United States
Environmental Protection
Agency
Effluent Guidelines Division
WH-552
Washington DC 20460
Development
             I!
Document f|>r Effluent
Limitations Guidelines
and Standards for the
             ii
Organic Chemicals
and Plastics! and
Synthetic Fibers
EPA 440/1-83/009-b
February 1983
Point Source Category
Volume III (BAT)

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                  DEVELOPMENT DOCUMENT

                          for

         PROPOSED EFFLUENT  LIMITATIONS  GUIDELINES
                          AND
             NEW SOURCE PERFORMANCE STANDARDS

                        FOR THE

ORGANIC CHEMICALS AND PLASTICS AND SYNTHETIC FIBERS  INDUSTRY



             VOLUME   III   (BAT)
                     Anne M. Burford
                     Administrator
                Frederic A. Eidsness, Jr.
            Assistant  Administrator for Water

                Steven Schatzow, Director
        Office of Water Regulations and Standards

                Jeffery D. Denit, Director
               Effluent Guidelines Division

          Devereaux Barnes, Acting Branch Chief
                 Organic Chemicals Branch
                     Elwood H. Forsht
                     Project Officer
                      FEBRUARY 1983

               EFFLUENT GUIDELINES DIVISION
        OFFICE OF WATER REGULATIONS AND STANDARDS
           U.S. ENVIRONMENTAL PROTECTION AGENCY
                  WASHINGTON, DC  20460
                                 U.S. Environmental Protection Agency
                                 ?J*ion 5.Library (PJ.-12J)
                                 522 «?%&12th

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                                   NOTICE        MAR 31 1983
     On February 28, 1983,  EPA proposed effluent  limitations  guidelines and



standards for the organic chemicals and plastics  and synthetic  fibers (OCPSF)



point source category.  The Federal Register notice of this proposal  was printed



on March 21, 1983 (48 F£ 11828 to 11867).







     Information received by the Agency after proposal indicates that the total



OCPSF industry estimated annual  discharges of toxic pollutants  are too high.



The Agency will be Devaluating these estimates when additional  information



becomes available prior to  promulgation of a final  regulation.   In the interim,



the Agency advises that there should be no reliance on the annual  total toxic



pollutant discharge estimates presented in the Federal Register notice, the



February 1983 OCPSF Development Document,  and February 10, 1983 OCPSF Regulatory



Impact Analysis.
         n^T Protection

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                       VOLUME   III   (BAT)
                            TABLE OF CONTENTS
APPENDIX
                                                       PAGE
APPENDIX A:

APPENDIX B:


APPENDIX C:
SAMPLE 308 QUESTIONNAIRES

CHEMICAL PRIORITY LIST  FOR SCREENING
AND VERIFICATION SAMPLING PROGRAMS

ANALYTICAL METHODS  DEVELOPMENT
AND REVIEW OF DATA

I.    INTRODUCTION                                    C-1

     A.   General                                       C-1

     B.   Quality Assurance/Quality Control               C-1

     C.   Wastewater Analysis in the OCPSF Industry       C-2

     D.   Available Analytical Methods                     C-3

II.   ANALYTICAL METHODOLOGIES AND QA/QC
       FOR THE BAT STUDY                            C-3

     A.   Screening Phases  I and II                       C-9

          1.  Analytical Methods                          C-9
         2.  Quality Assurance/Quality  Control            C-10

     B.   Verification Phase                              C-13

          1.  Background                                C-13
         2.  Analytical Methods                          C-14
         3.  Quality Assurance/Quality  Control            C-20

     C.   CMA  Five-Plant Study                          C-22
                    REVIEW OF DATA FROM SAMPLING STUDIES

                    A.  Introduction

                    B.  Screening  Phases I  and II

                        1.  Description of the Review
                        2.  Use of Phase I and II  Data
                                                       C-23

                                                       C-23

                                                       C-24

                                                       C-24
                                                       C-25
                                  Ill-i

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APPENDIX
APPENDIX D:


APPENDIX E:

APPENDIX F:
                             TABLE  OF CONTENTS
                               (continued)
      C.   Verification  Phase

          1.  Background
          2.  1982  Data Review by Original Contract
                Laboratories
          3.  Results of the  Review
          4.  Effect of the Review on the OCPSF
                Industry Database

      D.   CMA  Five-Plant Study
          1.  Description of the Review
          2.  Transcribing and Encoding Errors
          3.  Errors from Improper Application of
                 GC/CD  Methods

 REFERENCES

ACTIVATED CARBON AND STEAM
STRIPPING QUESTIONNAIRES

TREATABILITY STUDIES

STATISTICAL DETAILS AND DEVELOPMENT
OF VARIABILITY FACTORS

      A.    Formulas and Definitions
      B.    Rationale for Using Daily Sample Averages
           in Modeling -Effluent Variability
      C.    Goodness-of-Fit Tests
      D.    Derivation  of Variability Factors
      E.   Example of Variability Factor
           Calculations
      F.   Subcategorization
      References
PAGE

C-25

C-25

C-25
C-26

C-27

C-27
C-27
C-27

C-28

C-33
                                                                      F-1

                                                                      F-2
                                                                      F-8
                                                                      F-9

                                                                      F-14
                                                                      F-18
                                                                      F-32
APPENDIX G:


APPENDIX H:
CHEMICAL TREES OF THE  GENERALIZED
PLANT CONFIGURATIONS (GPCs)

HEALTH  AND  ENVIRONMENTAL EFFECTS OF
PRIORITY POLLUTANTS

A.  General
B.  Priority Pollutants
    1.  Volatile Organic Compounds
    2.  Acid Extractable Organic Compounds
    3.  Base/Neutral Extractable Organic
         Compounds
    4.  Metals  and Cyanide
                                                                      H-l
                                                                      H-1
                                                                      H-1
                                                                      H-28

                                                                      H-38
                                                                      H-74
                                  Ill-ii

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APPENDIX

APPENDIX I:


APPENDIX J:
                             TABLE OF CONTENTS
                               (continued)
FATE OF PRIORITY POLLUTANTS IN PUBLICLY
OWNED TREATMENT WORKS:  EXECUTIVE SUMMARY

TREATMENT CATALOGUE FOR THE  CATALYTIC
COMPUTER MODEL
                                                        PAGE
APPENDIX K:  DESCRIPTION  OF MODEL COMPONENTS AND USE

              A.  Permanent Files
                  1.  Master Process File
                  2.  Parameter and Treatment Selection File
                  3.  Effluent Target File
                  4.  Unit Process Sequence Rules File
                  5.  Plant Adder File
                  6.  Capital Costs File
                  7.  Operating Costs  File
                  8.  Cost Allocation Rules File
              B.  Treatment  Technology Program Modules
              C.  Model  Logic Control  Programs
                  1.  Model Run Modes
                     a.   Model Selection Run Mode
                     b.   Specified Unit Process Train
                           (SUPT) Mode
                  2.  Subsequent Steps for Both Modes
                                                        K-1
                                                        K-1
                                                        K-2
                                                        K-3
                                                        K-3
                                                        K-3
                                                        K-3
                                                        K-4
                                                        K-4
                                                        K-4
                                                        K-7
                                                        K-11
                                                        K-11

                                                        K-11
                                                        K-11
                                 Ill-iii

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                                LIST OF  TABLES
TABLE                            TITLE                                  PAGE

C-1           Characteristics of Analytical Methods Used
                for the OCPSF Industry Sampling Phases                   C-4

C-2           Analytical Methods Used  During the Verification
                Phase                                                     C-17

F-1           Comparison of Standard Deviations  Estimated by
                Two Methods                                              F-6

F-2           Goodness-of-Fit Tests for Variability Data:
                Log  (C-D) for Daily  Averages C over D  yg/fc              F-10


F-3           Values of C  and X for 1,2-Dichloroethane Results             F-15

F-4           Principal  Component Weights for Organics Data                F-25

F-5           Principal  Component Weights for
                Metals/Cyanide Data                                       F-27

F-6           Comparison of Plastics-Only Plants  with
                Other  Plants                                              F-28

F-7           Comparison of Organics-Only Plants with Mixed
                Organics/Plastics Plants                                   F-30

F-8           Comparison of Three BPT Subcategories for
                Not Plastics-Only Plants                                   F_3-j

K-1           Cost Factor  for Each  Element  in Operating
                Cost File                                                  K_5

K-2           Operating Cost File Unit Costs                               K_g

K-3           Cost and Scale Factors for Each  Unit Process                  _
                                    Ill-iv

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                              LIST OF FIGURES


FIGURE                           TITLE                                PAGE

C-1          Comparative Chronologies of OCB and EMSL Method
                Validation  Programs                                      C-15

C-2          Verification Quality Assurance/Quality Control
                Program                                                 C-21

K-1          Schematic of Major Model Components                         K-9
                                   Ill-v

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                             LIST OF EXHIBITS








EXHIBIT                         TITLE                                PAGE



C-1          Organic Chemicals Verification (OCV) Program                C-29
                                   Ill-vi

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      APPENDIX A
SAMPLED .308_QUESTJONNAI RES

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308 BPT QUESTIONNAIRE
          A-l

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       UNITED STATES ENVIRONMENTAL PROTECTION AGENCY
                      WASHINGTON. D.C. 20460
                                                OFFICE OF WATER AND
                                                HAZARDOUS MATERIALS
As you may be aware, we are in the process of reconsidering
and re-issuing regulations with respect to water pollutants
discharged as a result of the manufacture of organic
chemicals and plastics and synthetics.  The earlier
regulations were issued as 40 C.F.R. Parts 414 and 416,
respectively.

The reconsideration of organic chemicals is a result of a
joint stipulation filed in the Fourth Circuit Court of
Appeals entered into on behalf of companies in the industry
and the Environmental Protection Agency.  The stipulation
requires the Agency to obtain new and more reliable data and
requires the industry to cooperate in the gathering and
furnishing of data necessary to formulate regulations for
the organic chemicals manufacturing point source category.

The reconsideration of plastics and synthetics results from
the remand by the Fourth Circuit Court of Appeals of the EPA
regulations promulgated on April 5, 1974.  The Court ordered
the EPA to restudy areas where the record was ruled to be
inadequate.

