely distributed use of 1,1,1-trichloroethane
 as a degreasing agent.

      In contrast,  occupational exposure  to  1,1,1-trichloroethane  is
 estimated  to be at least one thousand  times greater  than in  the urban
 scenario.   Again,  inhalation absorption  is  probably  the most significant
 contributor  to  total  daily dose, although percutaneous  absorptio'n rn^y be
 quite high  for  that small  subpopulation  of  workers who  use 1,1,1-trichloro-
 ethane  without  appropriate protection for their hands.  At the  OSHA
 belllOO »!   r  HPPm °I  ^?°  mg/m ' inhalation Absorption is estimated to
 be 9100 mg per  day.   As discussed in Section 5.1  (see Table 5-1)  at
 least 602, and  as  much  as 98%, may be rapidly excreted  unchanged 'via
 exp ir ed  air.

 5.2.5.2  1,1, 2-Trichloroethane
in TaM           detail6^ in Tables 4~lb a*d 4-2 have been summarized
in Table 5-6.  Exposure of populations through contaminated water
^n^- %r!   bly/Stimated °n the basis of the Bailable data.  Certain
contaminated ground sources, notably in New Jersey and Long Island
suggest that for an unknown subpopulation, exposure through drinking
water may be significant.

     Consistent with the monitoring data for the 1,1,1- isomer and with
considerations of the fate of the trichloroethanes  inhalation is
thought to be the major daily exposure route.   On the basis of rather
                                  5-29

-------
     TABLE 5-7  TOTAL EXPOSURE SCENARIOS FOR 1,1,1-TRICHLOROETHANE
                          Estimated Daily Absorbed Dose (Ranee)
Route              ^ban        Rural        Near Sites        Occupational



Ingestion




  Water         <2yg            <2yg         <2yg             <2yg




  Foodstuff      3yg             3yg          3yg              3ug






Inhalation      37 (6-300)yg     6 (4-7)yg    - (20-2200)ug    - (24-10,600)n






Percutaneous        -	       -          -	0.03-460 mg




       Total    42 (ll-3C5)ug   11 (9-12)yg  >25  (25-2205)ug   - (27-11,000)u
                                 5-30

-------
limited air monitoring data for some large cities, the average daily
absorbed dose from inhalation is estimated to be 1.3 yg/day, with a range
of 0.45-2.6 ug/day.  Since the majority of urban inhabitants receive
their water from surface sources and the monitoring data available
suggest that the 1,1,2- isomer is not detectable in most surface
supplies, the total daily dose has been taken to be given by the
inhalation dose.  This level of exposure may involve 74% of the
U.S. population or the 150,000,000 urban inhabitants (U.S. Bureau of
the Census 1979).
                                 5-31

-------
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 Publication No.  (NIH) 77-303; 1977.  70 p.

 National  Cancer  Institute  (NCI).  Bioassay of 1,1,2-trichloroethane for
 possible  carcinogenicity.  Carcinogenesis.  Technical Report  Series NO. 74.
 CAS No. 79-00-5.  NCI-CG-TR-74.  U.S. Department of Health Education and
Welfare.  Public Health  Services.  National Institutes of Health.  Publication
No.  (NIH) 78-1324; 1978.  48 p.
National Institute for Occupational Safety and Health (NIOSH).   Criteria for
recommended standard—occupational exposure to 1,1,1-trichloroethane
(methyl chloroform).  NIOSH, U.S. Department of HEW, DHEW Publication No.
NIOSH 76-184.  179 pp.; 1976.  (As cited in MRI 1979.)

Parker, J.C.; Casey, G.E.; Bahlman, L.J.; Leidel, N.A.; Rose, D.; Stein,
H.P.  Chloroethanes:  review of toxicity.  NIOSH Current Intelligence
Bulletin #27.  Am. Ind. Hyg. Assoc. J. 40:A-46-A-60; 1979.
                                 5-35
a

-------
  Plaa,  G.;  Evans,  E.;  Hine,  C.   Relative hepatotoxicity of seven
  halogenated hydrocarbons.   J.  Phannacol.  Exp.  Ther.  123:224-229-  1958
  (As  cited  in Aviado  1977,  IARC 1979).                           '

  Plaa,  G.L.;  Larson,  R.E.  Relative  nephrotoxic properties of chlorinated
  7n?a^'//ethfo! = and,ethylene derivatives  in mice.  Toxicol.  Appl.  Pharmacol.
  /U;: 37-44;  1965.   (As  cited in MRI 1979,  IARC 1979).

  Prendergast,  J.; Jones, R.A.;  Jenkins,  L.  Jr.;  Siegel,  J.  Effects on
  experimental  animals  of long-term inhalation of  trlchloroethylene
  carbon tetrachloride, 1,1,1-trichloroethane, dichlorodifluoromethane,  and
  1,1-dichloroethylene.  Toxicol. Appl. Pharmacol. 10:270-289-  1967
  (As  cited  in  MRI 1979.)                                          '

  Price,  P.J.;  Hassett, C.M.; Mansfield, J.I.  Transforming activities  of
  trlchloroethylene and proposed  industrial  adternatives.   In Vitro
  14:290-293; 1978 (As cited in EPA 1979).

  Quast,  J.F.;  Rampy, L.W.;  Balmer, M.F.; Leong, B.D.J.; Gehring, P.J.
  Toxicological and carcinogenic  evaluation of a 1,1,1-trichloroethane
  formulation by chronic inhalation in rats.  Available from Dow Chemical Co.
 Midland, Michigan 48640.  Preprint written in 1979; 1978.   (As cited in
 MRI 1979.)

 Rannug, U.; Sundvall, A.;  Ramel, C.   The mutagenic effect  of  1,2-dichloro-
 ethane on Salmonella tvphimurium.   I.  Activation through  conjugation with
 glutathion  in vitro.   Chem.  biol.   Interact.  20:1-16;  1978.   (As cited
 fay IARC 1979.)

 Rampy,  L.W.; Quast,  J.F.;  Leong, B.K.J.; Gehring, P.J.   Results of
 long-term inhalation toxicity studies on rats  of 1,1,1-trichloroethane
 and perchloroethylene formulations  (Abstract)  In:  Proceedings of  the
 International Congress of  Toxicology, Toronto,  Canada,  1977,  p.  27-
 1977.  (As  cited in  IARC 1979.)

 Registry of Toxic  Effects  of Chemical Substances  (RTECS);  On  line computer
 search: 1,1,1-trichloroethane;  1,1,2-trichloroethane; July 1980.

 Riihimaki,  V.; Pfaffli,  P.   Percutaneous absorption of  solvent  vapors
 in man.  Scand.  j. Work  Environ, and Health 4:73-85; 1978.

 Schwetz, B.A.; Leong,  B.K.J.; Gehring, P.J.  The  effect  of maternally
 inhaled trichloroethylene, perchloroethylene, methyl chloroform, and
 methylene chloride on  embryonal  and  fetal development in mice and rats.
 Toxicology  and Applied Pharmacology  32:84-96; 1975.

 Simmon, V.K.;  Kauhanen, K.; Tardiff,  R.G.  Mutagenic activity of chemicals
 identified  in  drinking water.   In: Scott, D.; Bridges, B.A.; Sobels, F.H.,
 eds., Progress in Genetic Toxicology, Amsterdam,  Elsevier/North Holland
 pp. 249-258; 1977.
Singh, H.B.; Salas,  L.J.;  Smith, A.;  Shigeish,  H.   "Atmospheric measure-
ments of selected toxic organic  chemicals,  First Year  Interim  Report,"
Research Triangle Park, NC:   Environmental  Sciences  Research Laboratory,
U.S. Environmental  Protection Agency; 1979.

                                5-36

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 Singh,  H.B.; Salas,  L.J.;  Smith,  A,;  Shigeish,  H.   Selected hazardous
 organic chemicals,  Draft Second Year  Interim Report;  1980.

 Stahl,  C.J.; Fatteh, A.V.; Dominguez, A.M.  Trichloroethane poisoning:
 observations on the pathology and toxicology in six fatal cases.  J.
 Forensic Sci. Soc.  14:393-397; 1969.   (As cited in IARC 1979, MRI 1979,
 TSAC 1978, EPA 1979.)

 Stewart, R.D.  Toxicology of 1,1,1-trichloroethane.  Ann. Occup. Hyg.
 11: 71-79; 1968.   (As cited in MRI 1979).

 Stewart, R.D.;  Andrews, J.T.  Acute intoxication with methyl chloroform.
 J.A.M.A. 195:904-906; 1966.  (As cited in MRI 1979, Aviado 1977.)

 Stewart, R.D.;  Dodd, H.C.   Absorption of carbon tetrachloride, trichloro-
 ethylene, tetrachloroethylene, methyl chloride  and 1,1,1-trichloroethane
 through the human skin.  Am. Ind. Assoc. J.  25:439-446; 1964.   (As cited
 in MRI  1979, EPA  1979).

 Stewart, R.D.;  Gay,  H.H.;  Erley,  D.;  Hake, C.;  Schaffer,  A.   Human
 exposure to 1,1,1-trichloroethane vapor: relationship of  expired air
 and blood concentrations to exposure  and toxicity.  Amer.  Ind. Hyg.
 Assoc.  J. 22:252-262; 1961.  (As  cited in MRI 1979, EPA 1979.)

 Stewart, R.D.;  Gay,  H.H.;  Schaffer, A.W.; Erley, D.S.;  Rowe, V.K.
 Experimental human  exposure to methyl chloroform vapor.   Arch.  Environ.
 Health  19:467-474;  1969.   (As  cited in MRI 1979.)

 Stewart, R.D.;  Hake,  C.L.;  Wu,  A.; Graff, A.; Forster,  H.V.; Lebrun,  A.J.;
 Newton,  P.E.; Soto,  R.J.  1,1,1-trichloroethane—development of  a  biologic
 standard for the worker by  breath analysis.  Report No. NIOSH-MCOW-ENVM-
 1,1,1-1-75-4.   University of Wisconsin Medical College, Department of
 Environmental Medicine,  Wisconsin. 102 pp; 1975.   (As cited in EPA 1979
 MRI 1979).   •

 Torkelson,  T.R.; Oyen,  F.;  McCollister,  D.; Rowe, V. Toxicity  of 1,1,1-
 trichloroethane as determined  on  laboratory animals and human  subjects.
 Am.  Ind.  Hyg. Assn. J.  19:353-362; 1958.   (As cited in Aviado  1977, MEI 1979.)

 Travers,  H.  Death from  1,1,1-trichloroethane abuse:  Case report.  Mil.
Med. 139:889-893;  1974.  (As cited in Aviado 1977).

Tsapko,  V.G.; Rappoport, H.B.  Effect  of methylchloroform vapors on
animals.  Farmakol.  Toksikol.  (KIEV)  7:149; 1972.   (As cited in USEPA 1980.)


 TSCA Interagency Testing Committee, Washington, D.C. Second report of the
 TSCA Interagency Testing Committee to  the Administrator, Environmental
 Protection Agency and  Information Dossiers on Substances Designated.
 1,1,1-trichloroethane;  1978.  pp  VIII-3  - VIII-26.  U.S. Department of
 Commerce  National Technical  Information  Service.  No. PB-285-439.