To complete these reconsiderations, the Agency is collecting
additional information on the production processes, raw
waste loads, treatment methods and cos'«, and effluent
quality associated with the manufacture of these materials.
The Environmental Protection Agency is no* soliciting your
cooperation in obtaining the necessary information.
                             A-2

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According to our records/ your Corporation produces one or
more of the products on the attached list(s)  (Part I), which
were covered by the referenced regulations.  For the
plastics and synthetics category, plants that solely
purchase polymer, resin or fiber to manufacture finished
plastic components should return the enclosed forms
unanswered and state this reason.  Plants that manufacture
plastic components in addition to the polymer, resin or
fiber should list the manufactured components as "other
products" in the appropriate section and complete} the forms.

The information requested shall be provided for each plant
of your firm in the format of the attached portfolios.  This
will allow the Agency to correlate and make available to
interested parties the results of the data gathered.  If our
records are incorrect and you do not feel that the requested
information is related to your plant (i.e., you no longer
manufacture the products listed or do not produce them at
this site), please inform us as soon as possible.  In order
to expedite the process we have sent a copy of this letter
to those individuals and plants of your firm as noted on the
attached list.

The information requested in this letter and the enclosed
data collection portfolio is sought pursuant to Section 308
of the Federal Water Pollution Control Act Amendments of
1972.  That section authorizes this Agency, whenever
required for developing any effluent limitation, or other
limitation, prohibition, or effluent standard, pretreatment
standard, or standard of performance under this Act, to
require the owner or operator of any point source to
establish and maintain such records, make such reports,
install, use and maintain such monitoring equipment or
methods (including where appropriate, biological monitoring
methods), sample such effluents (in accordance with such
methods, at such locations, -at such intervals, and in such
manner as the Administrator shall prescribe),  and provide
such other information as the Agency may reasonably require,
and to have access to and copy any records, inspect any
monitoring equipment and sample any effluents.
                             A-3

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Information requested pursuant to Section 308 may not be
withheld from EPA on the ground that it is considered to be
confidential or proprietary.  Section 308(b), however, does
accord protection to trade secrets.  Accordingly, please
indicate clearly on your response any information which you
consider to be confidential or to constitute a trade secret,
BO tnat the Agency may take appropriate protective measures.
Any information not so identified in your response will not
be accorded this protection by the Agency.   Effluent data
cannot be protected as trade secrets.  Any data may be
disclosed to officers, employees, or authorized
representatives of the United States concerned with carrying
out the Act or when relevant in any proceeding under the
Act.

For your convenience, a data collection portfolio has been
enclosed with this letter.  This form is divided into
several parts.  Those parts that are applicable to your
operations should be filled out and returned to the Agency
as soon as possible but in no event later than sixty days
after receipt of the letter.

The parts contained in the data collection portfolio are as
follows:

         Part X.   General Information
         Part II.  Water Use, Reuse and Discharge
         Part III. Treatment Technology

Please answer all items.  Also, please provide a separate
set of responses for each plant.  The purpose of this
request is to gather all available, pertinent information
and is not designed to create an undue burden of sampling
requirements on your plant personnel.  If a question is not
applicable to a particular facility, indicate by writing
"Not Applicable".  If an item is not known, indicate unknown
and include an explanation of the reason for not knowing
such information.  If an item seems ambiguous, complete as
best as possible and state your assumptions in clarifying
the apparent ambiguity.  Also, submit copies of the summary
                             A-4

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data sheets compiled or used in completing the tables in
this form.

The Agency will review the information submitted and may, at
a later date, require site visits and additional sampling in
order to complete the data base.

Thank you in advance for the cooperation of your company.
The Environmental Protection Agency is committed to
promulgating effluent regulations which are in accordance
with the Federal Water Pollution Control Act and which are
reasonable.  The Agency has found that only with complete
cooperation of all parties concerned can thoughtful and fair
regulations be published.  Z am confident that we can
anticipate your assistance in carrying out that goal.

Should you have any questions regarding this request, please
do not hesitate to contact Lamar Miller with respect to
organic chemicals at (202) 426-2582 or Michael Kosakowski at
(202) 426-4617 with respect to plastics and synthetics.

Sincerely yours,
Robert B. Schaffer
Director
Effluent Guidelines Division (WH 552)

Enclosures
                             A-5

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ORGANIC CHEMICALS OR PLASTICS AND SYNTHETICS (Identify Category)
PART Z                  GENERAL INFORMATION
To be returned within 60 days of receipt to:
                               Robert B. Schaffer, Director
                               Effluent Guidelines Division
                               U.S. EPA (WB-552)
                               Washington, D. C. 20460

1.  Name of Corporation

2.  Address of Corporation Headquarters
    Street:	
    City:	
    State;                             Zip Code
3.  Name of Plant
4.  Address of Plant
    Street:	
    City:	
    State:	 2ip Code
5.  Name(6) of corporation personnel to be contacted for information
    pertaining to this data collection portfolio.
    Name                       Title                 fArea Code) Telephone
6.  Plant NPDES Permit Number (s)
    Date of expiration ____
    If no permit, application number
    Date of application 	
                                    A-6

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                                Corporation
                                Plant	
                                Citv                     State

7.  Products produced at this plant site.

a.  Indicate which of the products in list 1 (Plastics and Synthetics-
page 3) or list 2 (Organic Chemicals-page 4)  that you produce at  this
site  and  the  production  rate  during the period January 1, 1975 to
September 30, 1976.  If there is more than  one  process  type  for  a
given  product,  identify and list each separately.  The average daily
production while operating should match  with  the  waste  water  data
tables in Part II.
                                                  Avg. Daily
                                                  Production   Year
                                        Design      While     Process
Product           Process               Capacity  Operating  Installed
                                        Ibs/day    Ibs/day
Attach additional pages, if necessary.
                                          A-7

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                                LIST 1

                        PIASTICS g SYNTHETICS
ABS/SAN
Acrylic Resins
ADcyds and Unsaturated Polyester Resins
Cellulose Acetate Fiber/Resin
Cellulose Derivatives
Cellulose Nitrate
Cellophane
Epoxy Resins
£thylene-Vinyl Acetate Copolymers
Fluorocarbon Polymers
Melamine Resins
Nylon Resins/Fiber
Phenolic Resins
Polyamides
Polyester Resin/Fiber
Polyethylene
Polypropylene Resin/Fiber
Polystyrene
Polyurethane Resins
Polyvinyl Acetate
Polyvinyl Chloride
Rayon
Si li cones
 rea Resins
                                    A-8

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                                LIST 2

                          ORGANIC CHEMICALS
Aeetaldehyde
Acetic Acid
Acetone
Acetylene
Acrylates  (includes acrylic add,
 methacrylie acid, and esters)
Acrylonitrile
Adiponitrile
Aniline
Benzene
Benzole Acid
Bisphenol A
Caprolactam
Chloromethanes  (Methyl Chloride,
 Dichloromethyl, Chloroform, and
 Carbon tetrachloride)
Citronellol
Coal Tar
Cumene
Cyclohexane
Dimethyl Terephthalate
Diphynylamine
Ethyl Acetate
Ethyl Benzene
Ethylene
Ethylene Dichloride
Ethylene Glycol
Ethylene Oxide
Formaldehyde
Bexamethylenedianine
Isobutylene
Isopropanol
Maleic Anhdride
Methanol
Meta-Xylene
Methyl Amines  (including mono,
 di, and tri methyl amine)
Methyl Ethyl Ketone
Methyl Salicylate
Ortho-Nitroaniline
Ortbo-Xylene
OxoChemicals
Para-Ajninophenol
Para-Cresol
Para-Mi troaniline
Para-Xylene
Phenol
Pbthalic Anhydride
Plasticizers (esters of
 phthalic acid)
Propylene
Sec-butyl-alcohol
Styrene
Tannic Acid
Terephthalic Acid
Tetraethyl Lead
Toluene
Vinyl Acetate
Vinyl Chloride
                                     A-9

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                                Corporation
                                Plant	"m
                                City	
State
c.  Indicate which of the products in list 3 (Organic Chemicals - page
6) that you produce at this site and the production  rate  during  the
period  January  1r 1975 to September 30, 1976.  If there is more than
one process type for a given product, identify  and  list  separately.
The  average  daily  production  while operating should natch with the
waste water data tables in Part II.

                                                  Avg.  Daily
                                                  Production   Year
                                        Design      While     Process
Product           Process               Capacity  Operating  Installed
                                        Ibs/day    Ibs/day
Attach additional pages, if necessary.

                                  A-10

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                                LIST 3

                          ORGANIC CHEMICALS
Proplyene Oxide
Acetic Anhydride
Ethyl Alcohol, Synthetic
Adipic Acid
Cyclohexanone
Nitrobenzene
Tetrachloroethylene (Perchloroetbylene)
Propylene Glycol  (1,2-Propanediol)
Diethylene Glycol
Tri chloroethy1ene
N-Butyl Alcohols  (N-Propylcarbinol)
Di chlorodifluoromethane
Ethanolamines, Total
Trichlorofluoromethane
4,U-Isopropylidenediphenol  (Bisphenol A)
2-Methoxyethanol  (Ethylene Glycol
  Monomethyl Ether)
2-Aminoethano1  (Monoe thanolamine)
Cresols, Total
Epoxidized Esters, Total
2,2-Zminodiethanol (Diethanolamine)
Trietbylene Glycol
Pentaerythritol
Eexamethylenetetramine, Tech*
Ortho-Dichlorobenzene
a-Chlorotoluene  (Benzylchloride)
Funaric Acid
Dipropylene Glycol
Glutamic Acid, Monosodium Salt
Choline Chloride  (All Grades)
Para-Nitrophenol and Sodium Salt
Pentachloropbenol  (PCP)
Propionic Acid
Xylenesulfonic Acid, Sodium Salt
Aspirin
Acetic Acid Salts, Total
Methyl Bromide
Dodecyl Mercaptans
Salicylic Acid
Benzole Acid Salts:  Sodium Benzoate, tech.
  and U.S.P.
5-Nitro-Ortho-Toluenesulfonic Acid  (SO3H-1)
Benzyl Alcohol
Benzoyl Peroxide
Castor Oil, Ethoxylated
2-Ethylhexanoic Acid (a-Ethylcaproic Acid)
2-£imethylaminoethanol
                                    A-ll

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                                Corporation
                                Plant	"
                                City	 State.
,-.  List below all other products (not appearing on lists 1, 2  or  3}
manufactured  at  this sane site that account for at least one percent
of the plant* s total production.  Minor products  may  be  grouped  in
this  listing  if  the  products  are  similar in nature and made by a
similar process.  The products should be listed  individually  with  a
total  production  indicated  for  the  group  in  all instances where
grouping is used to report.
                                                           Avg. Daily
                                                           Production
                                                 Design      While
Product                 Process                  Capacity  Operating
                                                 Ibs/day    Ibs/day
                                   A-12

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                                Corporation
                                Plant	"
                                City	 State.
d.  List below products not in items 7a, b and c if they  account  for
an  inordinate pollution load either in terms of pounds discharged per
1,000 pounds of production (RWL)  or difficult treatment problems.
8.  For each product indicated in response to Questions 7a and  7b  of
    Part  I,  attach  a process flow diagram which identifies the unit
    operations involved in each product manufacturing process and  all
    sources   and   quantities   of  waste  waters  from  the  process
    operations.  Show recycle loops for both process  water  and  non-
    contact  cooling  water  and specify the blowdown control systems.
    Indicate raw materials used  and  contact  and  non-contact  water
    entering  each  operation.   Identify  pollution  control  devices
    associated with the process that  have  wastewater  streams.    Use
    consistent  units  throughout;  for  example,   gallons per hour or
    pounds  per  hour.   Supplement  the  diagram  with  a   narrative
    description for clarity or completeness where necessary.

    The  respondent may use process flow diagrams from EPA Development
    Documents if representative of the process.  The process  diagrams
    should be modified to include all requested information.

    On  each  process  flow diagram, clearly state whether the process
    operational mode is batch, continuous or other.  If the answer  is
    •other*1  the operational mode should be specified.  If the process
    is batch or semi-continuous, describe  the  length  of  cycle  and
    frequency.

9.  Describe  major  process  modifications  made  (to  each   process
    described  in  response  to Question 6)  since January 1,  1972 that
    significantly affect either the volume of flow, or the  amount  of
    waste  water  pollutants  per  unit of production originating from
    that  process.   Explain  the  purpose  behind   each   of   these
    modifications.   Give  your  best estimate as to the technological
    age of each process installation as it now exists.

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                            Corporation
                            Plant	
                            ttty	 State.
Give an analysis of the effect of mafcing the  modification,  i.e.r
describe the load and flow prior to the modification and after the
modification.   Do  you  have  future  modifications  for in-plant
control of waste water  pollutants  scheduled,  if  so,  on  which
processes?   Specifically highlight any process changes that would
not be made  except  for  pollution  control.   Include  all  such
changes  in  the  process  flow diagram of Item 8 using a separate
block wherever feasible.
                               A-14

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                                Corporation
                                Plant	
                                City	 State.
 *GANIC CHEMICALS OR PLASTICS AMD SYNTHETICS (Identify Category)

 iRT II            HATER USE, RE-USE, AND DISCHARGE

 :>  be returned within 60 days of receipt to:

                               Robert Scbaffer,  Director
                               Effluent Guidelines Division
                               U.S.  EPA (WH-552)
                               Washington, D.  C.  20460


 •   Hater Use. Total Plant Needs During the Period
    January 1. 1975 to September 30. 1976


    List below for your plant the sources and quantities of water used
    and describe the disposition of  waste waters.   If a time period of
    less tban January 1, 1975 to September 30, 1976 is used, state the
    reason that the values used are  representative of that period.
    Hater Source:
                                                    Time Period
                                                    of Calculation
       Municipal 	 mgd (average value)
       Surface   	 mgd
       Ground    ________ »gd
       Other (specify)  	 mgd
3.   Uses:
       Non-contact cooling                   mod
       Direct process contact (as diluent, solvent,
         carrier,  reactant, by-product,
         cooling,  etc.)                 	mgd
       Indirect process contact (pumps,
         seals, etc.)                   	mgd
       Non-contact ancillary uses (boilers,
         utilities, etc.)               	mgd
       Maintenance, equipment cleaning
         and work  area washdown              mqd
       Air pollution control                 mod
       Sanitary and potable                  mod
       Other (specify)                 	mgd
                                   A-15

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                               Corporation
                               Plant	
                               Citv                     State.

j.  Source of waste water flows:

       Non-contact cooling                  mgd    ________
       Direct process contact                mad    _____
       Indirect process contact              mod    __.____.____,
       Won-contact ancillary uses            mad    _______
       Maintenance, equipment  cleaning
         and work area wasbdown              mod    _______
       Air pollution control                mad    ________
       Sanitary/Potable water                mad    _______
       Storm water (collected  in
         treatment system)                   mod    ________
       Other (specify)                      mod    _______
D.  Process or Process Contaminated Waste Water Discharged To:
      (Do not include cooling water,  boiler blowdown, etc.)

       Surface water or storm sewer
        Treated                             mad    __________
        Untreated                           mod    __________
       Municipal Sewage Treatment Plant     mod    _________
       Deep well                            mod    _________
       Other (Specify and describe          »od    ____________
        briefly)

2.  Quality of Water Discharged;

    For the period January 1, 1975 to September  30,  1976,  summarize
    your  influent,  effluent and raw waste loads in Tables A, fi, C, D
    and £.  If data for individual waste streams  are  not  available,
    information  for  combined waste  streams should be furnished which
    represents the greatest degree of detail  available.   The  tables
    are located at the end of this section.


    Instructions for Completing Tables AX B^ C^. D and jg:

    For  Tables  A,  fi,  C, D and £,  use the following definitions and
    notes.  The period covered should correspond with  that  used  for
    Part I question 7 to calculate average daily production.

         Flow - Do not include rainfall runoff, unless it is collected
         in  the treatment system. If, collected, estimate the percent
         of total flow which is attributed to this source.

         Average day - Should represent the average of the data period
         covered.

         Significant  parameters   -   Those  potential  pollutants  not
         specifically  listed, but which are introduced into the waste
         streams as a result  of   materials  used,  product  produced,
         process used and for which you have test data.

                                A-16

-------
                                Corporation.
                                Plant	
                                City	 State,
         Identify  all  data  which results from abnormal operating or
         other conditions.

         If use of a different time period  (a  portion  of  the  time
         period January 1, 1975 to September 15, 1976)  results in more
         adequate representation of the pollution loads,  you may do so
         if  the  time period is not less than six months.  You should
         specify the time period and explain why that period  is  more
         re pr e sen tati ve.

              Table  A - Complete Table A for the combined influent to
              each treatment facility.

              Table B - Complete Table  fi  for  each  untreated  waste
              discharge  point  (to  surface  waters, deep veils, land
              application, etc.)

              Table C - Complete Table C for the treated effluent from
              each treatment facility.  Hot applicable to plants  that
              have not yet installed waste treatment facilities.  This
              section is not restricted by type of treatment.

              Table  D  - Complete Table 0 for the process wastewaters
              from each of the  product/process  lines  identified  in
              Part  I,  items  7a  and 7b.  Do not include non-contact
              cooling  waters  but  do  include  all  contact  cooling
              waters.   If  measured  values  are  not  known  or  not
              available, ' supply  the  best  estimate  available   and
              specify  the  basis  for  the  estimate.  The production
              basis should be the same as the average daily production
              while operating that was given din Part Z.

              Table £ - Complete Table £ for the plant intake water.

3.  Attach the water analysis data summary sheets  shoving  the  daily
    water  analyses that were used to compute Tables A through £, e.g.
    monthly summary tables.  Also include  any  data  for  the  period
    January 1, 1975 to September 30, 1976 that was omitted in Tables A
    through £ as not being representative.

4.  The method of sample collection for the data supplied in  response
    to Question 2, Tables A, B, C, D and £, should be specified (e.g.,
    daily  grab  sample,  8  hour flow composited, 24 hour continuous,
    etc.).

5.  Indicate all parameters listed in Part II,  tables  A  through  Z,
    which were not measured by EPA approved methods.
                                A-17

-------
                                                           TAbLL A
                                             HASTE LOADS TO TFEATMI.KT
CIIY                    .              it«i*_
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           (••rcrd).
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                                             PtHy	    Hxathlv *¥tra»r«
     (HC»)
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            (*C)
            (*C) - A>ki«at Air
eoc
tec
T$*
 •2 M I
TC* •• I
•tk«r» (X««»ttfy)
                                                      A-18

-------
Corporal )»n_
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ili*tb«l(«  faint
•rot.*  p;*ck«t««  »«.
      frrl»J
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                                                             TA»I t.  f
                                             PVTft£*TEI> r-i'CCSS VATtK !.»»*» BIKCHAlCr.il
                             Air
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                   tlfc./^r)
                    CIH/4.T)
                                               P»H Y
                                                                        Caltudar
                                                                     Monthly Av«r»ge»
                                              A»«r«f .•   m»1«ufi
                                                                                          t»««rk«
                                                         A-19

-------
                                                           TAILI t
                                           TKCATcn Fkocii-k vAsrr. LOAU» nuriuKCED
CltT                                   *lBt»-
TrB«t»*Bt Facility __________________
T*BBtB»Bt Facility 6«»crlp»»»»_
•lackargc ?»l»t_
                                            TB«         If ?BI,  4o yBv chl»rlB«t«  ..   (A)  y»ll-Tl»«
                                            •e                                     __ (B)  r»rt-Ttl»«
                                                                  Mpnthlr Av«ta«»»
     (HCB)
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            (*C)
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    •• i 
-------
                                                           TADLC l>
                                            r«PBi'CT/r«nci.-r. LIKES «AV WASTI LOADS
CitT
                                  lt«tf_
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TIM
             OO IbO*
       Mica)
            (*C) -
            (*C) -
     (Ik./l.OOO ih.)»«
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XSS (lk«/i.OOO Iks)
TVS Uk
-------
                                                          TABI.C  I
                                                          IRTAKt VAlik
rt»c*»*
TIM »•
                                                                     Calendar
     CMC»)
   CM M
                           Alt
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TU •• K
•tk«r«
                                                   A-22

-------
                                Corporation
                                Plaint	
                                City	 State.
6.  fias the seed used in the BOD5 test been acclimated  to  the  waste
    waters that have been tested?
         	 Yes       	 No
    If yes, what is the source of the seed?
         A ___    sewage treatment plant
         fi __    plant treatment facility
         C __    laboratory acclimation
         D __    other explain ______.______________«.
                                    A-23

-------
                                Corporation
                                Plant	"
                                City	 State.
 ORGANIC CHEMICALS^OR PIASTICS AND SYNTHETICS (Identify Category)

PART III                TREATMENT TECHNOLOGY


To be returned within 60 days of receipt to:

                               Robert B. schaffer. Director
                               Effluent Guidelines Division
                               U.S. EPA (WH-552)
                               Washington, D. C.  20460
           have a treatment system(s) at this plant?
If yes, complete the following and attach a separate  flow  sheet  for
each  distinct  treatment  facility  indicating waste streams treated,
unit sizes of treatment equipment,  detention  times,  recycle  rates,
effluent   concentration   or  design  criteria  and  other  pertinent
engineering information  for  operation  of  the  treatment  facility.
Include treatment of storm runoff, where applicable.