Tsurata,  H.  Ind.  Health 13:227; 1975.   (As cited in Tsurata 1977.)
                                 5-37

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 Tsurata,  H.   Percutaneous absorption of organic solvents.   2)   A method
 for measuring the penetration rate of chlorinated solvents through
 excised rat  skin.   Industrial Health 15:131-139;  1977.

 U.S.  Bureau  of  the Census.   Population and  land area  of  urbanized areas
 for the U.S.; 1970 and  1960.   Washington, D.C.;  U.S.  Department of
 Commerce.  April,  1979.

 U.S.  Department of Agriculture (USDA) .   Food and  nutrient  intakes of
 individuals  in 1  day  in  the United  States,  Spring 1977.  Nationwide
 Food  Consumption  Survey  1977-73, Preliminary Report No.  2.   Science and
 Education Administration, Washington,  D.C.; 1980.

 U.S.  Environmental Protection  Agency  (USEPA) .  Ambient water quality
 criteria for chlorinated  ethanes.  Washington, D.C.:  Criteria  and
 Standards division, Office of  Water Regulations and. Standards;  1980a.

 U.S.  Environmental Protection  Agency  (U.S. EPA).  STORET.  Washington
 DC:   Monitoring and Data  Support Division.  Office of Water Regulations
 and Standards, U.S. Environmental Protection Agency; 1980b.


 Van Dyke, R.A.  Dechlorination mechanisms of chlorinated olefins.
 Environmental Health  Perspectives 21:121-124; 1977,,

 Wahlberg, J.E.; Boman, A.  Comparative  percutaneous toxicity of  ten
Walter, P.; e£ al..  Chlorinated hydrocarbon toxicity (1,1,1-trichloroethane,
trichloroethylene, and tetrachloroethylene) :  a monograph.  PB Rep.
PB-257185.  Natl. Tech. Inf. Serv. , Springfield, Virginia; 1976.  (As
cited in USEPA 1980.)

Yllner, S.  Metabolism of l,l,2-trichloroethane-l,2-14C in the mouse
Acta. Pharmacol.  Toxicol.  30:248-256;  1971.  (As cited by EPA 1979,
IARC 1979) .
                                  5-38

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                6.0  EFFECTS AND EXPOSURE—NON-HUMAN BIOTA

 6.1  EFFECTS ON BIOTA

      This section provides information concerning the levels of tri-
 chloroethanes that cause mortality or disrupt physiological functions
 and processes in aquatic organisms.  Toxicity information for the tri-
 chloroethanes is limited and includes data for only four freshwater
 and three marine species.  Only one study on chronic effects was
 available.

      Both 1,1,1-trichloroethane and 1,1,2-trichloroethane are liquids
 in the ambient temperature range and are soluble enough in water to be
 of potential concern as water pollutants.   No information was available
 on the environmental factors that may influence toxicity.

 6.1.1  Freshwater Species

      Acute toxicity levels in freshwater organisms were determined for
 bluegill (Lepomis macrochirus).  Daphnia magna,  fathead  minnows,  and the
 alga Selenastrum capricomutum.   The lowest concentration at which
 lethal effects occurred was 18.0 mg/1 of 1,1,2-trichloroethane in
 Daphnia.   Toxicity data for freshwater species  are presented in  Table
 6-1.   The highest concentration  tested,  669 mg/1,  did not affect the
 algae (Selenastrum).   A chronic  value of 0.4 mg/1  1,1,2-trichloroethane
 was  determined for the fathead minnow in embryo-larval  tests (U.S.  EPA
 1980).   No other chronic data were available.

 6.1.2  Saltwater Species

      The  acute toxicity data  base  for 1,1,1-trichloroethane  to saltwater
 to organisms  is  limited to  the sheepshead minnow,  mysid  shrimp,  the
 algae Skeletonema costatum. and  barnacle larvae  (Table  6-2). No  data
 on toxicity of  1,1,2-trichloroethane  to marine species were  available.
 The effects of  salinity,  temperature,  or other water characteristics
 are also  unknown.  The  1,1,1-isomer was not  toxic  to Skeletonema at
 the highest test  concentration.

 6.1.3  Phytotoxicity

     The  toxicity of 1,1,1-trichloroetuane to the green freshwater algae
Selenastrum capricomutum and the saltwater algae Skeletonema costatum
were tested, using chlorophyll and a  cell number as indicators of growth.
Both species were relatively tolerant of the compound at the levels
tested.  No acute effects were observed at the highest concentrations
tested, 669 mg/1, for either S.  capricomutum or S. costatum (U.S.  EPA
1980).  No data are available on the effects of trichloroethanes on
vascular plants.
                                 6-1

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             TABLE 6-1.   ACUTE TOXICITY  OF  1,1,1-  AND 1,1,2-TRICHLOROETHANE
                         FOR FRESHWATER  SPECIES
                                                 96-hr
Species Isomer
Fathead minnow 1,1,1-
Pimephales promelas 1,1,2-
Bluegill 1,1,1-
Lepomis macrochirus 1,1,2-
LC (mg/1) Reference
52.8 (FT)1 105. 0(S)2 Alexander _e_t al
81.7 U.S. EPA (1980)
69.7 U.S. EPA (1978)
40.2 U.S. EPA (1978)
Cladoceran
Daphnia magna
           1,1,2-
43.0
Adema (1978)
Species
TABLE 6-2.  ACUTE TOXICITY OF 1,1,1-TRICHLOROETHANE
           FOR SALTWATER SPECIES
                                 96-hr
                              LC5Q(mg/l)          Reference
Mysid Shrimp
Mysidopsis bahia
                              31.2 mg/1
                U.S. EPA (1978)
Sheepshead minnow
Cyrpinodon variegatus
                              70  mg/1
                U.S. EPA  (1978)
Barnacle larva
Flominius modestus
                               7.5 mg/1
                U.S. EPA  (1978)
                                        6-2

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  6.1.4   Biological Fate

      The high  fat solubility and low chemical reactivity of 1,1,1-tri-
  ?«  «f?«?a?e tfldS "  °a^e  bioconcentration; however,  this tendency
  is  offset by the  compound's  high vapor pressure (100 mm at  20°C)
  and  resultant  volatility.  Neither  of the  trichloroethanes  bioaccumulate
  strongly; a steady-state bioconcentration  factor of  9 for 1 1  1-tri-
  chloroethane was  measured for Bluegill.  Based  on  the octanolI water
  partition coefficient  of 117, a  BCF of  22  was estimated  for 1,1,2-tri-
  chloroethane (U.S. EPA 1978,1980).

      In  field experiments where  1,1,1-trichloroethane was detected at
  0.5 jig/1  in water, fish concentrations were found up  to 100  times the
  concentration in water.  No evidence indicated accumulation  through
  food chains, however.  Algae have been found to accumulate 1,1,1-tri-
  4-K   inn  ft            W lfi^  range, at bioconcentration factors less
 labnJLn,  K^— *%' 1979)'   SeCti°n 4'3-3'4 discusses the results of
 laboratory biodegradation tests on the trichloroethanes.  No natural
 biodegradation  of the trichloroethanes has been demonstrated.

 6.1.5  Conclusions

      The lowest level at which adverse effects to aquatic organisms
 have been experimentally determined  for the trichloroethanes is 7.5
 mg/1 for barnacle  larvae.  The most  sensitive  fish  species  tested  is
 the  Bluegill  (69.7 mg/1 for 1,1,1-trichloroethane;  40?2  mg/1 "or 1 1  2-

 in thfrangeTl'mg^trSf'7 T^* ^  ^^  ^ inver^br^^s  ««e
 chloroethanes/ N^acute effeSs^n  a^gae were obseJverin'tes't'con-1"
 centrations up  to  670 mg/1.

 6.2  EXPOSURE OF BIOTA


water^^^viilabirfrom1^613 °f 1>1!1-trichloroethane in nondrinking
sites upstream and dnJ!=4fIf^J!^!1.!3; ,Bftte^1f, (1977? m°nitored
   e   pstdd                                              e
facturers' d^ch   downstream !rom  fiv« 1,1,1-trichloroethane manu-
facturers  discharge points and at  the outfall pipes.  In general
                                                  es.
the results show that the average concentration found in

              11
                                                                 waters
ecforne
n^'    ,.;?,*    W  h an 3Verage °f 132 ug/1 (5° m upstream of the
plant s outfall).  Downstream of the plants, concentrations of 1,1, J!
tnchloroethane were higher than those upstream in all cases  with
average concentrations ranging from a low of 0.8 ug/1 to" high value
of 169 ug/1.  Battelle also sampled a user site, at which 1 1 l-tri^
chloroethane is used for metal cleaning operations.  The highest con-
                                                             "    B
                                 6-3

-------
     The University of Illinois has conducted a study to detect 1,1,1-
trichloroethane in surface water at different sites in the United States.
Of the 204 sites sampled, 95% showed less than 6 ug/1.   Approximately
75% of the sites sampled showed 
-------
                               REFERENCES
Alexander, H.C.   Toxicity of perchloroethylene,  trichloroethylene,
1,1,1-trichloroethane, and methylene chloride to  fathead minnows.
Bull. Environ. Contain. Toxicol.  20:344; 1978.

Battelle Columbus Laboratories.  Determination and evaluation of environ-
mental levels of methyl chloroform and trichloroethylene.  EPA 560/16-
77-030.Columbus, OH:  U.S. Environmental Protection Agency; 1977.

Lapp, T.W.; Herndon, B.L.; Mumma, C.E.; Tippit, A.D.; Reisdorf, R.B.
An assessment of the need for limitations on trichloroethylene, methyl
chloroform, and perchloroethylene.  Washington,  DC : Office of Toxic
Substances, U.S. Environmental Protection Agency; 1979.

National Science Foundation.  Second Report of the TSCA Interagency
Testing Committee to the Administrator, Environmental Protection Agency,
and Information Dossiers on Substances Designated.  Washington, DC
National Science Foundation; 1978.

U.S. Environmental Protection Agency (U.S. EPA) In depth studies on
health and environmental impacts of selected water pollutants.  EPA
68-01-4646 Washington,  DC  :  U.S. Environmental  Protection Agency;
1972.

U.S. Environmental Protection Agency (U.S. EPA)  Ambient Water Quality
Criteria Document for Chlorinated Ethanes.  EPA 400/5-80-02;  Washington,
DC  : Office of Water Planning and Standards, U.S. Environmental Pro-
tection  Agency; 1980.
                                  6-5

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                        7.0   RISK CONSIDERATIONS
 7.1  RISKS TO HUMANS

 7.1.1  1,1,1-Trichloroe thane

     The compound 1,1,1-trichloroethane  does  not  appear  to  present
 carcinogenic risks based on data avialable at  this time.  In addition, no
 positive mammalian mutagenic or teratogenic effects have been demonstrated
 However, if exposure levels are high  enough,  acute or  chronic toxic
 effects may be not.ed.  An acceptable  daily intake (ADI)  of  37.5 mg/day
 has been estimated from findings of reduced survival in  rats (see
 5.1.4.1).  Estimated exposures for urban and  rural exposed  populations
 are considerably lower than the estimated ADI.  Only the estimated
 absorption by the occupationally exposed population is in the range of
 the ADI.
       Exposure Scenario        Estimated Exposure  (absorbed dose)

        Urban Exposure                  42 yg/day

        Rural Exposure                  11 yg/day   ADI: 37.5 mg/day

        Near Sites                25-2,200 yg/day

        Occupational             27-11,000 mg/day
Consequent!*7, urban and rural populations and populations near user and
manufacturing sites appear not to be at risk from chronic exposure to
1,1,1-trichloroethane.  Urban exposures are more than 500 times lower
than the ADI, which has a safety factor of 1000 included.  Rural
exposures are 4000 tines lower than the ADI.  Some of the 130,000 occu-
pationally exposed individuals might be subject to adverse toxic effects
from 1,1,1-trichloroethane since their estimated exposure levels are
similar to the estimated ADI for 1,1,1-trichloroethane.