*ndicate  the  process  lines for which any portion of the waste water
 xow is diverted to separate treatment, pretreatment or disposal (e.g.
deep well, solvent recovery, incineration, etc.).  Which portions  are
so diverted and which portions are combined for joint treatment?

For each treatment facility complete the following:

Name of Facility 	
Source(s)    of    Haste    Water
                                                      Cost f1976 dollars)
1   a.   Original installation
      (Battery limits of treatment plant only)
    b.   Other costs  (include collection
           system, piping, pumping, etc.)

2   Estimated replacement cost

3   Estimated total capital expenditure
      for this facility to date

    Annual cost of operation and maintenance 	
    (exclude depreciation and debt service cost)
    last major modifications or additions since original installation and
                                A-24

-------
                                Corporation
                                Plant	"
                                City	 State	

    state the purpose of the modification or addition.

                              Treatment                    Cost        Pur;
•iodification-Addition	  Facility	  Year   (1976 Dollars)
6   List scheduled modifications or additions and estimated date of complei
    and state the purpose of the modification or addition.

                              Treatment                    Cost        Purj
Codification-Addition	Facility	  Year   H976 Dollars)
7   is nutrient addition practiced:

    	 Yes  	 No

8   Bow many employees (equivalent man-years/year)  are primarily engaged
    as operators of the waste water treatment facility? (exclude maintenanc
    Bow many employees (equivalent man-years/year)  are engaged as support
    personnel for the waste water treatment facility?


9   Is an operator always present?

    	 Yes  	 No

10  Quantity of wastewater treatment facility solid wastes disposed
    of at present (dry basis)
                                        Ibs/dav

                                  A-25

-------
                                Corporation
                                Plant	"
                                City	State.

11  Moisture content of waste solids disposed of at present
                                        % moisture

12  Present disposition of solids
13  Estimated annual cost of solids handling and disposal (1976 dollars)
                                         S/ton dry basis

14  Planned future disposition of solids:
15  What are the total annual energy requirements for the treatment
    facility?
              Electrical         	Kwhr
              Other (e.g. Beat)             Btu

16  For discharges of industrial wastes to municipal treatment plants
    are there local pretreatment regulations applying to you?
    Yes 	  NO     .

    Zf yes, reference those regulations and attach a copy.
                                  A-26

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                               Corporation
                               Plant	"
                               City	 State	

j.   carbon Sorption Technology.

Jave you determined carbon  sorption isotherms
>n your waste waters?                                     .   ___
                                                      Yes   No
lave carbon sorption isotherms been determined
:or  waste waters  from  your  plant(s) by a person(s)
>ther  than company personnel?                          _   —_

iave you or anyone else  evaluated carbon
:olumns on waste  waters  from this plant?                __   ___

>o you have carbon sorption data from
rour plant (s) on:

    raw wastes                                         _   ___

    biologically  treated wastes                        ___   ___

    individual  process lines                           ___   __

    combined process lines                             ___   __

    pilot plant studies                                ^__   ^^^

    contractor  evaluations                             ___   __

    cost evaluations                                   ^^   _-

    plant scale evaluations                           ___   ___

    operational units                                  ___   __—>

 or  each question above  which was answered affirmatively*
 ive a brief description of the data  (source and  types of wastes,
 eriod of time  covered,  plant involved, extent of data base and
 ontact personnel suggested) in the space below.
                                    A-27

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                                Corporation
                                Plant	
                                Citv                     State

w.  Filtration

fiave you done filtration studies on your waste waters
(sand, multi-media, etc.) beyond what was described
in Section A, Part III?                          _ Yes    ___ Ho

If yes, give a brief description of the data (source and types of
wastes, period of time covered, process stream involved, extent of
data base and contact personnel suggested) in the space below.
    Biological Treatment

~~ive biological treatability studies been
  ^nducted on your wastewaters beyond what was
described in Section A, Part III?                 	Yes   	No

If yes, give a brief description of the data and results  (source and
types of wastes treated, duration of the study, extent of data base,
conclusions of study, and contact personnel suggested) in the space belov
£.   Save other treatability studies, beyond what
     vas described  in  Section A, Part III,  employing
treatment processes such as sedimentation, neutral-
ization, hydrolysis,  precipitation, oxidation/
reduction,  ion exchange, phenol recovery,  etc,,
heen run on any  of the process wastewater  streams
  om the plant?                                      __ Yes

If  yes, list  on  a  separate sheet  those product/process
streams from  which such treatability studies were conducted.
Identify the  sheet as response to III-E.
                                  A-28

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308 BAT QUESTIONNAIRE
          A-29

-------
      ,yp    UNITED STATES ENVIRONMENTAL PROTECTION AG€NCY

      ^                      WASHINGTON. D C. 20460
Dear Sir:

As you may be aware, we are in the process of reconsidering and re-
issuing regulations with respect to water pollutants discharged as a
result of the manufacture of organic chemicals and plastics and
synthetics.  The earlier regulations were issued as 40 C.F.R.  Parts
414 and 416, respectively.

The reconsideration of organic chemicals is a result of a joint stipu-
lation filed in the Fourth Circuit Court of Appeals entered into on
behalf of companies in the industry and the Environmental Protection
Agency.  The stipulation requires the Agency to obtain new and more
reliable data and requires the industry to cooperate in the gathering
and furnishing of data necessary to formulate regulations for  the
organic chemicals manufacturing point source category.

The reconsideration of plastics and synthetics results from the remand
by the Fourth Circuit Court of Appeals of the EPA regulations  promul-
gated on April 5, 1974.  The Court ordered the EPA to restudy  areas
where the record was ruled to be inadequate.

To Implement these reconsiderations, the Agency collected additional
information on the production processes, raw waste loads, treatment
methods and costs and effluent quality associated with the manufacture
of these materials in a data portfolio mailed to your company  on
October 18, 1976.  The Environmental Protection Agency is again solic-
iting your cooperation in obtaining information to supplement  those
data previously requested.  This portfolio seeks Information not
requested 1n the prior portfolio, particularly with regard to  the
presence or absence of the priority pollutants.

According to our records, your Corporation produces one or more of the
products on the attached list(s) (Part I) which were covered by the
referenced regulati ons.

The information requested shall be provided for each plant of  your
firm in the format of the attached portfolios.  This will allow the
Agency to correlate and make available to interested parties the re-
sults of the data gathered.  If our records are incorrect and  you do
not feel that the requested information is related to your plant
(i.e., you no longer manufacture the products listed or do not produce
them at this site), please inform us as soon as possible.  If  you have
supplied EPA previously with the information requested, you need not
do so again, however, please indicate to whom you submitted the data.

                                 A-30

-------
The purpose of this request is to gather all available, pertinent in-
formation and is not designed to create an undue burden on your plant
personnel.  Please return the portfolio to the Agency as soon as
possible, but in no event later than sixty days after receipt of the
letter.

For your convenience, the form is divided into three parts, with
descriptive headings and instructions for completing the portfolio.
Please answer all items in each part of the portfolio.  If a question
is not applicable to a particular facility, indicate by writing "Not
Applicable".  If an item is not known, indicate unknown and include  an
explanation of the reason for not knowing such information.  If an
item seems ambiguous, complete as best as possible and state your
assumptions in clarifying the apparent ambiguity.  Also, submit copies
of the summary data sheets compiled or used in completing the tables
in this form.

The Agency will review the information submitted and may, at a later
date, require site visits and additional sampling in order to complete
the data base.

Addenda A and B attached are a part of this letter.  They provide you
with information regarding the legal authority for requiring the com-
pletion of the portfolio and your options for requesting that certain
information be held confidential.

Thank you in advance for the cooperation of your company.  The
Environmental"Protection Agency is committed to promulgating effluent
regulations which are in accordance with the Federal Water Pollution
Control Act and which are reasonable.  The Agency has found that only
with complete cooperation of all parties concerned can thoughtful  and
fair regulations be published.  I am confident that we can anticipate
your assistance 1n carrying out that goal.

Should you have any questions regarding this request, please do not
hesitate to contact Paul Fahrenthold with respect to organic chemicals
at (202) 426-2497 or Michael Kosakowski at (202) 426-2497 with respect
to plastics and synthetics.
Sincerely yours,
Robert B. Schaffer, Director
Effluent Guidelines Division (WH-552)

Enclosures
                                    A-31

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                     ADDENDUM A:   AUTHORITY
This request for information is made under authority provided by
Section 308 of the Federal Water Pollution Control  Act,  33 U.S.C.
61318.  Section 308 provides that; "Whenever required to carry out the
objective of this Act, including but not limited to ...   developing
or assisting in the development of any effluent limitation .  . .
pretreatment standard, or standard of performance under  this  Act"  the
Administrator may require the owner or operator of any point  source to
establish and maintain records, make reports, install, use and
maintain monitoring equipment, sample effluent and provide "such other
information as he may reasonably require."  In addition, the
Administrator or his authorized representative, upon presentation  of
credentials, has right of entry to any premises where an effluent
source is located or where records which must be maintained are
located and may at reasonable times have access to and copy such
records, inspect monitoring equipment and sample effluents.
                                  A-32

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                    ADDENDUM B:   CONFIDENTIALITY
Information may not be withheld from the Administrator or his
authorized representative because it is confidential.   However, when
recuested to do so the Administrator is required to consider
information to be confidential and to treat it accordingly if
disclosure would divulge methods or processes entitled to protection
as trade secrets.  EPA regulations concerning confidentiality of
business information are contained in 40 CFR Part 2, Subpart B, 41
Fed. REG.  36902-36924 (September 1, 1976).  These regulations provide
that a business may, if it desires, assert a business  confidentiality
claim covering part or all of the information furnished to EPA.  The
n.anner of asserting such claims is specified in 40 CFR 82.203(b).
Information covered by such a claim will be treated by the Agency in
accordance with the procedures set forth in the Subpart B regulations.
In the event that a request is made for release of information covered
by a claim of confidentiality or the Agency otherwise  decides to make
a determination whether or not such information is entitled to
confidential treatment, notice will be provided to the business which
furnished the information.  No information will be disclosed by EPA as
to which a claim of confidentiality has been made except to the extent
and in accordance with 40 CFR Part 2, Subpart B.  However, if no claim
of confidentiality is made when information is furnished to EPA the
information may be made available to the public without notice to the
business.

Effluent data (as defined in 40 CFR 62.302(a)(2)) may  not be considered
by EPA as confidential.  In addition, any information  may be disclosed
to other officers, employees or authorized representatives of the
United States concerned with carrying out the Federal  Water Pollution
Control  Act or when relevant in any proceeding under this Act.
                             A-33

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         Instructions for Completing the Attached Questionnaire

Part I

1.  Questions 1 through 6:  You may have completed these items in response to
our previous industry survey.  If these items have changed please bring them
up to date.  In addition, indicate in Item 5 the location of the persons
familiar with your response to the questions.

2.  Question 7:  Lists 1, 2 and 3 on Pages 8, 9 and 10 represent the group of
products for which a limited data base exists.  In order to insure the con-
tinued usefulness of the existing data base, current production data for
existing and new plants producing chemicals on Lists 1, 2 and 3 is necessary.
The previous questionnaire required the reporting of all "minor" products
(defined as being greater than one percent of total production).  You are
now requested to report the production or use volumes of'all chemicals on
List 4, if they were not previously reported as greater than one percent of
total production, regardless of the production or usage rate.

Part II

1.  Tables A through E:  Place in the columns of the .tables labeled "Analytical
Results - Concentration ranges - parts per billion" the number of analytical
results which have been obtained, in the range indicated at the top of the
column.  The column labeled "Method" should be filled with the analytical
methodology used for the analyses.  (For example: gas chromatography,UV
spectrophotometry, IR spectrophotometry, NMR, or wet chemistry.)  It is not
essential to itemize each analysis.  If the number of analyses is greater than
100, estimate as accurately as possible the actual number of analyses.
Specify the concentration units used in completing the table - define all
abbreviations used.

Part III

For the purposes of Part III of the questionnaire the concept of a "set" of
effluent data will be very helpful.  A "set" of effluent data contains the
following items:

(1)  a list of all activated sludge plants located at a facility with the
product/process wastewater lines discharging to that facility clearly listed;

(2)  a summary of long-term data in the format as requested in Tables A and C
of this part (the last two pages of Part III): and

(3)  a short summary of specific wastewater parameters which are essential in
determining the effectiveness of the biological treatment plant at your facility.


                                    A-34

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The questions in this part are designed to supplement data previously supplied
by requesting all or parts of Items 1, 2 and 3 above.  The questions will
provide a means of effective performance evaluation of the existing waste-
water treatment plants.

1.  Question 2:  If you feel that recent production levels or wastewater
treatment plant data are mere representative than data included in your
previous submission you may submit a new set of data.

2.  Question 3:  In Part A, clarification is being requested to enable the
Agency to identify specific product/process wastewater lines entering
treatment facilities.  Fart B requests summer/winter performance data from
the plant to determine the effectiveness of the biological treatment system
in place.  The evaluation of treatment effectiveness is necessary to establish
the effect of operating conditions on the cost of waste treatment.

3.  Question 4:  For new plants or modified plants, a full set of information
is requested.

Example tables are attached for reference.
                                  A-35
                                    ii

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                                 EXAMPLE TABLE A,B,C,D or E.

PRIORITY
POLLUTANT
BENZENE
ETHYLENE
DI CHLORIDE

CHROMIUM
CHROMIUM






UNITS
PPM
PPM

PPM
PPB






CONCENTRATION RANGES
CIO
2
3

0
6






10-100
25
2

5
1






100-1000
20
6

6
0






>1000
1
2

2
0







ANALYTICAL METHOD
GC-Flame Detector
GC-EC Detector

Atomic Absorption
Wet Chemical - SULFATE






NOTE:  For Units, use standard wastewater abbreviations, such as:

       parts per million - ppm
       parts per billion - ppb

Line 1 indicates 48 analytical results in the ranges shown.
                                          A-36
                                             iii

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                           EXAMPLE RESPONSE TO QUESTION 7d
la
Product/
Process Line
Aromatics
Aklylation

Description of the Process
Modification or In-Process
Control
Steam stripper installed
on raw waste line to
treatment plant.
Intended Objective of
the Modification or
Control System
remove benzene, toluene,
xvlene, ethylbenzen* to
ppm level.
b  Quantify the results of the use of the Modification or PC System
Parameter
Benzene
Toluene
Xylene
Effluent Parameter
Value Before Modification
40 ppm, 25 gpm
60 ppm, 25 gpm
10 ppm, 25 gpm
Effluent Parameter
Values After Modification
5 ppm, 20 epm
2 ppm, 20 gpm
10 ppm, 20 gpm
   Repeat the above table for each modification
a


b Parameter







Effluent Parameter
Value Before Modification







Effluent Parameter
Values After Modification




  +Flow and concentration if possible
                                        A-37

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308 LETTER QUESTIONNAIRE FOR THE ORGANIC CHEMICALS AND PLASTICS AND
SYNTHETICS MANUFACTURING POINT SOURCE CATEGORIES
PART I
GENERAL INFORMATION AND PRODUCT-PROCESS INFORMATION
To be returned within 60 days from date of receipt to:
                                                  Robert B.  Schaffer,  Director
                                                  ATTN:   P.  D.  FahrenthoLd
                                                  Effluent Guidelines  Division
                                                  U.S.  EPA (WH-552)
                                                  Washington, D. C.  2046-)
1.   Name of Corporation
     Address of Corporation Headquarters

     Street:
     City:
     State:
     Name of Plant
                                             Zip Code:
     Address of Plant

     Street:	

     City:	
     State:
                                             Zip Code:
     Name(s) of personnel to be contacted for information pertaining to this data
     collection portfolio
                                                                        Location
     Name and Title                               Telephone           (plant or Cor?.
                                       A-38

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                                        Corporation_
                                        Plant
                                        City	State
Plant NPDES Permit Number^

Date  of Exoiration
If No Permit, Application Number_

Date of Application	
This question consists of four parts, some or all of which may apply to your
facility.  The parts of the question are labeled i through iv, corresponding
to questions 7a, 7b, 7c and 7d.  Where questions relate to Lists 1, 2, or 3
an update of the previously submitted portfolio (October 18, 1976) is intended
The heading beside the question and the Instructions provide more detail re-
garding the intent of the questions.

Has your plant (since October 18, 1976)

  i. Added new production processes for chemicals on Lists 1, 2, 3, or does it
     use or produce either as a product, by-product or intermediate any
     chemical on List A.

 ii. Changed design production capacity or average daily production ay
     means of debottlenecking, removal/replacement of process equipment,
     etc.

iii. Discontinued production process(es) that is(are) on Lists 1, 2 or
     3 (see Part I, Pages 7, 8 and 9).

 iv. Installed any new process modifications or  in-plant controls which
     affect raw waste characteristics.


    II  None Apply.              Proceed directly to Part II.


    1   1  Some or all Apply.       Continue through Part I.


    I   J  The data submitted in response to the October 18, 1976, request
          substantially represents current plant operations.  Proceed to
          Question 1, Part II.
                                A-39

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                                             Corporation
                                             Plant	~
                                             City	
                                              State
7a.  If your facility has added the production Of new processes for chemicals on
     Lists 1, 2 or 3, please coraolete the table below using the units indicated.
Product
Process
  Design
 Capacity
(Ibs/day)
Avg. Daily
Production
  While
Operating
(Ibs/day)
   Date
  Process
 Installed
Ciear.  Month)
Attach additional pages, if necessary.
                                       A-40
                                 PART I - Pace 3

-------
                                              Corporation
                                              Plant	~
                                              City	
                                               Stats
 7a.   (Continued)
      Do you produce as a product or intermediate,  consume, package or use* as a
      diluent,  solvent, raw material (feedstock)  or intermediate in any narmer
      other than in laboratory research or analytical programs any of the 129
      priority  pollutants (see Part II, Pages 2 and 3) which were not reported
      in the previous questionnaire dated October 18, 1976?  If so, please list
      these below.
 Product
Process
  Design
 Capacity
(Ibs/day)
Avg. Daily
Production
  While
Operating
(Ibs/day)
   Date
  Process
 Installed
(Year.  Mont
Attach additional pastes, if necessary.
*the word "use" in this context excludes uses or production of less than 1000 Ibs p<
 year in any research, pilot or laboratory operation.

                                    A-41
                                PART  T  -

-------
                                             Corporation
                                             Plant
                                             City	State
7b.  If your plant has changed design production rate or average daily production
     rate throup.h orocess modifications which involve debottlenecking of certain
     unit operations by the modification or replacement of equipment, or expansion
     or other similar projects, please complete the table below using the units
     indicated for products on Lists 1, 2,  3 and 4.

                                                            Avg. Daily
                                                            Production        Date
                                                 Design       While          Process
Product                 Process                 Caparity    Operating        Changed
                                               (Ibs/dav)    (Ibs/dav)     (Year, Month)
Attach additional pages, if necessary.
                                         A-42

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                                             Corporation
                                             Plant
                                             City                     State
7c.  If your plant has discontinued, since October 18,  1976,  the production of any
     product on List 1, 2 or 3, please complete the table below using the units
     indicated.

     At your discretion, you may indicate the reasons for the discontuance.  For
     example, was the process line technologically out  of date and too costly to
     update; were applicable environmental controls prohibitive; etc.


                                                  Date
                                              Discontinued
Product                Process                (Year, month)  Reason for Discontinuan
                                       A-43

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                                         Corporation^
                                         Plant	~
                                         City	
State
 7d.   If you have installed any process modifications (reactor design, distillation
      column operating conditions, etc.) or in-plant controls, (steam stripping,
      solvent extraction, etc.) since October 18, 1976, which  either sj.gnificantly
      affected or were designed to reduce the raw waste loads (flow or composition)
      of wastewater discharged to either a treatment facility or direccly to surface
      waters, please complete the following table.*
I Product/Process
! line
i
la.


Description of the Process
Modification or in-Process
Control



Intended Objective of the
Modification or Control System
e.g. remove volatile organics.



b.    Quantify the results of the use of the modification or process control system.
Parameter



Effluent Parameter
Values* Before Modification



Effluent Parameter
Values"*" After Modification



Repeat the above table for each modification
2a


b. Parameter







Effluent Parameter
Values Before Modification







Effluent Paramters
Values After Modification




+ Wastewater flow and pollutant concentration if possible.