7.1.2  1,1,2-Trichloroethane

     Because of very limited monitoring data and the consequent limited
exposure estimates developed in Chapter 5.0, only very tentative risk
predictions can be made regarding 1,1,2-trichloroethane.  For the urban
population, the average daily exposure from inhalation alone was estimated
                                   7-1

-------
to be 1.3 ug/day.  Table 7-1 presents the estimated excess lifetime
cancers per million exposed population at this daily dose using four
risk extrapolation models.  If this daily dose of 1,1,2-trichloroethane
can be taken as representative of that experienced by the urban popula-
tion (estimated to be 150 million), the incidence of excess lifetime
cancers in this population is estimated to be between 1.5 and 150 (i.e.,
150 x 0.01 and 150 x 1).

     A small subpopulation may be exposed to much higher levels via
contaminated drinking water from certain groundwater sources.  The size
of this population has not been estimated.  The range of excess lifetime
cancers per million persons exposed to a daily lifetime dose of 0,6 mg/day
in this manner is estimated from the four extrapolation models to be
between 6 and 1,350.  This level of exposure is thought to be extremely
atypical, even though monitoring data are limited.

     There is considerable uncertainty associated with the estimates in
Table 7-1, as considerable controversy exists over the most appropriate
model for performing such extrapolations.  Moreover, additional
uncertainty is introduced into the risk estimates by the choice of a
particular set of laboratory data, by the conversion techniques used to
estimate human equivalent doses, and by possible differences in
susceptibility between humans and laboratory species.  Due to the use
of a number of conservative assumptions in the risk calculations, the
results shown in Table 7-1 most likely overestimate the actual risk to
humans.

7.2  RISK TO AQUATIC BIOTA

     The toxicity data base for 1,1,1- and 1,1,2-trichloroethane is
limited to one invertebrate fish and algal species for both fresh and
salt water.  The lowest level at which adverse effects to aquatic
organisms have been detected in the laboratory is 7.5 mg/1 for salt water
barnacle larvae.  The most sensitive fish species tested is the bluegill
(69..7 mg/1 for 1,1,1-trichloroe thane; 40.2 mg/1 for 1,1,2-trichloro-
ethane) .  All toxicity values for fish and invertebrates ranged from
1.0 mg/1 to 100 mg/1.  Neither of the trichloroethanes bioaccumulated
strongly; a bioconcentration factor of 9 was measured for 1,1,1-tri-
chloroethane (bluegill Lepomis macrochirus), and 22 was estimated for
1,1,2-trichloroethane.

     The monitoring data indicate that the concentrations found
in most major river basin samples and near production and user sites
were in the low ug/1 range.  The highest reported 1,,1,1-trichloroethane
level, detected near a manufacturing site, was 169 yg/1.  Although no
known fish kills or other short-term high concentrations of trichloro-
ethanes have been reported, the possible episodic occurrence of levels
of trichloroethanes greater than 10 mg/1 would be of greater potential
concern than those levels reported heretofore in the monitoring data.
The water quality criteria for trichloroethanes (5300 ug/1 finished
                                  7-2

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                   TABLE 7-1.  ESTIMATED LIFETIME EXCESS PROBABILITY OF CANCER IN HUMANS DUE

                               TO ABSORPTION OF 1,1,2-TRICHLOROETHANE AT DOSES OF 0.6 mg/DAY

                               AND 1.3  ug/DAY ON THE  BASIS  OF  FOUR EXTRAPOLATION MODELS3
                                              Estimated Lifetime Excess Cancer  Incidence

                                              (per million exposed population)3

                                                      Risk Extrapolation Model
                              Absorbed Dose   Linear     Log-Probit      Multistage
GAG
i
OJ
1.3 pg/day
0.6 mg/day
1
600
0.02
1350
0.01 1
6 480
                    dlfferlf ,lncldence is 8iven Per million population exposed, based on four










                                                                      -y «'e  application of

-------
water, 240 ug/1 surface water for 1,1,1-trichloroethane,  310 ug/1 for
1,1,2-trichloroethane) are not exceeded in ambient and effluent waters
in the United States, based on information reported in this document.
Exposure levels and known effects levels do not overlap.  No acute or
chronic effects are known to occur at less than 400 ug/1.  Risk to
aquatic organisms is, therefore,  determined to be negligible on a wide-
spread chronic basis.
                                  7-4

-------
                                APPENDIX A

       NQT£  1;  Total VOC emission ratio from distillation v«nt in
  n1^1uC^1PrideciDrOCeSS = °'19 9/kg of 1,1,1-trichloroethane produced =
  0.19 kg/kkg.  Given a 90% removal efficiency for aqueous scrubbers
  where the VOC emissions are comprised solely of 1,1,1-trichloroethane,
  then 0.17 kg were captured by control devices and sent to water per
  I Kkg of 1,1,1-trichloroethane produced.   The remainino 0.02 kg p°r
  1 k  that which  *^ would
  emit  0.01 kg  VOC/1 kkg of 1,1,1-trichloroethane  produced.  Also  the
  n^fnr^f °^^°? ?f.t!l?  d1st^^tion vent  gases from a model
  TJ^^J^^nlsS'J'i^n^?^?"8,1? ?5%  1.1.1-tnchloroethane.
               .oj  vu •<•'•>• Kg vuL,j/i KKg  1,1,1-trichloroethane produced =
     ^       4;  If 5% of the total VOC wastes are emitted to air
 (derived in note 3), then 95% was captured by glycol pot control
 devices and sent to landfill.  If the air emission ratio =3 0035 kg

 Jhen 8    kl°nr0enhnfln?,e?,;tted/1 ^ °f LU-trlchloroethane producld.
 mPtHr ;? c9 J    ?875 kkg were e™tted to the atmosphere when 25,000
 of 11 1 tr^nr^ ™r* ^'  ^efzre, the ratio of kilograms
              •  ° roethane captured by control  devices per metric >on  Of
                                    ^
as a  semisolid waste
^•if-t-iii j    j u • L r  "-"—"   """  ' ' •'- = ' cu "/ur-utdroon szream is
rl^n  i       high-boiling chlorinated hydrocarbons  (polymers) are
removed as a waste stream.  Alternatively, spent catalyst and
polymeric material may  be removed  in  a single steS by d?stl"laMon
although this simplification is at the expense of 1  1 1-tr rhloro
ethane yields.*  The overhead from this column ?s farther


catafys°C(l°ri'n£fl?n-cS f3V°red 1" the prssence of Frledel-Crafts
distillation temperatures).              C "V ^  LerT1Perat-res (e.g.
                                 A-l

-------
fractionated  into two streams:   (1) the  lighter  components  primarily
vinyl  chloride) hydrogen chloride,  and  (2)  1,1-dichloroethene  and
1,1-dichloroethane.  The lighter components  are  recycled  to  the
hydrochlorination reactor  and the  1,1-dichloroethane  product  is
removed  at the  bottom stream.

      1,1-Dichloroethane and  chlorine  react  in  the  chlorination reactor
at  temperatures between 350-400°C  and pressures  of 2-5  atmospheres.
To  minimize by-product formation,  low molar ratios (e.g., 0.35-0.70)
of  chlorine to  1,1-dichloroethane  are used.  Table 33  in  Appendix  B
presents  typical  reactor effluents  found  in patent examples.   Hydrogen
chloride  and  low  boiling organic hydrocarbons  are  taken overhead.
This  stream is  normally used to  supply  the  hydrogen chloride
requirements  of this process although it  may be  used  in other
oxy-chlorination  processes.  The bottom stream from the hydrogen
chloride  column is  further fractionated;  1,1,1-trichloroethane is
removed  overhead  and, after  the  addition  of a  stabilizer,  is  stored.
The bottom stream from the 1,1,1-trichloroethane column,  comprised
largely  of 1,1,2-trichloroethane,  is  used as a feedstock  for
production of other chlorinated  hydrocarbons (e.g., tetrachloroethane,
trichloroethene and vinylidene chloride).
                               i
      NOTE 6:  Chlorine and  ethane react  in an adiabatic  reactor at
approximately 400°C and a  pressure of 6 atm.  with a residence time  of
approximately 15  seconds.  The reactor  effluent  (containing ethane,
ethene,  vinyl chloride, ethylchloride,  vinylidene  chloride,
1,1-dichloroethane  1,2-dichloroethane,  1,1,1-trichloroethane,
1,1,2-trichloroethane, a small amount of other chlorinated
hydrocarbons, and hydrogen chloride)  is quenched and cooled.   The
bottom stream from  the quench  column, primarily  tetrachloroethane  and
hexachloroethane, is removed and the  overhead  product is  fractionated
in  the HC1 column into a chlorinated  hydrocarbon stream and light
products stream --  ethane, ethene, and  hydrogen  chloride.   The bottom
stream from  the hydrogen chloride  column is sent to the heavy-ends
column where  it is  separated into  two streams.  1,2-Dichloroethane and
 1,1,1-trichloroethane  are  removed  as  a  bottom  stream and  are suitable
as  feedstock  for  other  chlorinated hydrocarbon processes.  The
 overhead product  (principally  1,1,1-trichloroethane, vinyl  chloride,   .
 vinylidene  chloride, ethyl chloride,  and 1,1-dichloroethane) is
.fractionated  and  1,1,1-trichloroethane  removed as  a bottom product.
 The overhead  stream from  the 1,1,1-trichloroethane column is fed to
 the 1,1-dichloroethane  column,  where  1,1-dichloroethane is  separated
 as  the bottom stream and  recycled  to  the chlorination reactor.

      Vinyl  chloride, vinylidene  chloride, and  ethyl chloride (the
 overhead stream)  produced  as a result of the direct chlorination of
 ethene are fed to the hydrochlorination reactor, where vinyl chloride
 and vinylidene chloride  react with hydrogen chloride to form
                                  A-2

-------
  1,1-dichloroethane and 1,1,1-trichloroethane, respectively.
  Hydrochlori nation reaction conditions are approximately 65°C and 4
  atm.   The reactor effluent stream is  neutralized with ammonia.   The
  resulting complex (ammonium chloride  - ferric chloride - ammonia)  is
  removed by the spent  catalyst  filter  as a semi sol id waste.   The
  filtered hydrocarbon  stream is fractionated further:   the bottom
  fraction (primarily 1,1,1-trichloroethane)  is recycled to the
  1,1,1-trichloroethane  column,  while the overhead stream (primarily
  ethyl  chloride and  1,1-dichloroethane)  is  recycled  to the chlorination
  reactor «

      NOTE. .7:.  ^. most  cases the  vent  gases  from direct  chlorination
  and oxy-ch ion nation processes  are incinerated or catalytically
  combusted  to  recover HC1  (EPA,  1975a; McPherson, et aj.. f  1979).

      NOTE1:   Calculations for quantity of  1,1,1-trichloroethane
  contained  in  heavy ends wastes  generated by  vinyl chloride  "balanced
  Sn°?Q7A i(!ex- APpendl'*B> Fl'9Ure B3'  for waste source  ^cation), based
  on 1978 1,2-dichloroethane production figures.    '

      In 1978, approximately 5.1 x 106 kkg of 1,2-dichloroethane
 were produced by the "balanced process", ^here'approx Sat*  29 kg of
 l I ^vh3?^  £6aVy end,S Ve?ctor tar*) were generated per 1 kkgof
 1,2-dichloroethane produced, (Lunde,  1965).*  Of  the total solid

                                                                if
°ff kk1 ?Vyal,so11d waste'  then;    1-48 x 10  kko  (total wasted
 kkg or 1,2-dichloroethane              5.1 x 10  1,2-dichloroethane

similarily applies; and 96% of 1.48 x 105 = 1.42 x 105 kka of
heavy ends wastes.  According to an EPA report (1975a), approximately
0.8% (by weight) of vinyl chloride heavy ends was 1,1 i-trichloro-
w tMn'thl Href0re',1>13^kk? °f M.l-trlchloroethini were   Stained
within the heavy ends.  The lower end of the range,  20 kkg  which
    '                   p°f 1.1.1-tHchloroethane iX  heavyendl was
                        Based on quantities of vinyl  chloride product
                          1n 1978 (l'-e" 3'15 x  10^  kk   and
oOQ08 kn nh                      -"  '   x       g  and
0.0008 kkg of heavy ends were generated per 1 kkg of vinyl chloride
197^   ?fSn°£ ^52° kkE ?f heavy  ends wastes were generated (EPA
i?hJn}' J    8% (t>^ WS1ght) Of the  heav^ ends 1-s 1.1,1-trlchlorS-
cont^J f ahPPr°xlmats^ 20 kkg of 1,1,1-trichloroethane were
contained in the heavy ends wastes (EPA, 1975a).
*The figure representing 1978 1,2-dichloroethane production quantity
u at variance with data reported by the United States Inte^a?ionaf
                           8 Production ^ ^ intermediate
                                 A-3

-------
         NOTE
_9:   Calculation  of  1,1,1-trichloroethane  contained in vinyl
\art^rtV»  ^ ^ W»^  f^-\/%  C * X«* i U.A  Q ^  ~ ..  4 _ _	»JJ_  r\  ^ _ _   __!_
    chloride  reactor tars  (see Figure S3  in Appendix 3  for waste  source
    location).

         Based on 1978  1,2-dichloroethane production figures  via  the
    "balanced process"  (5.1 x 106 :
-------
Plant No
12119
12161
12204
12257
12311
12420
12439
12447
Influent (vo/1 )
110
3
27
110
17
110
251
720,000
Effluent (uq/1)
10
__
33
110
--
110
12
--
Flow rate (mad)
0.05
1.00
0.20
0.50
0.16
0.17
0.01
1.50
g/day
discharged
2
-0-
25
208
-0-
71
.45
-0-
      NOTE  12:   Based  on  EPA data  (1980c),  average  POP^  influent
 equalled 66  yg/1 ;  effluent  equalled  10  x 4 ug/l .   Using a total
 nationwide POTW  flow  of  10n I/day  and  365 day/yr  operation,  2,410
 kkg  of  1,1,1-Trichloroethane were  contained in  POTW  influent;  380 kkg
 in effluent.   Based on raw  sludge  concentration  of 30.8 ug/1  of
 1,1,1-trichloroethane, and  a total  of 6 x  106 kkg  dry  sludge
 generated  per  year which  is  9555 water (by  weight), 4 kkg of
 1,1,1-trichloroethane were  contained in land-destined POTW  sludqe in
 1978.
                I/day x 66  yg/l  x  365 day/year =  2,410 kkg/yr.

          1011  I/day x 10  x 4 yg/l x 365 day /year =  380 kkg/yr.


          .05 x = 6 x 106   x = 1.2 x 108 kkg  1.2 x lO^1 1

          1.2 x 1011 1 x 30.8 yg/1 = 3.69 kkg


     NOTE 13:   Estimated production of 1,1,2-trichloroethane is
calculated as follows:  122,450 kkg 1,1-dichloroethylene/yr x 1.528
kkg 1,1,2-trichloroethane  per kkg 1,1-dichloroethylene = 187,100 kkg
1 ,1 ,2-triehloroethane.

     NOTE 14:  Some 1,1,2-trichloroethane is discharged with the solid
waste generated during 1,2-dichloroethane production.  Based on 1975
discharge rates:  2 kg of  1,1,2-trichloroethane discharged/kkg 1,2-di-
chloroethane produced by direct chlori nation x 2.08 x 10° kkg
1,2-dichloroethane produced = 4,000 kkg of 1,1,2-trichloroethane
generated and contained  in solid waste.
                                 A-5

-------
                               APPENDIX B

                     VINYL CHLORIDE MANUFACTURE VIA
                          THE BALANCED PROCESS

      In  addition  to  direct  chlorination and  oxy-chlori nation
 processes,  a  pyrolysis  (dehydrochlorination)  process  with  attendant
 purification  process  has  been  added.   Current yields  of  dehydro-
 ch  onnation  of 1,2-dichloroethane are on  the order  of  50  to  60*,  with
 selectivity  to  vinyl  chloride  of 96-99+% (McPnerson et al.,  1979
 Based  on  the  current  yield  of  1,2-dichloroethane  pyrolyTis" with
 equimolar production  of hydrogen  chloride  (and  allowing  for losses)
 capacities  of  oxy-chlorination and  direct  chlorination processes  are
 approximately  equal.
     Crude 1,2-dichloroethane from the oxy-chlorination process is
     !LW1Jh ? ll*tS,Cauf?1c *? remove h^dr°9en chloride and chlorinated
  :rS?   5 ("?tably chloral) and dried.  "Crude" 1,2-dichloroethane
from direct chlonnation may be combined with this stream and purified
for pyrolysis; alternatively 1 ,2-dichloroethane from direct
                                 pure for pyrolysis without further
               After dehydrochlorination, the reactor effluent is
quenched with 1,2-dichloroethane and separated by fractional
JiriJ]8^?" •" ;.ser1es of co1umns.  Hydrogen chloride is recycled to
the oxy-chlorination reactor while recovered 1,2-dichloroethane is
returned to the 1,2-dichloroethane purification system.
                                8-1

-------
                    1AQLE  B.I   1,1,1-Trlchloroolhano Releases  to tho Environment  from Vinyl  Chloride Process  In  1979
                                                                                                        (kkg)
      I'rodiict-r
     (I n< uI inn)
(Jiuiil ity  Produced
 (x  ll)3 kkl)t'                   ™»\            vent            cor, eel Ion of
                           condensers      condensers     major  leaks

            none   none    refrigerated    relri.j«raled   detection and  none
                           wcllt            *«••<•            correction of
                           condensers      condensers     major  leaks

recycled    none   none    refrigerated    refrl.jeraled   detect ion a,	one
                           vtilt\             v«-'"1            correction of
                          condensers     condensers     major  leaks
CO

ISJ
                                                                                      ()iiantity Dispersed
                               rc
                                                 f|e
                                          IIIC
                                                                                        I'S
   CroUucur
   (local ion)
        ^^J^l^l^!!_^.^^^  Waler^ Airland  Wale.  Air   Un7 Wat^7,7, and""Ja«  ^U,


                 IILHJ"   J   iiou'1   iieq'1 itco*1   111*11'*  1 (    ..., fi    ii    i .        h                  i       .
                              •"      "   *  J     IIL*I   I J    III'CJ    /I    II    ikitji"   £. I    f        It      li     i      I      I
                                                                                "'9    oi    !>     nt'(|"   ney"  NA1   n«i|"  neii1'     (ft/



                                                            "l!y     ''     '    ""'J1   10    3     wey'1   neii'1  NA'   ncu'1  ni-n'1     i?^
                                     „
                                                                                                                                                          „
   lul.il
                                                                                              "'   "
                                                                                              »
                                                                                                                                           «••
                                                                                                                                                               «/

-------
                                                 Table H.I (concluded)


a) Soo text and Noto 5 In Appendix A fur supplemental Information.

l») Assuming production quantities per plant are similar to those production quantities  In  1978; and total  production
   quantity equal to difference between total  quantity of 1,I,l-trIcliloroethane produced  (321,830 kkg, Harris,  1980)
   and quantity of I,I,l-trIchloroethane produced by direct chlorlnatlon of ethane  (25,000 kkg, Phillips,  I9fl0).

c) TC = 1,1,1-trlchloroolhano column vent; Fj  = filter, IIEC - heavy ends column, PS = product  storage; II »
   handling; F2 = fugitive emissions; and W = wastewaters from steam stripping; vent  losses of
   1,1,l-trIchloroothano  from light ends column and  Intermediate storage (I.e., vents LEG and  IS, Figure B.I) are
   negligible  (see Appendix A, note 2) are assumed to bo  negligible (EPA,  1979); see Figure B1  for  location  of  waste
   s11os.

d) Kilograms of  I,1,l-trIchloroothane dispersed to air (and water)/kkg produced from TC vent with aqueous  scrubltors  Is
   0.02 (and 0.17), see  nolo  1, Appendix A; fromF,  vent  sent to  landfill  Is 0.022,  (Elkln, 1969);  from IIEC  vent
   w11 limit controls  Is <0.001; from PS, H, and F2 waste sources controlled with refrigerated vent condensers, or
   through detection and  correction of major  leaks,  are 0.103, 0.00 and 0.039  to air, respectively,  and 0.58, 0.5 and
   0 10 wator, respectively; and W discharges (uncontrolled) are 
-------
       TAUI t H.2   Environmental Keloasos  from I, I, l-Trlchloroolhane Product Ion via  Dlroct Cli lor I nation of FKicino Procoss, 19/U  (kkg/yr)'
()
negl
neg
1
negf
6
'
                                                                                                     ili
2
negf
13
it.
1
negl
negl
neg
Soiine:  ll'A,  lrils  are %, H'j. ft5. IIS and 90*
      respectively and already  included in wasle cinission/dischargc/disposal  ratios  lie low.

   e) Kdl i<» «f kilograms of  1 .1 .l-tricliloroethdiie dispersed to air and  (water)  per nioli ic Ion protluced from fC  with
      glycol (Hit conlrol device  is  O.OOJ'j (see Appendix A. nole 3) and  (().()(,/);  for  uncontrolled ,nr ctuissions  frmn
      inc iner.il ion and releases  to  landfill from I, and I) comUined (assuming  wasles  lo he solely composed of
      I ,1 ,1-lrichloroethane)  is  < 0.001;  from US. l"j and II controlled hy ref rigei «led venl condensers are (I.Ojg,  0.103
      and  0.0'JO to air. respecl ively  and  0.221, O.WI and O.bl  lo water, respectively; 1 2 a|r emissions (assuming  to
      l>e solely composed of  1 .1 ,1 -Iricfifuroelhane) controlled  hy detection and  correction of iiMjor leaks is 0.17U;  and W
      dischai ijes (unconlrol li.-d)  is  0.001.