*Attach additional tables, if necessary (photocopy this page).
*Attach flow diagrams or drawings, if appropriate.
                                    A-44
                               PART I  - Page 7

-------
                                   LIST 1

                            PLASTICS & SYNTHETICS
ABS/SAN
Acrylic Resins
Alkyds and Unsaturated Polyester Resins
Cellulose Acetate Fiber/Resin
Cellulose Derivatives
Cellulose Nitrate
Cellophane
Epoxy Resins
Ethylene-Vinyl Acetate Copolymers
Fluorocarbon Polymers
Melamine Resins
Nylon Resins/Fiber
Phenolic Resins
Polyamides
Polyester Resin/Fiber
Polyethylene
Polypropylene Resin/Fiber
Polystyrene
Polyurethane Resins
Polyvinyl Acetate
Polyvinyl Chloride
Rayon
Silicones
Urea Resins
                                     A-45
                               BADT T _ T>~~« 3

-------
                                   LIST 2

                             ORGANIC CHEMICALS
Acc-taldehyde
Acetic acid
Acetone
Acetylene
Acrylates (includes acrylic acid,
 methacrylic acid, and esters)
Acrylonitrile
Adiponitrile
Aniline
Benzene
Benzoic acid
Bisphenol A
Caprolactam
Chloromethanes (Methyl Chloride,
 Methylene Chloride, Chloroform,and
 Carbon tetrachloride)
Citronellol
Coal Tar
Cumene
Cyclohexane
Dimethyl terephthalate
Diphenylamine
Ethyl acetate
Ethyl benzene
Ethylene
Ethylene dichloride
Ethylene glycol
Ethylene oxide
Formaldehyde
Hexame chylened1 ami n e
Isobutylene
Isopropanol
Maleic Anhydride
Methanol
meta-Xylene
Methyl amines (including mono-
 di- and tri-methyl amine)
Methyl ethyl ketone
Methyl salicylate
ortho-Nitroaniline
ortho-Xylene
Oxo-Chenicals
para-Aminophenol
para-Cresol
para-Nitro aniline
para-Xylene
Phenol
Phthalic anhydride
Plasticizers (esters of
 phthalic acid)
Propylene
sec-Butyl-alcohol
Styrene
Tannic acid
Terephthalic acid
Tetraethyl lead
Toluene
Vinyl acetate
Vinyl chloride
                                   A-46
                               PART I - Page 9

-------
                                   LIST 3
                             ORGANIC CHEMICALS

Acetic acid salts, Total
Acetic anhydride
e<-Chlorotoluene (Benzyl chloride)
Adipic acid
2-Asinoethanol (Monoethanolamine)
Aspirin
Benzyl alcohol
Benzoyl  peroxide
Benzoic  acid  salts:   Sodium Benzoate, technical
   and U.S.?.  grades
Castor Oil, Ethoxylated
Choline  chloride  (All Grades)
Cresols, Total
Cyclohexanone
Dichlorodif luoromethane
Diethylene glycol
2-Diaethylaminoethanol
Dipropylene glycol
Dodecyl  mercaptans
Ethanolamines, Total
Ethyl alcohol, Synthetic
2-Ethylhexanoic acid  (ot-Ethylcaproic Acid)
Epoxidized esters, Total
Fumaric  acid
Glutamic acid, Monosodium salt
Hexamethylenetetramine, Technical  grade
2,2-Iminodiethanol  (Diethanolamine)
4,A-Isopropylindenediphenol  (Bisphenol A)
2-Methoxyethanol  (Ethylene Glycol
  Monomethyl Ether)
Methyl bromide
N-Butyl  Alcohols  (N-Propyl carbinol)
Nitrobenzene
5-Nitro-ortho-toluenesulfonic acid (S03H-1)
ortho-Dichlorobenzene
para-Nitrophenol  and  Sodium  salt
Pentachlorophenol (PCP)
Pentaerythritol
Propionic  acid
Propylene  glycol  (1,2-Propanediol)
Propylene  oxide
Salicylic  acid
Tetrachloroethylene  (Perchloroethylene)
Trichloroethylene
Trichlorofluoromethane
Triethylene glycol
Xylenesulfonic acid,  Sodium Salt
                                  A-47

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                                         Corporation
                                         Plant
                                         City	State
PART II

INTRODUCTION

The objective of this part is to obtain information related to the analysis of
wastewaters, and the detection,  quantification and treatment of the 129 priority
pollutants named on List 4.  The logic flow of the questions in this section is
as follows:

     (1)   Identify which wastewater streams have been analyzed for the
           129 priority pollutants.

     (2)   Report the analytical results for those streams where compounds
           on List 4 have been detected.

     (3)   Describe all efforts of any scale directed toward the removal
           of one or more compounds on List 4 by a wastewater treatment
           or In-process control system since October 1972.
1.   The identification of compounds on List 4 has been categorized into three
     areas as follows:   (please check the appropriate box)

I   -1 a.    No analyses have been conducted for any of the compounds oa
           List 4.  Please go to Question 4 of Part II.

I    1 b.    Wastewaters have been analyzed for some of the compounds or
           List 4.  Please go to Question 2 of Part II.

I    I c.    Wastewaters have been analyzed for some of the compounds on
           List 4 (e.g., metals, etc.) and part of the data was reported
           in the previous Section 308 questionnaire (October 18,  1976).
           Those priority pollutants previously reported are as follows:
     Please go to Question 2 of Part II and report on those not included in the
     previous questionnaire.  If there are no additional List 4 pollutants to
     those listed above, please go to Question 4 of Part II.
                                     A-48
                               PART II - Page 1

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                                     LIST 4
                            129 PRIORITY POLLUTANTS
Compound Name

acenaphthene
acrolein
acrylonitrile
benzene
benzidine
carbon tetrachloride
  (tetrachlorome thane)
chlorobenzene
1,2,4-trichlorobenzene
hexachlorobenzene
1,2-dichloroethane
1,1,1-trichloroethane
hexachloroethane
1,1-dichloroethane
1,1,2-trichloroethane
1,1,2,2-tetrachloroethane
chioroethane
bis(chloromethyl) ether
bis(2-chloroethyl) ether
2-chloroethyl vinyl ether
  (mixed)
2-chloronaphthalene
2,4,6-trichlorophenol
chloroform (trichloromethane)
2-chlorophenol
1,2-dichlorobenzene
1,3-dichlorobenzene
1,4-dichlorobenzene
3,3'-dichlorobenzidine
1,1-dichloroethylene
1,2-trans-dichloroethylene
2,4-dichlorophenol
1,2-dichloropropane
1,2-dichloropropylene
  (1,3-dichloropropene)
2,4-dimethylphenol
2,4-dinitrotoluene
2,6-dinitrotoluene
1,2-diphenylhydrazine
ethylbenzene
fluoranthene
Compound Name

4-chlorophenyl phenyl ether
4-bromophenyl phenyl ether
bis(2-chloroisopropyl) ether
bis(2-chloroethoxy) methane
methylene chloride (dichlorometh.j.ne)
methyl chloride (chloromethane)
methyl bromide (bromomethane)
bromoform (tribromomethane)
dichlorobromomethane
trichlorofluoromethane
dichlorodifluoromethane
chlorodibrocomethane
hexachlorobutadiene
hexachlorocyclopentadiene
isophorone
naphthalene
nitrobenzene
2-nitrophenol
4-nitrophenol
2,4-dinitrophenol
4,6-dinitro-o-cresol
N-nitrosodime thylamine
N-nitrosodiphenylamine
pentachlorophenol
phenol
bis(2-ethylhexyl) phthalate
butyl benzyl phthalate
di-n-butyl phthalate
di-n-octyl phthalate
diethyl phthalate
dimethyl phthalate
benzo (at) anthracene
  (1,2-benzanthracene)
benzo («) pyrene (3,4-benzopyrene)
3,4-benzofluoranthene
benzo(k)fluoranthane
  (11,12-benzofluoranthene)
chrysene
acenaphthylene
anthracene
benzo(ghi)perylene (1,12-benzoperylene)
                                     A-49
                                PART II - Page 2

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                                     LIST 4

                            129 PRIORITY POLLUTANTS
                                   (Continued)
Compound Name

fluorene
phenanthrene
dibenzo (a,h) anthracene
  (1,2,5,6-dibenzanthracene)
indeno (l,2,3-cd)pyrene
  (2,3-o-phenylenepyrene)
pyrene
tetrachloroethylene
toluene
trichloroethylene
vinyl chloride
  (chloroethylene)
aldrin
dieldrin
chlordane (technical mixture
  & metabolites)
4,4'-DDT
4,4'-DDE (p,p'-DDX)
4,4'-DDD (p,pf-TDE)
a-endosulfan-Alpha
b-endosulfan-Beta
endosulfan sulfate
endrin
endrin aldehyde
heptachlor
heptachlor epoxide
a-BHC-Alpha
b-EHC-Beta
r-BHC (lindane)-Gamma
g-BHC-Delta
PCB-1242 (Arochlor 1242)
PCB-1254 (Arochlor 1254)
PCB-1221 (Arochlor 1221)
PCB-1232 (Arochlor 1232)
PCB-1248 (Arochlor 1248)
PCB-1260 (Arochlor 1260)
PCB-1016 (Arochlor 1016)
Toxaphene
Compound Name

Antimony (Total)
Arsenic (Total)
Asbestos (Fibrous)
Beryllium (Total)
Cadmium (Total)
Chromium (Total)
Copper (Total)
Cyanide (Total)
Lead (Total)
Mercury (Total)
Nickel (Total)
Selenium (Total)
Silver (Total)
Thallium (Total)
Zinc (Total)
2,3,7,8- tetrachlorodibenzo-
  p-dioxin (TCDD)
                                       A-50
                                PART II - Page 3

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                                           Corporation
                                           Plant
                                           City	State_
2.  Complete Tables A through £ on the following pages with the results of
    analyses of wastewaters from processes  at  the  plant  site.  Include in the
    tables the names of priority pollutants detected and quantified by the
    analyses of wastewaters, at the locations  described  in Tables A through E.

          Table A:   Complete this table with the influent raw waste loac.ings
                    to either on-site treatment or pre-treatment facilities.