   I ) He-jl Hjible, i.e., 
-------
  Table  8.3  Vapor Phase Chlorination of 1,1-Dichloroethane
                                Product  Stream,  Mole %
 Reaction  Product                Process  Aa     Process  3b
Vinyl Chloride
1,1-Dicnloroethane
1,1-Dichloroethene
1 , 1 , l-7richloroethane
1,1,2-Tricnloroethane
cis-l,2-Dichloroetnene
trans- 1,2-Oichloroetnene
Tetrachloroe thane
Tricnloroethene
Tetrachloroethene
Pentachloroethane
Unknown
22.7
4.6
34.9
25.9
1.]
2.7
2.3
1.5
2.9
0.2
0.1
1.2
19
38
6
36
1.5
0.5
0.5
w • v
__
^ —
— —
--
a)  Tuoular nickel reactor 6.1 m x 6.35 mm ID.  Reactor
    conditions:  4500C, 3.55 atm., 1  sec. residence
    time, molar ratio C12/1,1-dichloroethane:   0.7,
    1,300 ppm C02 added to gaseous feed.   Source-
    Rideout and Monsell, 1980.

b)  Glass reactor 0.75 m x 50 mm ID.   Reactor
    conditions:  4lqoc, 1  atm.,  8  sec.  residence
    time, molar ratio C12/1,1-dichloroethane:  0.45.
    Source:  Campoell and  Carruthers,  1972.
                              3-5

-------
          Table 3.4  Industrial Classes Utilizing Degreasing
           Source  Type
Industrial  decreasing
  Metal  furniture                                              25
  Primary metals                                               33
  Fabricated products                                          34
  Nonelectric machinery                                        35
  Electric-equipment                                           36
  Transportation equipment                                     37
  Instruments and clocks                                       38
  Miscellaneous                                                39
Automotive3
  Auto  repair shops  and garages                                ?5
  Automotive dealers                                           55
Gasoline stations                                              55
Maintenance shops                                               a
Textile plants  (fabric  scouring)                               22
 a)  No applicable SIC for  this category.
 Source:  EPA, 1979c.
                                      3-5

-------
  Table B.5  Industrial  Wastewaters
             Been Detected
                 in  which  1,1,1-Trichloroethane Has
Industry
Adhesives/Sealants
Batteries
Coal Coating
Coal Mining
Electrical
Electroplating
Foundries
Iron/Steel
Laundries
Leather
Mechanical Products
Nonferrous Metals
Organic Chemicals
Organics/Plastics
Paint/Ink
Pesticides
Petroleum Refining
Pharmaceuticals
Phosphates
Photographic
POTWs
Printing/Publishing
Pulp/Paper
Rubber
Steam/Electric
Textiles
Timber
Number of Times
Detected
1
1
2
18
9
3
3
1
8
3
26
3
4
122
45
10
7
18
1
7
12
• 12
4
7
/
11
A 4
i
i
1
Number of Samples
Taken

•3
o
12
1 £.
249
-5C
O3
10
10
G.A.
01
4^1
HOi
56
^u
SI
01
7^
Oi>
173
723
QA
:?f
147
7fi
/O
0£
rD
-5 -3
jj
oc
CJ
40
*tv
109
no
yo
^ *7
o7
O>1
84
121
285
a) False positives
b) Not given.
are accepted.
Source:  EPA, 1980b.
                                      3-7

-------
Table 3.5  Industrial  Uastewaters in which 1,1,2-Trichlcroethane has
           Been Detected
Type of Wastewater
Adhesives/Sealants
Foundries
Iron/Steel
Laundries
Mechanical Products
Organics/Plastics
Paint/Ink
Petroleum Refining
Pharmaceuticals
Phosphates
Printing/Publishing
Timber
Number of Times
Detected3
1
1
2
2
7
22
8
7
4
1
1
1
Number of Samples
Taken
11
34
431
56
35
723
94
76
95
33
109
285
a) False  positives are accepted
Source:   EPA,  1980b.
                                      B-3

-------
          •j
         I
         £»
       OvlH
                      i«vouo-
                 F,
                 IICI
                 iLOLUMU
          CO-UMU
•n
                                          rj
                                          r
                                          t
                                           c
                                                                 J]
                             J'. 1-S
                             u
                                                                 DC
                                                                  t
                        1.^?^!
 .	I Ctti.rtu.iUA.Yioj
 —^ RAALTTUH-
^

  r   ..   f.Ui^rr'^t
                                               H
                                                              MISCELLANEOUS
                                                              WASTEWATER
                                                           V  SOURCES
                                                                                               W
n«jure R.I   Flow Diagram  for  1.1,1-Trlchorocthane Production  from Vinyl Chloride and Point and Nonpolnt Waste Sources3

footnoLos,  next  page

-------
CO
I
o
                                                   Figure B.I (concluded)
      a) F2=Fugitive Emissions; TC=l,l,l-Trichloroethane Column  Vent;  Fi=Filter;  HEC=lleavy Ends Column Vent;
         LEC=Light Ends Column Vent;  IS=Iritermediate  Storage;  PS-Product Storage; ll=llandling; and W^Miscellaneous
         Wastewaters.

      b) This stream is primarily composed of  hydrogen  chloride  gas and low-boiling organic compounds and is
         either used to supply the hydrogen chloride  requirements of other chlorinated organic processes directly
         or is purified and then used.

      c) This bottom stream is composed primarily  of  1,1,2-trichloroethane, which is kept in-house as a feed
         material to other chlorinated  organic processes.
      Source:  EPA, 1979a and 1979b.

-------
                                             If I MCI
                                             •>uni|»c*T»O«j
                                                                                                            r*
                                                                                                            pdlLORINATION
                                                                                                               REACTOR
                                                                                                               PRODUCT
                                                                                                               RECOVERY
                                                                                                               COLUMN
                                                                                                             MISCELLANEOUS
                                                                                                             WASTEWATER
                                                                                                             SOURCES    I


                                                                                                                       W
 Figure B.2  Flow Diagram for  1,1,1-Trlchloroethane Production from Ft.hane  anH  Point  anH Nonpoint Wast.. Sources^

a) F2^FugiLive omissions; Q=quench column vent; TC=l,l,l-trichloroothane column, 1,1-dichloroethane column and product
   recovery column vents combined; Fi=fliter (catalyst) vent; RS=recycle storage vent; PS=product storage vent;
   ll-handliny; and W-wastewaters from steam stripping.

b) Wdsl.es from the hydrogen chloride column overhead stream contains IICI, ethane and cthylene.

c) Wastes in (.his bottoms stream (primarily 1,2-dichloroethane and 1,1,2-trichloroethane) are transferred as feed to
   other chlorinated hydrocarbon processes.

SourceT'Tl'A, 197'Jli and  197%.

-------
1IC1



Mil
  co
  i
 Cl.
           i     »
IlKACTOIl
                  NuOII

                     1
-/WASIIHIl   j	


             i
                 OXYCIJLOHINATION
               nillKCT CIH.OHINATION
                       1UIAGT011
                          WASTH-

                          WATliIl
                                                                o
                                                                o
                                                                   ^.UGIIT

                                                                      HNDS
                                                                        O
                                                                        o
                                                 Y
                                                                      IIKAVY

                                                                       ENDS
                                                            c/»
                                                              Ml
                                                            U»(J

                                                            >* rf
                                                            »-l -x
                                                              K
                                                                         o
                                                                                             O
                                                                                             as
                                                        0.

                                                        en
                                                                                                       O
                                                                                                       O
                                                          1.2-DIGIIf.OIlOHTIIANH

                                                                Ui:CYGLH
                 Figure B.3  The Balanced Process for Vinyl Chloride Manufacture and Waste Sources
                                                                        VINYL

                                                                        CIILOIU
                                                                                            TARS
                 Source:   EPA,  1979d.

-------
                               APPENDIX C

                      SOLVENT RECYCLE CALCULATIONS


      Derivations  of  the  total  quantity of solvent used 1979,  including
the  amount  recycled  from the previous  year is  shown below;  fable  Cl
gives  values  used  to  derive  variable y.

Quantity Recycled  = x  •  quantity wasted     x =  .45  (45X of  waste  is
                                                    recycled)

Quantity Used = quantity virgin solvent +  quantity  recycled or
         used = virgin solvent + .45 waste.

Quantity Wasted = y  .  quantity used or y  (virgin solvent + .45 waste)


          y « percent wasted solvent    68,630_ =   312
                                       220,130

     'Solving for waste:

         Waste  =  y (virgin solvent)  +  .45 y waste
                  waste = 0.363 (virgin solvent)

     Then:

         Recycle  * .45 waste
                  - (.45)  (.363)  (virgin  solvent)
                 =0.162  virgin solvent

    Also:  Use = Virgin  solvent + recycle
           Use - 0.1404  Use  = virgin solvent
           Use = 1.16  (virgin solvent)
                               C-l

-------
      Table C.I  Waste Solvent Generation by Degreasi'ng Operation
Operation
                       Virgin
                    Solvent Used
 Precent (%)Solvent Wasted
Solvent Wasted        (kkg)
Cold Cleaning:
Manufacturing
Maintenance
23,310
29,700
40-60(50)
50-75(62.5)
11,660
18,560
Open-top vapor        106,280
degreasing

Conveyorized vapor
degreasing             45,530

Conveyorized
nonboi1i ng
                                      20-25(22.5)
                                      10-20(15)
a) Totals do not add due to rounding.
                      23,910
                       6,830
degreasing
Fabric scouring
Total3
. 12,070
3,260
220,130
40-60(50)
40-60(50)

6,040
1,630
68,630
                                 C-2

-------
                              APPENDIX C

               AMBIENT LEVELS OF 1,1,1-TRICHLOROETHANE

     The compound 1,1,1-trichloroethane has been found  in a broad
range of environmental redia such  as:  freshwaters, saltwaters, soils
sediments, and the atmosphere (Table Cl).  The concentration of
1,1,1-trichloroethane in these media depends upon many  factors (i.e.
location of sampling site and meteorological conditions).           '

     According to Singh and his associates (1977), 1,1,1-trichloro-
ethane is present in the environment due to the activities of mankind
and has no known natural source.  Furthermore, the urban-rural
relationship of 1,1,1-trichloroethane is typical of an  urban-sourced
pollutant (Table Cl), and in fact, the average concentration ratio of
rnnc!£6o1«M Durban  and  rural air  is about 15  (Sinah et al. 1977).
Consequently, 1,1,1-tnchloroethane wastes found in the environment
are most likely released from man's activities.
                                C-3

-------
         Table C.2  Concentrations of  1,1,1-Trichloroethane  in Select  Environmental  Samples
Environment^ «ei:a Sarple Location5
U R
.„. .ar ..j^^. -.
PGTV5
Fresriv.ate- In'lusnt to
Tas »atsr »
Surfac* «ata' (law) •'
Seav.a-.5-- (coastal } /
Soil ^
Sediments (lake) •'
Air
Air ^
Air
Air /
Air
Air /
Air /
Air S
Air /
Kean Concentration (spt)
16,530

16.50C
22, COO
5u
140
530
430
S4
330
100(sl5)
-•<3CO
610
1,530
57
95
33
Infcrration Source
EPA, 1975

Sel'ar, Lic.itsnoa'g,
and Krone'', 137C
EPA, 1377C
E?A, 1377C
Sincn, Sa'as, ana
Cavar.agn, 1377
EPA, 1377C
EPA, 1977C
Sinah, Salas, ar.c
Cavanagn, 1977
Lillian, ft. aj... 15
1975
£?A, 1977c
Lillian, fj.. jj. , 19









"5
36f

75
Lillian, et. al.. 1975
Lillian, et. a]., 13
Russell and Shaacff,
1977
Russell and Shasof*.
1577
75


>} y « Ursan; S « Sural
b) Before Trei—.an:
                                                      C-4

-------
                                 APPENDIX D

 D.I  ESTIMATION OF VOLATILIZATION FROM WATER

      Volatilization from water can be estimated using procedures described
 in the literature.  The mathematical modeling of volatilization involves
 interphase exchange coefficients that depend on the chemical and physical
 properties of the chemical in question, the presence of other pollutants,
 and the physical properties of the water body and atmosphere above it.
 Basic factors controlling volatilization are solubility, molecular weight,
 and the vapor pressure of the chemical and the nature of the air-water
 interface through which the chemical must pass.

      Volatilization estimates can be based on available laboratory and
 environmental data.  Because of the lack of data for most chemicals,
 however,  estimates of volatilization rates from surface waters on the
 basis of  mathematical data and laboratory measurements are necessarily
 of unknown precision.   Still, comparisons of experimental results with
 theoretical predictions indicate that these predictive techniques generally
 agree with actual  processes within a factor of two  or three in most cases.

      The  methods described below have been used  to  estimate volatilization
 from natural surface  water (see Section 4.12).   The EXAMS Model has been
 used to investigate behavior in natural surface  water bodies,  however,
 this method was  not used  as input  to EXAMS.   An  input parameter similar
 to the reaeration  coefficients described below is used in EXAMS to
 estimate  volatilization;  this value  was obtained elsewhere.

      The  following procedures can  be used  to  estimate the volatilization
 rate  of a chemical.  Minimum data  required  are:

      •  Chemical properties—vapor pressure,  aqueous  solubility,
        molecular  weight;

      •  Environmental characteristics—wind speed, current speed,
        depth of water  body;

 (1)  Find  or estimate the Henry's Law constant H from:

     H = P/S  atm-m /mole

where  P = vapor pressure, atm
       S = aqueous solubility, mole/m .

When calculating H as a ratio of vapor pressure to solubility, it is
essential  to have these data at about the same temperature and applicable
to the same physical state of the compound.  Data for pure compounds
should be  used because vapor pressure and solubilities of mixtures mav
be suspect.
                                  D-l

-------
 (2)   If H<3  x  10    atm-m /mole, volatilization  can  be  considered unim-
 portant as an  intermedia transfer mechanism  and no  further  calculations
 are necessary.

                -7       3
 (3)   If H>3  x  10    atm-m /mole, the  chemical  can be considered volatile.
 The nondimensional  Henry's Law constant H' should be determined from:

      H' = H/RT                                                     (2)

 where R » gas constant, 8.2 x 10    atm-m /mole K

       T - temperature,  K.

 At 20C (293K)  RT is 2.4  x 10"2 atm-m3/mole.

 (4)   The liquid phase exchange coefficient k& must  be  estimated.  This
 coefficient  is from a method that analyzes the  volatilization  process
 on the basis of a two-layer film, one water and one  air, which separates
 the bulk of  the water body from the bulk of the air  (Liss and  Slater 1974)

      For a low molecular weight compound (1565, kjj, can be estimated from equations developed by  Southworth
 (1979).  Because this method is different from  Equation (3) / the esti-
mated values may vary.  If the average wind speed is < 1.9 m/sec,
             T0.969\
/
(
\
              .673/
             curr _ 1   J32_



where  V     » water current velocity, m/sec

       Z     « depth of water body, m.

If wind speed  is  >1.9 m/sec and <5 m/sec,

            ,0.969'.
                             0.526 (V  . ,-1.9)     ..
                            i        wind       cm/hr              (5)


where  V . , = windspeed, m/sec.
        wind

If wind speed  is >5 m/sec, liquid phase exchange coefficients are diffi-
cult to predict and may range up to 70 cm/hr.

(5)  The gas phase exchange coefficient must be estimated.  This too is
based on the two-film analysis.   For a compound of 15
-------
  Slater (1974),

       k  -  3000 yia/M* cm/hr                                          (6)


  If M>65  (Southworth  1979),

       kg  =  1137.5  (Vw.nd + V)  li/S  cm/hr  .
  (6)  The Henry s Law constant and gas and liquid phase  exchange  coefficients
 are used to compute the overall liquid phase mass transfer coefficient,
 KL (Liss and Slater 1974), which is an indicator of the volatilization' •
 rate:                      f
           (H/RT)k k£      H kgk£

      \ = (H/RT)k +k   "  H'k + k   Cm/hr                           (8)
                  g  4        g   i

 (7)  The volatilization rate constant k  is:
                                        v
                hr"1
                                                                     ( 9}

 where  7. is  in cm.

 (8)  Assuming a first  order volatilization process,  the concentration
 in the  stream in  the absence  of  continuing inputs  at the location at
 which volatilization occurs,  is

      c(t) -  c/V                                                 (1Q)


 where   c(t)  = pollutant  concentration  in  the water column  at  time t

        co    " initial pollutant  concentration in the water column.

 (9)  The half-life in the water  column for the pollutant volatilizing  at
 a  first order rate is:

     r  = 0-69 Z
     \    KT      hr'                                               (11)
Another method for computing k  for highly volatile chemicals with
H>10   atm-mJ/mole is based on reaeration rate coefficients (Smith and
Bomberger 1977, Smith et al. 1979, Tsivoglou 1967).  The following data
are required:

     •  Ratio of reaeration rate of chemical to that of water,

     •  Reaeration rate of oxygen for water bodies in the environment
        or steamflow parameters (velocity,  stream bed slope, depth).
                                  D-3

-------
 If the oxygen reaeration rate is known for a given water body or type
 of water body, the volatilization rate constant for the pollutant can
 be estimated from (Smith and Bomberger 1979):
(kv
                                                                     (12)
 where  kv - first order volatilization rate constant for the
             particular chemical (hr~^);

         o                                           -i
        k^ * reaeration rate constant for oxygen (hr  );

        env= designates values  applicable to environmental
             situations;

        lab - designates laboratory  measured  values.

 This  equation  applies  particularly to  rivers.   For  lakes and ponds,  the
 following  equation may be more  accurate:


      (k )    »  (k /k )   '   (k°)                                     t-i -n
        v env     v  v   lab   v  env                                ^-L-5'

 Typical values  of (k°)env are given in the  literature and reported by
 Smith et. al  (1979):

      Water Body
     Pond                 0.0046-0.0096

     River                0.008, 0.04- 0.39

     Lake   .              0.004-0.013

The values for ponds and lakes are speculative and depend on depth.

     Mackay and Yuen (1979)  present the equations listed below that cor-
relate k° with river flow velocity, depth, and slope:


     Tsivoglou-Wallace:    k° = 638 V    s  hr'1                    (14)


     Parkhurst-Pomeroy:    k° = 1.08 (1 + 0.17 F2) (V    s)°*0375 hr'1   (]


     Churchill et al.:      k° = 0.00102V2^5 Z'3'085 s~0.823 ^-1  (lg)


If no slope data are available:


     Isaccs-Gundy:         k° = 0.223V    Z~1>5 hr'1                (17)


     Langbein-Durum:       k° = 0.241 V    z'1'33 hr'1
                            v          curr
                                  D-4

-------
  where  VCUTT - river flow velocity (m/s) ;

             s - river bed slope = m drop/m  run (nondimensional) ;
             Z = river depth (m) ;

             g = acceleration  of  gravity  =9.8  m/s2.

       Because none of the foregoing is clearly superior  to  the others,
  the best approach is probably  to use all that are applicable  and  then
  average the  results.  For  a  river  2 m deep, flowing  at  1 m/sec, the re-
  aeration rate  is estimated as 0.042/hr.  (kj/kj)^  is  known  for  some
  chemicals  (See  Table D.I).   If a  In prjnciPle' kv is the same  as (KL/2) ;  however, due  to  the  use of
  <*v'env» W has the  depth  and other water body characteristics embedded
 within it.   Therefore, no  adjustment is required for use in the first
 order volatilization equation.

 D'2  ESTIMATION OF VOLATILIZATION RATE FOR TRICHLOROETHANES

      The half-lives  for trichloroethanes at 20° C in a river 1 meter deep
 flowing at  1 m/s will be estimated.  Wind speed is 3 m/sec.

 D.2.1   1,1, 1-Trichloroethane

     Vapor  pressure  of 1,1,1-trichloroethane at 20°C is  100 mm Hg

                                                  is  440°
      1.   Calculate  the Henry's  Law constant:

           ,,    0.13  atm                     •?
           H = - j  =   °-0039  atm-m /mole
                33 moles/m

      2.   Because H>10~3 atm-m3/mole, 1,1,1-trichloroethane  is highly
     3.  The nondimensional Henry's Law constant is H/RT,

           H' = 0.0039/0.024 = 0.16 at 20°C.
4.  Because M>65 and Vwind >1.9 m/sec, the liquid phase exchange
ic


                                                   1-».20.5 cm/hr.
coefficient kjj, is:

           kl - 23.51

     5.   The gas phase exchange constant is:

           kg = 1137.5 (3 + DN18/133.4 = 1700 cm/hr.
                                  D-5

-------
                    TABLE D.I
MEASURED RE AERATION
COEFFICIENT
RATIOS
FOR HIGH VOLATILITY COMPOUNDS
Compound
Chloroform
1 , 1-Dichloroethane
Oxygen
Benzo [b] thiophene
Dibenzothiophene
Benzene
Carbon dioxide
Carbon tetrachloride
Dicyclopentadiene
Ethylene
Krypton
Propane
Radon
Tetrachloroethyene
Trichloroethylene
H
atm-m3/
mole
3.8 x 10~3
5.8 x 10~3
7.2 x 10-2
2.7 x 1Q-1*
4.4 x 10~^
5.5 x 10~3

2.3 x 10- 2

8.6



8.3 x 10-3
1 x 10~2
Measured
. c /. o
k /k.
V V
,57 ± .02
.66 ± .11
.71 ± .11
1.0
.38 ± .08
.14
.57 ± .02
.89 ± .03
.63 ± .07
.54 ± .02
.87 ± .02
.82 ± .08
.72 ± .01
.70 ± .08
.52 ± .09
.57 ± .15
Source:  Smith et al. (1979).
                       D-6

-------
       6.  The overall liquid phase exchange coefficient  is:

             r  . (0.16X1700) (?n. 5)
              L   (0.16)(1700)+(20.5)  =  19  cm'hr-


       7.   The volatilization rate  constant  is:

             kv - 19/100 -  .19 hr.


       8.   The half-life for  volatilization  is:

             Tl/2  " °-69/0-19 " 3.6 hr.


      Alternatively, by the reaeration coefficient method:


  (17) a"nd ^^eaeration rate constant can be estimated by equations

      (kv}env = °'223 (Da)"'  » 0.223/hr,
 v'env

-c°)
 v'env
      'Oenv - °-2A1 aXD"1'33 - 0.241/hr.
               rM    rlues is  about  °-23/hr-   ™is  ±
        in the table of reaeration  rates  (0.008 - 0.39/hr for rivers).