          Table B:   Complete this table for those  process wastewaters which are
                    discharged without treatment to surface waters or to municipal
                    treatment (POTW).  Do not  include storm waters or nun-contact
                    cooling waters.

          Table C:   Complete this table for treatment plant effluents discharged
                    to surface waters or pre-treatment facility efflue-its prior
                    to discharge to a POTW.

          Table D:   Complete this table for individual product or process waste
                    streams where priority  pollutants have been identified as a
                    constituent.   Express values obtained for the priority pollutar.
                    in terms of unit raw waste loading,  e.g. (Ib priority pollutant
                    1000 Ib product).

          Table E:   Complete this table for priority pollutants found In the plant
                    intake raw water supply.   Its  purpose is to establish appropria
                    background levels.

    PLEASE READ THESE NOTES BEFORE COMPLETING  THE  TABLES;

          Please identify all treatment or  pre-treatment plants for which Tables A
          through E apply by a specific designation—especially if more than one
          facility  exists.   Use the same name  as on the  previous 308 letter respons
          If possible.

          Tables A  and C should be influent and effluent of the same facility and
          identified by the same name.

          Place the number of analytical results which fall within the concentratio
          ranges shown in the appropriate columns  of each table.  Please use ap-
          propriate concentration ranges such  as parts per million, part per billio
                                    A-51


                            PART  II - Pace 4

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                                             Corporation
                                             Plant	I
                                             City	
                       State
                                    TABLE A

                   COMBINED RAW WASTE TO TREATKEOT FACILITIES

Complete this table for each treatment or pre-treatment facility at the plant site.
Report the results of analyses performed on the influent wastewater to eitne.r com-
bined on-site treatment or a pre-treatment facility, for each facility (photocopy
the blank page, if necessary).

Treatment/Pretreatment Facility Name	
Treatment Unit Processes included in the Treatment/Pretreatment Facility
Identify the Product/Process lines which generated the vastevaters for which the
analytical results below apply.	
Results presented in the table below were obtained from analyses made
   I	1  Prior to January 1, 1973
After January 1, 1973, approximate
  date	    	
Process Wastewater Flow
  (million Gal/Day)
                                     min.
           avg.
max.

Priority
Pollutant












UNITS











CONCENTRATION RANGES
<10











10-100











100-1000











>1000












Analytical Method











                                PART II - Page 5

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                                              Corporation
                                              Plant	"
                                              City	
                                   State
                                      TABLE B
UNTREATED PROCESS WASTEWATER DISCHARGED TO SURFACE WATER OR TO MUNICIPAL TREATMENT
 Complete this table with the results of analyses performed on each undiluted pro-
 cess wastevater stream discharged without treatment to surface waters or to muni-
 cipal treatment.  (Photocopy the blank page, if necessary.)
 Product/Process producing wastewater_
            or
 Wastewater Source
 Discharge Point
 Time Period Represented^
 by the Results
 Results presented in the table below were obtained from analyses made

    I   1  Prior to January 1, 1973
        l__l After January 1, 1973, approximate
               date
 Process Wastevater Flow
   (million GAL/DAY)
min.
avg.
max.

FSIORTTT
POLLUTANTS











UNITS











CONCENTRATION RANGES
<10











10-100











100-1000












>1000












ANALYTICAL METHOD










A-B3
                                  PART TT - Pawn

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                                               Corporation,
                                               Plant	"
                                               City	
    State
                                      TABLE C

   PROCESS WASTEWATER DISCHARGED FROM FINAL TREATMENT  OR PRETREATMENT FACILITIES


Complete this table with the results  of analyses performed  on  the  effluent  from each
wastewater treatment plant or pretreatment plant.   (Photocopy  the  blank page.,  if
necessary.)
Treataient/Pretreatment Facility Name
Discharge Point of the Treatment/Pretreatinent facility:
Results presented in the table below were obtained from analyses made

        Prior to January 1, 1973         I   I  After January 1,  1973, approximate
                                                date
Process Wastewater Flow
  (million GAL/DAY)
                              min.
                                                 avg.
max.

'RIORITY
'OLLUTANTS











UNITS











CONCENTRATION RANGES
<10











10-100










100-1000










I
>1000












ANALYTICAL METHODS












-------
                                              Corporation	
                                              Plant	'^
                                              City	
                 State
                                      TABLE D

                       PRODUCT/PROCESS LINES RAW WASTE LOADS

Complete this table with the results of analyses on each individual product or pro-
cess wastewater stream.
Product/Process producing wastewater_

Or Wastewater Source
Results presented in the table below were obtained from analyses made

   II Prior to January 1, 1973       I   I  After January 1, 1973, approximate
                                              date
Process Wastewater Flow
  (million GAL/DAY)
min.
avg.
                  max.
Does the process wastewater flow include contributions from non-contact wastewater
such as cooling tower blowdown, boiler blowdown, etc?  If it does, report the per-
centage as follows:            	                  .     ___________
                                  min.
avg.
                                                                       max.

PRIORITY
POLLUTANTS











UNITS











CONCENTRATION RANGES
<10











10-100









100-1000









i
i

>1000












ANALYTICAL METHOD











                                    PART IT - Pa«» ft

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                                              Corporation_
                                              Plant	~
                                              City	
State
                                      TABLE E

                                 PLANT INTAKE WATER

Complete this table with the results of analyses on the raw water intake to the
facility.

Results presented in the table below were obtained from analyses made

   I   I  Prior to January 1, 1973     L_J After January 1, 1973, approximate
                                            date
Intake Water Flow
(million
PRIORITY
POLLUTANTS











GAL/DAY)
UNITS











min. avg.
CONCENTRATION RANGES
<10











10-100










100-100C










A-56
jj
>1000











max.
ANALYTICAL >SETHOD











                                  PART II - Page 9

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                                           Corporation
                                           Plant
                                           C i ty	S tat e_
    Describe the sampling and analytical techniques used for priority
    pollutants.
         Was/is EPA protocol used for the sampling?
         Was/is the EPA protocol used for the analysis?
         Describe other techniques by pollutant parameter,  (attach
         additional material if clarification of the technique is
         desirable).
             Pollutant	Technique
4.  If you have not analyzed for all of the 129 priority pollutants in various
    waters and wastewaters in your plant, please answer the following questions
    for those pollutants for which analyses have not been made.

    A.   Do you have reason to believe or would you suspect that any of the
         129 priority pollutants are present In your plant's raw wastewater
         or treatment plant effluent as a result of your manufacturing.
         operations or as a result of the presence of your facility at
         your site?  (Do not list suspected presence in intake waters as a
         source of priority pollutants in answering this question)..

            I    I    No - Co to Question 6.

            {    I   Yes - Continue below.

    B.   If the answer to 4A is yes, please list the priority pollutants you
         would suspect to be present and the suspected product source.

             Pollutant                         Suspected Source
                                  A-57


                              PART II - Page 10

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                                           Corporation
                                           Plant
                                           City	State
Questions 5 through 8 ask for Information  on the treatment and  research on  the
treatment of the List A priority pollutants.   If the  information  requested  was
supplied in the previous Section 308  questionnaire, in all cases,  please name
the priority pollutant and state that the  information was already submitted.
5.  Have treatment facilities (end-of-pipe or  in-plant  control)  been installed
    specifically for removal of any of  the priority  pollutants  (List 4)?

            1    i    No - Go to Question 7.

            I    i   Yes — Continue below.

    If the answer is yes, please list the treatment  unit  process or  processes,
    the pollutant(s) removed and whether installed in-plant  or  end-of-pipe.

         If in-plant, list the product  on which installed.

         Attach data, flow sheets and drawings as appropriate to define the
         design criteria and process effectiveness (e.g., removal efficiency,
         etc.).  If this was supplied in the previous questionnaire, please
         state so after listing the pollutant(s).

                                                         Indicate end-of-pipe
        Treatment                  Pollutants             or  specific product
    Unit Process(es)            	removed             on  which installed
    Do you have any data on the removal of specific  priority pollutants by
    existing end-of-pipe treatment facilities or in-process pollutant control
    processes which were originally designed for removal of conventional
    pollutant parameters?  (e.g.,  BODs, COD, NH, TSS,  etc.)

             j    I   No

                    Yes
    If answer is yes, please indicate the treatment process,  the priority
    pollutant(s) studied,  the design criteria,  and the removal efficiency
    by the process.   Attach flow sheets or other data as appropriate to define.
                             PART II - Page 11      A"58

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                                          Corporation
                                          Plant
                                          C it y	S ta t e
     Have vou conducted research and/or bench-scale or pilot-scale programs for
     studying the treatability or removal of one or more of the 129 priority
     pollutants exclusive of heavy metals?

                    No

                    Yes

     If the answer is yes, please describe the studies conducted,  the priority
     pollutants examined, and the results of the studies.  (attach extra pages
     if necessary, or provide a copy of the study to complete your answer).
B.   Do you have data on the adsorption capacity of activated carbon for specific
     process vastewaters resulting from the production of any of the compounds
     presented in Lists 1,  2, 3 or A.

             I	;   NO

                ' !   Yes

     If yes, list the product/process  effluents, the type of carbon tested
     (granules or powdered) and the adsorption capacity.

                                                      Adsorption Capacity*
                                Activated               (grams adsorbed/
     Product/Process          Carbon Tested               gram carbon)
     ^Specify adsorbate basis (e.g.,  COD,  TOC,  phenol,  butadiene,  PVA)  and
      concentration ranges evaluated.
                                     A-59

                              PART II -  Page 12

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                                           Corporation
                                           Plant
                                           City	Sta-e
PART III - TREATMENT INFORMATION

PLEASE READ THE INSTRUCTIONS FURNISHED PRIOR TO  PROCEEDING TO THIS PART.

1.   Even though you nay not now be discharging  to  a municipal  sewer system,
     is there an adequate municipal trunk sewer  close  by to  which you could
     discharge?

            CD   No

            I    I   Yes - Distance from production facilities	 ft.

            1    I   Already discharging to a municipal  system

2.   If the recent data from your plant production  or  wastewater treatment plant
     operation is, in your opinion, more representative than that submitted in
     the previous questionnaire, you may submit  new data (since October 18, 1976)
     on Tables A and C attached, being careful to:

     A.   Include the beginning and end dates of the period  covered.

     B.   Show average daily production for each product corresponding to .the
          time period that treatment plant and raw  waste parameters  are reported
          In Tables A and C.  You may use any of the tables  in  Part  I, Question 7
          to report production data.