      2.   A laboratory measured  value  of k£/k° is not available for 111
 trichloroethane.  Using the kv/k$  value fTom^able D.I for a chSlc.1
 with a similar H, chloroform (H =  3.8 x 10~3) ,               cnemicai

      GSP     = (°- 62) (0.23)  = 0.14/hr.
                                                            value of KL


     3.  Using equation (11), the half -life is:

     T1/2 » 0.69/(kJ)env » 0.69/0.14 = 4.9 hr.
                                ..           by the
D-2.2  1,1, 2 -Trichloroethane
     Vapor pressure of 1,1, 2-trichloroethane at 20°C is  19 mm Hs  f 025
                                   and  soluwuty  is 450°  "      "
     1.   Calculate  the Henry's Law constant:

     H -  0-025  atm      _  ,    -4      .
      ~  33.7 mole/m^ = 7.4x10   atm-m3/mole.
                                  D-7

-------
      2.   Because H > 3x 10"7 but < 10~3,  1,1,2-trichloroethane is only
 moderately volatile.

      3.   The  nondiznensional  Henry's law constant is H/RT,
      Hf  = 7.4xlO"4/0.024  =  3.1xlO~2.
      4,5.   ki and  kg  are the same  as  for  1,1,1-trichloroethane because
 molecular weights  are equal:
      k£  » 20.5 cm/hr
      kg  = 1700 cm/hr.
      6.   The  overall  liquid  phase  exchange constant is:
           (3.1xlO-2)a700K20.5)   ,,    ,.
           (3.1x10-2) (1700)+ 20.5  * 15  cm/hr*
      7.   The volatilization  rate constant is:
     k  -  15/100 = 0.15/hr.
      v
                             i
     8.  The half-life for volatilization is:
     Tl/2 = °-69/0-15 = 4.6 hr.

     Because 1,1,2-trichloroethane is not highly volatile, the reaeration
coefficient method is not used to estimate volatility.
                                  D-3

-------
                              REFERENCES

                    > P.  G.   Flux of
            Y' T''  V°U"liz*"°n rates of organic contaminants
Smith, J. H., Bomberger, D. C.  Prediction of volatilization rates of
chemcals in water.  Water: AICHE Symposium Series 190, 75: 375-381,


     ' Jf\*'i Boferfr' D' c" Ha>-". D- L.  Prediction of volatilization
Southworth,  G.  R.   The role of volatilization in removing polycycllc
                                                                Cl
                                D-9

-------
                               APPENDIX E

                 ATMOSPHERIC FATE OF TRICHLOROETHANES

      There must be a mechanism for removal of 1,1,1-trichloroethane
 from the atmosphere since cumulative world production (and assumed
 emissions) up to December 1975 uniformly mixed in the atmosphere would
 yield atmospheric levels about 75% higher than concentrations actually
 measured (Singh e_t al. 1977).  This appendix discusses removal mech-
 anisms for the trichloroethanes, although most information relates to
 1,1,1-trichloroethane.

      The compound  1,1,1-trichloroethane is resistant to  photo-oxidation
 (Hanst 1978).   In  the laboratory,  no  decay occurred when the compound
 was irradiated with black light-blue  lamps in the presence of 500 pphm
 N02 and 502 relative humidity (Lillian et, al .  1975).  Less than 57, de-
 composition was noted in 23.5 hr when 1,1,1-trichloroethane at  10 ppm*
 and NO at 5 ppm was irradiated by  a lamp  with a  UV short wavelength cut-
 off at 290 nm.   Less than 57,  decomposition was noted in  28 days at 50 ppm
 1,1,1 trichloroethane and 10  ppm NO-  (Billing ejt  al. 1975).   In studies
 with about 25  times the chlorine required to  initiate photo-oxidation in
 the chlorinated ethanes in comparable times,  the  following reaction pro-
 ducts were "noted:  CO,  HClt~CC1^0~ (phosgene) ,  and  CO .  Phosgene was
 found to  be the only chlorine-containing  product,  comprising 50% of
 the 1,1,1-isomer consumed.  The  1,1,1-isomer  was  found to be the least
 reactive  of the chlorinated ethanes,  some 30-50  times  less reactive
 than 1,1,2-trichloroethane.   The 1,1,2-isomer  photo-oxidized rather
 rapidly,  forming formyl chloride (HCC10) ,  phosgene (CC1  0) ,  and chloro-
 acetyl  chloride (CC12HCOC1) .   Formyl  chloride  accounted  for  44% of the
 chemical  consumed  (Spence and  Hanst
     The rate of photo-oxidation is a  function of latitude since OH
concentration ([OH]) is a function of  latitude.  Altshuller  (1980) estimates
that at 40°N latitude it would take 177 days in January and  11 days
in July for 1% of atmospheric 1,1,1-trichloroethane to be consumed by
OH.

     Because of 1,1,1-trichloroethane's long atmospheric lifetime and
pervasive use, it is distributed worldwide even though an estimated
97% of the world's use occurs in the Northern Hemisphere (Neely and
Agin 1980) .  The compound exists long enough for a portion to be trans-
ported into the stratosphere.  Lifetime in the atmosphere has been
estimated to be between 1.1 years and 15 years with 6-10 years a
reasonable "average" estimate (Hanst 1978, Cox _et al.  1976, Singh et al.
1978, Altshuller. 1980,. Rowland 1980, Neely and Agin 1980, Singh et al.
1980, and Campbell 1980).
 Concentrations were  originally reported in ppm, ppb, etc.  Those
 units will be maintained  in this section to facilitate comparison
 of concentrations.   Ippm  =5.46 mg/m  for 1,1,1 trichloroethane.
                                 E-l

-------
      Concentrations vary with location, altitude, latitude, and hemisphere
 (Cronn et al. 1977,   Singh et al. 1980, Cronn 1980, Campbell 1980,
 Singh st. alj.978, Spence and Hanst 1973).   The concentration in the lower
 stratosphere is noticeably lower than that in the troposphere (see
 Figures E-l, E-2, E-3).   The worldwide background in the troposphere is
 up to two times higher than concentrations at 13-14 km altitude, the
 lower reaches of the stratosphere (Spence  and Hanst 1973).   The transport
 mechanism causing this distribution is the influx of troposhperic air
 into the stratosphere.   Daily fluctuations in the lower stratosphere
 are usually due to meteorologic considerations.   In the intertropical
 convergence zone, it was noted that the rate of  decline in  concentrations
 was lower than in mid-latitude of the northern hemisphere,  probably
 because the tropics are  an area of upward  transport of tropospheric air
 into the stratosphere (Cronn 1980).

      Concentrations in the Southern Hemisphere are about  60%  of  concen-
 trations in the Northern Hemisphere (Singh .et al.  1980).  In  May,  1976,
 the (average Southern Hemisphere)/(average Northern Hemisphere)  concen-
 tration ratio was 0.42  (Singh et  al.  1978).   Above 30°N,  1,1,1-trichloro-
 ethane is well mixed in  the Northern Hemisphere;  between  20°N and  20°S,
 a  sharp decline is noted,  and below 20°S,  the concentration is lower
 (see Figures E-4 and E-5).   This  is  probably due  to  higher OH concen-
 trations, and hence  higher removal  rate  around the Equator, due  to  amounts
 of  sunlight  and water vapor,  and  not  to  a  normal mixing process.  The
 exchange time between hemispheres  is  about 14-17 months (Rowland 1980,
 Neely and Agin 1980).  Calculations  indicate that  one-half of all l,l|l-
 trichloroethane removal  occurs between 16°S  and 16°N, with the rate
 varying with altitude.   More  than one-half of  the  removal occurs in  the
 atmosphere below 2.4 km  (Campbell 1980).

      Concentrations  differ  between urban and rural areas.  Average urban
 concentrations  are about eight times background levels (Singh et_ al_. 1978).
 These  higher  urban levels may persist for  days (Cronn 1980).  AtTHmes,
 local meteorological  factors are more important than local emission  pat-
 terns  (Lillian  et. al. 1975).  During an inversion  situation in Wilmington,
 OH,  1,1,1-trichloroethane concentrations at 460 m, below the inversion
 height, were  about three times higher than concentrations above 1500 m.
 Localized and short-term variations in concentrations in an urban area
 and  in  the plume downwind are indicative of complex variable emission
 patterns with a  strong dependence on meteorological factors.

     Due to a long atmospheric lifetime, 1,1,1-trichloroethane is a good
 tracer  for the transport of urban pollutants.  Figure E-6 illustrates these
 observations where airborne concentrations  in New York City  are seen to
 increase during  the middle of the day.  In  the White Face Mountains of
New York, concentrations are seen to increase later in the day (see
Figure E-7).  Relative variations and time  dependence of the variations
at each location reinforce the relationship between the urban and rural
measurements.
                                   E-2

-------
    «4
    •3
    •2
   -4-
       «20
       •10
        «S
      -10-
      -15-
   -«- -10
         4O
                                   (300ml
                         *       • I
                       •      •      •
                           A   A  • .
                                              TROPOPAUSE
                 K1»CH i.ItT*
                 •ARCH t, I»T«
                 • AKCN 10, l*r<
                 MAKCN ll.l«?«

                 MAHCM I2.I§T«
                 •«lCM2t.l»7t
                                 (0
                               Ppt
                                                           —I
                                                            1)0
   Source:  Cronn et al. (1976)
100    110    120


Note:   1 ppt = 5.46 ng/m3
 FIGURE E-1   MIXING RATIO DISTRIBUTION OF 1.1.1 - TRICHLOROETHAIME
               AS A FUNCTION OF TROPOPAUSE HEIGHT, MARCH 1976
               47aN LATITUDE
••-

•5-

»«-
      •20.
  -9-
      •»-
       *
     -10-
                       (1001*1
                               4  *
* A

* •
TRCPOfiftCSe/

'x •'

X"
             90
                                  «o    no
                                                      130
  Source: Cronn et al. (1976)


FIGURE E-2   MIXING RATIO DISTRIBUTION OF 1,1,1 - TRICHLOROETHANE
              AS A FUNCTION OF TROPOPAUSE HEIGHT, APRIL 1977
              37° N LATITUDE
                            E-3

-------
                                                 DATE WKXEAIR
 KU
a-
      18-
      13-
      12-
       9-
          rr
         70-H
         SO-
         SO -
          40-
          30-
          20-
_ ,.
V*
7/1*
A, , -31 , 7/23 v
7X2S •
^_ y j^ o
* ^" 7/tai »
^ .

' 	 1 	
T
>
	 L
0 . V
•0- FOR CEARJCT VALUES
1 i _. I
                   CO      8O      lOO     IZO     I4O      I6O



                         CH,CO.j  MtXNG RATO, pp«
Source: Cronn and Robinson (1978)
FIGURE E-3    1,1,1 - TRICHLOROETHANE MIXING RATIO DISTRIBUTION AS

              A FUNCTION OF TROPOPAUSE HEIGHT, JULY 1977,9° N LATITUDE
                                E-4

-------
                200
              a
              a
                 50
              fB
              e
                lOO
              ."SO -
              o
              o
                            77" ppt
                                                  113' QOt
                                       j	L
                 •90'-aO* -60* -40* -20*   0*  20*  «0«  60*  80*90*

                  s              Latitude (deg)               N
     * A weighted average concentration is used to represent the total burden of the species


      in the hemisphere since a significant gradient within the hemisphere is observed.



     Source:  Singh et al. (1980)




         FIGURE E-4   GLOBAL DISTRIBUTION BY LATITUDE OF


                       1.1.1 -TRICHLOROETHANE IN LATE 1977
  120-
 100 H
c.
a
.28(H

 «j
cc


 c-

JeoH
                 *
    S  -80     -60
                                                           \

                                                           "Six
                                                   X AEROCOMMANOER FLIGHT. SEPT, 1978



                                                   * C-130 FLIGHTS, NOV., 1978



                                                   • AVERAGE OF HOURLY  GROUND

                                                     MEASUREMENTS,  OCT.-NOV., 1973




                                                   & GROUND SAMPLES, APRIL 8 JULY. 1978



                                                   o GROUND SAMPLES. NOV. 1978
                                       LATITUDE
                                                                   60
                                                                            80  N
    Source:   Singh et al. (1980)
             FIGURE E-5   LATITUDINAL GRADIENT OF 1,1,1 - TRICHLOROETHANE

                           CORRECTED TO NOVEMBER 1978
                                    E-5

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   12
	
.3
-—
.5
c
8
§
o
CO
o
U
CO
I
u

10

8
6


4




0
Location: New York
City
(45th St. and
Lexington
6/27/74



CH3CCI3

•
_^f ^.
_-—^*"^ \
1 1 1 1 1 1 1 ! 1 I^»— .
Ave)









»f-T
     100    500    1000      1500
               Time (Hours)

   FIGURE E-6   DIURNAL VARIATIONS IN
                1.1.1 -TRICHLOROETHANE
                LEVELS IN NEW YORK CITY
   26


1 22

I 18
"^
CO

I 14

J 10
 CO
    6
_


O
             Location: White Face Mountains
                     (Elev. 3000 FT)
                     N.Y. State 9/17/74
             CH3CCI3
                    L L  i L L_ i t
            60

            50

            40

            30

            20

            10
     600   1000
                    1500   2000
                  Time (Hours)
2500  3000
   FIGURE E-7   1,1.1 - TRICHLOROETHANE LEVELS IN
                NON URBAN AREAS DUE TO TRANSPORT
                FROM URBAN AREAS
                    E-6

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       Over the past few years, atmospheric concentrations and emissions have
  North"  ^^ 1980)'  ^ the 1975'77 Peri°d' concentrations In the
  Northern Hemisphere at temperate latitudes increased at 12-17%/yr
  (Singh |t al. 1980,  Singh  et  al.  1978,  Singh  et al.  1979),  a
  a somewhat lower rate than expected (Singh et "al~ 978) .  Emissions
  growth over the same period was also exponential (Singh et al. 1978) with
  available emissions data indicating about 15-25%/yr (SinglT eT al. 1979)
  On the basis of these observations, it appears that atmosphe7i~con-
  centrations have not increased as rapidly as emissions.  Figures E-8
  fc-y,  and E-10 show atmospheric concentrations  as a function of time.'

    _   The long tropospheric  lifetime of the chlorinated compound 1,1  1-
  trichloroethane and the  past  and  continuing  dispersive losses  are of
  possibly serious significance (Altshuller 1980,  Hanst 1978).   From 12 to
  (ILlt  8i  ?  hl'r,l~^±ChlOTOethane ^ssions  may reach the stratosphere
  (Singh  e^ al.  1980,  Singh et  al.  1979),  where  Cl atoms may  be  released bv
  photolysis  to  attach  and  deplete  ozone (Hanst  1978, Lillian et  al. 1975,'
                                      ,
98°Neely ^ A§in 198°'  SinSh et al.  1979,
                                                                     and
   Mff          v                                       ,
  Schiff  1978    The  ozone  situation  can  be  put  into  perspective  by  com-
  parison of 1,1,1-trichloroethane with the  chlorofluoromethanes  (CFM's)
  The annual stratospheric  flux of chlorine  atoms due to  1,1,1-trichloro-
  ethane  is about ten times less than the flux due to Freon-11 and Freon-12

  t!ke L*5S  ^       ^ ,/3Sed °n SeVeral reaS°na ble ^sumptions, it would
  the Jf   ,-7?ar8iaV 67'^ 1,1,1-trichloroethane growth rate to reach
  ^Mnrn  !t     Ve u°f °Z°ne dePletion ^ CFM.  The amount of 1,1,1-tri-
  chloroethane reaching stratospheric 0.  may be  less  than 6-12% of yearly
  emissions since in the lower stratosphere',  [OHJ is  high enough and dif-
  fusion and mixing to the stratosphere is sufficiently slow so that more
  1,1,1-trichloroethane than previously estimated (the 12-25% reported bv
  Singh et £.  1979)  may degrade due solely to tropospheric reactions be-
 dpn^J6   ^Jn ?! stratosPhere and ^e 03 layer.   The steady state ozone
 depletion (A03)  due to CFM release at  1973 levels is estimated to be 6.6-
 7.5^ of the unperturbed  value (McConnell and Schiff 1978).   When 111-
 trichloroethane  is  added to  the  calculations,  the steady state A03'is
 7.8    an increase of 20% over the  6.6% AOo.  If steady-state CFM levels

                 ~
           U                                            A03 decrease
           With a release schedule of 1,1,1-trichloroethane added (10%/
 year  increase  until  1982,  then 7%/year  until  1990),  A03 goes  to  4.6%  a
 HU/s increase.
     Crutzen  et al.  (1978) have  simulated  ozone  depletion  due  to many
chlorinated compounds in  the atmosphere.   According  to  their calculations
1,1,1-trichloroethane in  1978 was contributing about 0.2%  reduction in
total ozone.  Estimates of future ozone reductions due  only to 1,1 1-
trichloroethane use and release  increases  of 13%/year arTthown in
Figure E-11.  Other curves for other chlorinated chemicals are also
shown for comparison.

     Since 1,1,1-trichloroethane has a relatively short lifetime in the
atmosphere when compared with CFM's, it would contribute little to Q\
depletion 25 years after termination of emissions.   This is due to the
                                   E-7

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_   s.
CC


C
'x

i
o
u
 n

o
8
,
tr
                             I
       JULY
              1977
            —,	1	1         I

            OCTOBER    JANUARY   APRIL     JULY

                          	  1978
                                                      OCTOBER  JANUARY
                    -H
      Source: Cronn (1980)



      FIGURE E-8  WEEKLY AVERAGES FOR CONTINUOUS GROUND MONITORING OF

                  1.1,1 - TRICHLOROETHANE LEVELS. JUNE 1977 - JANUARY 1979,

                  47° N LATITUDE. EASTERN WASHINGTON STATE
             2001
100-
| 50-

oe
z
10-
f
g *

2
1
l<


NORTH :j
•1
•.
•
SOUTH •



>70 19

ssrf
;jS!||||?f:*
; •;. .:".::"-::-.-"T"
• • ••.."• ° X ?
—
i
l
0
o

72 1974 1976
YEAR
S^ '.'.••'.".•• "


/•e/^uu
CRVHrl
LOVELOCK
RASMUSSEN
ROBINSON
ROWLAND
SINGH

1978 I960

             Source: Cronn (1980)
             FIGURE E-9   OBSERVED NH AND SH MIXING RATIOS OF

                          1.1.1 - TRICHLOROETHANE LEVELS, 1972 - 1978
                                  F-R

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       Source: Various data cited by Neely and Agin (1980)
FIGURE E-10  ATMOSPHERIC LEVELS OF 1,1,1 - TRICHLORETHANE
             1972 - 1978. NORTHERN HEMISPHERE
       1940    1960
1980
                              2000   2020    2040   2060
             Loss due to
             C2H5CI3 on|V
                     10
  18
                          Year
     Source: Crutzen et al. (1978)
  FIGURE E-11  TOTAL OZONE LOSSES FOR VARIOUS SCENARIOS

                       E-9

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tropospheric sink rather than a stratospheric sink, where most ozone is
found and where Cl release is of more concern.

     For the reasons discussed above, 1,1,1-trichloroethane may con-
tribute to ozone destruction, but at a level less than that of the
chlorofluoromethanes.
                                  E-10

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                                   REFERENCES

                                           of trace gases
                          _ cu aurma rue -r,-.
          Washington,  B.C.:
                                      ._..„	«„	._  . ,             ^  i97g^
                                           :^
 and other halocarbon poUutants     a    I ?" On ""y^hlorofonn
 vironmental Protection Agency  i980a?      Trian§le Park' NC:  U'S' ^n-
         n              o.
 363, 1978.  (As cited by C^n ^80?.*
                                                      to esma
 on inethylchloroform and other  fialocarbon  ^ i  r°Ceedlng of the conference
 Park,  NC:   U.S.  Environoental
    	     ' =i-u«*nes, propanes  and nrnn i     f     	 -«•«.=.« WJ.
solutions.  Comparisons with th^nr**-!,. i  py^fnes from dilute aqueous                 f
Tech. 405-409, 1976.         theoretical predictions.  Environ. Sci.

Hanst, P.L.  Noxious trac  o-
lutants.   Chemistry 51(2):   6-12  lQ7fl     '            Halogenated pol-
                                                                                      L
                                  E-ll

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Lillian, D.; Singh, G.B.; Appleby, A.; Lobban, L-;Arats, R.jGumpert, R. 5
Haque, R.;Tooney, J.; Angell, M.;  Hansen, D.; Scott, B.  Atmospheric fate
of halogenerated compounds.  Environ. Sci. Tech. 9:  1042-1048, 1975.

McConnell, J.C.; Schiff, H.I.  Methylchloroform:  Impact on stratospheric
ozone.  Science 199:  174-177, 1978.

Neely, W.B.; Agin, G.  Environmental fate of methylchloroform.  EPA.600/9-
80-003.  Proceedings of the conference on methylchloroform and other halo-
carbon pollutants.  Research Triangle Park, NC:  U.S. Environmental Pro-
tection Agency, 1980.

Rowland, F.S.  Status of the stratospheric ozone depletion issue, including
comments on methylchloroform. EPA 600/9-80-003.  Proceedings of the
conference on methylchloroform and other halocarbon pollutants.  Research
Triangle Park, NC:  U.S. Environmental Protection Agency, 1980.

Singh, H. B.; Fowler, D.P.; Peyton, T.O.  Atmospheric carbon tetrachloride:
another man-made pollutant.  Science 192:  1231-1234, 1976.  (As cited by
Singh ejt al. 1980).

Singh, H.B.; Salas, L.J.J Cavanaugh, L.A.  Distribution sources and sinks
of atmospheric halogenated compounds.  J. Air. Pollut. Control. Assoc.
27:  332-336, 1977.

Singh, H.B.', Salas, L.J.,'.Shigeishi, H. J Scribner, E.  Atmospheric
halocarbons, hydrocarbons, and sulfur hexaflouride:  global distributions,
sources, and sinks.  Science 203:   899-903, 1979.

Singh, H.B.', Salas, L.J.', Shiseishi,  H.', Smith, A.H.  Fate of halo-
genated   compounds in the atmosphere.  Menlo Park, CA:  Stanford Research
Institute, 1978.  Available from NTIS PB 2781980.

Singh, H.B.; Salas, L.J.,* ShigeishI,  H.  Halogenated trace constituents
in the global environment.  Proceedings of the conference on methylchloro-
form and other halocarbon pollutants.  Research Triangle Park, NC:  U.S.
Environmental Protection Agency, 1980.

Spence, J.W.; Hanst, P.L.  Oxidation of chlorinated ethanes.  J. Air.
Pollut. Control. Assoc. 28:  250-253, 1978.

U.S. Environmental Protection Agency  (U.S.EPA).  Proceedings of the con-
ference on methylchloroform and other halocarbon pollutants.  Research
Triangle Park, NC:  Office of Research and Development, U.S. Environmental
Protection Agency, 1980.
                                   E-12

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