     C.   If raw waste is discharged without treatment, describe discharge point
          (e.g., municipal sewer, river, etc.).

     D.   Indicate where (location) the samples  were taken which generated the
          analytical data presented in Tables A  and C.

     E.   Continue responding to the questions in this part.

3.   Does your plant operate an activated sludge process for treatment of either
     a single process wastewater effluent or a combination of two or more product/
     process wastewater effluents?

  !    I   No - It is not necessary to complete the  remainder of Part III

  Ii  Yes - (1)  If you reported data from your  plant in  the previous portfolio,
               dated October 18, 1976, please continue below with Parts A & B.
               (2)  If you commenced operation or modified an  activated sludge
               plant since October 18, 1976,and  did not report  on it or its
               operation, please go to Question  A.

     Certain areas of the previous question portfolio  dated  October  18, 1976, were
     not adequate to provide the necessary information for an  effective performance
     evaluation of the existing wastewater treatment plants.  The performance
     evaluation is essential in determining the  cost of waste  treatment as a functi
     of plant operating criteria, external factors  such as  temperature, etc.
                                    A-60

                            PART III - Page 1

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                                              Corporation
                                              Plant
                                              Ci ty	S tate_
Parts A and B request supplemental or clarifying information resulting from gaps in th
previous submittals.  Complete this page for each Activated Sludge System on this site

A.  If the answer to Question 3 is yes, please list each activated sludge facility
    operated at your plant and list the product/process effluents included In the
    influent to the activated sludge process.

    Activated Sludge                      Type of Activated Sludge Systec
        Plant Name                        (Contact Stabilization, Conventional, etc.)
    Product/Process lines discharging to this treatment plant.
    Activated Sludge                      Type of Activated Sludge System
        Plant Name                        (Contact Stabilization, Conventional, etc.)
    Product/Process lines discharging to this treatment plant.
    Activated Sludge                      Type of Activated Sludge System
        Plant Name                        (Contact Stabilization. Conventional, etc.)
    Product/Process lines discharging to this treatment plant.
                                         A-61

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                                           Corporation_
                                           Plant	~
                                           City	
                                                             Stats
 List the following daily average values.  Please select a three-month operating
 period representing typical summer conditions , and if climate changes are sig-
 nificant, select a second three-month period representing winter conditions.
 Unless otherwise noted below, production levels reported in your October 18,
 19 76 » questionnaire will be used as representative of the data below.
 Activated Sludge Plant Name or Designation (Complete for each plant)
 1.
 2.
 3.
 4.
 5.
 6.
 7.

 8.
 9.
10.

11.
12.

13.
14.
                                                     Summer
                                                            Winter
Influent total BOD. concentration
Effluent total BOB, concentration
Influent soluble BOD. concentration
Effluent soluble BOD,, concentration
Influent TSS concentration
Effluent TSS concentration
Mixed liquor suspended solids concen-
tration maintained in the aeration tank
Mixed liquor volatile- suspended solids
concentration maintained in the
aeration tank
Temperature of mixed liquor
Detention time maintained in the
aeration tank
F/M ratio
Sludge production (excess biological
sludge)
Total oxygen (air) supplied
Is activated carbon added to the
activated sludge system?
  mg/1
_mg/l
  mg/1
"ng/1
  mg/1
""mg/1
  mg/1
  hours
  Ibs/day
  Ibs/day
                                      A-62

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                                              Corporation_
                                              Plant
                                              City	State
4.  Have you modified, installed or added any wastewater treatment facilities since
    submission of the October 18, 1976, portfolio.
               No - If no, the balance of the portfolio does not apply.

        L—J   Yes - continue to the next paragraph

    A.   If the answer to the above questions is yes,  please complete the following
        items, if information is available,  for each  new or modified wastewater
        treatment facility.

        1.  Please describe the modified or  new facilities.

        2.  State the purpose of the change/new installation.

        3.  Give the month/year of the change/new installation.

        4.  State the capital costs of the change/new installation.

        5.  State the operating costs for the system  changed or  added.

        6.  Give the new operational parameters.   (If the new unit operation is
            activated sludge, the operational parameters should  be listed below.)
            Attach a diagram illustrating the process as it currently exists.

        7.  Please.complete the attached Table A (treatment plant influent raw
            waste load)  and Table C (treatment plant  effluent characteristics) for
            the new or modified facility.

        8.  Please complete Sections B and C for each new or modified accivated
            sludge plant.
                                        A-63


                                 PART III - Paae 4

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                                          Corporation
                                          Plant
                                          City	State
B.  Please list each activated sludge facility operated at your plant  and list
    the product/process effluents included in the influent to the activated
    sludge process.

    Activated Sludge                  Type of Activated Sludge System
       Plant Name                     (Contact Stabilization. Conventional, etc.)
    Product/Process lines discharged to the activated  sludge plant
    Activated Sludge                  Type of Activated Sludge Systea
       Plant Name                     (Contact Stabilization.  Conventional,  etc.)
    Product/Process lines discharged to the activated  sludge plant
    Activated Sludge                  Type of Activated Sludge System
       Plant Name                     (Contact Stabilization,  Conventional,  etc.)
    Product/Process lines discharged to the activated sludge plant
    Activated Sludge                  Type of Activated Sludge System
       Plant Name                     (Contact Stabilization,  Conventional,  etc.)
    Product/Process lines discharged to  the activated sludge plan;
                                  A-64

                              PART III - Page 5

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                                          Corporacion_
                                          Plant
                                          City	State
C.  Complete this question for each activated sludge plant indicated is  Part  A
    above.  List the following daily average values.  Please select a three-
    month operating period representing typical summer conditions,  and if
    climate changes are significant, select a second three-month period
    representing winter conditions.
    Activated Sludge Plant Name or Designation
    (Complete for each plant)_
                                                   Summer      Winter

    1.   Influent total BOD_ concentration         	   	 mg/1
    2.   Effluent total BOD. concentration         	   	mg/1
    3.   Influent soluble BOD. concentration       _______   ___________ m8/l
    4.   Effluent soluble BOD. concentration       ________   	»g/l
    5.   Influent TSS concentration                	   	mg/1
    6.   Effluent TSS concentration                ________   	m8/1
    7.   Mixed liquor suspended solids concen-
        tration maintained in the aeration tank   _______   _______«. m8/l
    8.   Mixed liquor volatile suspended solids
        concentration maintained in the
        aeration tank                             	   	mg/1
    9.   Temperature of mixed liquor               	   	 °C
   10.   Detention time maintained in the
        aeration tank                             	   _         hours
   11.   F/M ratio                                 	   	^
   12.   Sludge production (excess biological
        sludge)                                   	   	Ibs/day
   13.   Total oxygen (air) supplied               _______   _         Ibs/day
   14.   Is activated carbon added to the
        activated sludge system?                  	   	
                                  A-65

-------
                                            TABU A
                                HARK LOAM TO TttATMBIT FACILITIES
Corporation.
Plant
City	
State
          TmeLU.tr
Trvacant Fadlicy D*Bcrl»cloe
           Sowrc«(*)_
     (wo)
            (°C) -
                          Air
low
COD (Ito/tey)
TOC
TSS (Ita/tey)
TBS
TIB M » (lba/««y)
St»»iflc«nt Hoc«ls  (Idoacify)
                   ( lb«/«Uy)
_ (lb./
-------
                                              TABLE C

                               TREATED PIOCESS WASTE UUSS DISCHARGED
Corporation,
ria&t	
Citv                             ftat»
Traataaat Facility                                               Saaplc  location (final diacharat line.  «te.)
Traacaant Facility Baacrtotlaa                                   _______^_________^___^^_______
Diacharc* Fwiat
Do you poat-chierinat* tki* BffliMat?      To   M y*«, do you ebloriMt*      (A) fell-T
                                          »o                                  (j) Fart-TlM
>«ra»»t«r
Flov (NED)
pi (pM «tt»)
Ta»p«rat«r« C*C) - Uaacawatar
                          Air
     (Ika/dar)
ODD (Ifca/day)
TOC (IWoay)
TSS (Ifca/day)
TM (laW*ay)
•B2 a* • (Ua/day)
TO) a* M (lka/4ay)
fhanol (Ika/day)
Slgnlfle«t Naeala (Zdratify)
_ (Ua/day)
                 _(lba/aay)
                 JIbt/day)
                 Jtta/oay)
Othara (Xaaatlfy)
                  (lba/daT>
                  (Iba/dav)
„	(Ika/day)
	Uba/day)
                                           TAXI III - Pat*  8
                                                A-67

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              APPENDIX B
        CHEMICAL PRIORITY LIST FOR



SCREENING AND VERIFICATION SAMPLING PROGRAMS

-------
                                APPENDIX B

                        CHEMICAL PRIORITY LIST FOR
               SCREENING AND VERIFICATION SAMPLING  PROGRAMS
    In September, 1977,  the Organic Chemicals  Manufacturing  Industry Working
Group approved a priority list containing seven categories of products
manufactured by the industry.   This Appendix lists  the  chemicals  in each of
the top five priorities.  The last two priority lists are omitted because of
their length.

    The seven levels of priorities are as follows:

Priority 1:   Chemicals manufactured in excess of 5 million  pounds per year
              (top 100 production items) that  are on the list of  priority
              pollutants.  This list contains  25 products.

Priority 2:   Chemicals derived from priority  pollutants that are identified
              in an ORD survey (Radian report) and  are  manufactured in excess
              of 5 million pounds per year.  This list  contains  19 products.

Priority 3:   The organic chemicals on the list of  priority  pollutants, not
              including Priority 1 above and not including pesticides.  This
              list contains 67 products.

Priority 4:   Chemicals derived from priority  pollutants but that are
              manufactured at less than 5 million pounds per year.  This list
              contains 146 products.

Priority 5:   All other organic chemicals manufactured  in excess  of 5 million
              pounds per year.  This list contains  81 products.

Priority 6:   Organic, non-pesticide entries on the TOSCA list that are not in
              Priorities 1 through 5 above.  This list  contains  325 products.

Priority 7:   The remainder of the 20,000 commercial industrial  chemicals.
                                   B-l

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                   CHEMICALS IN PRIORITY LEVELS 1 THROUGH 5
Priority 1

Acrylonitrile
Benzene
Bis(2-ethylhexyl) Phthalate
Butyl Benzyl Phthalate
Carbon Tetrachloride
Chloroform
1,4-Dichlorobenzene
Diethyl Phthalate
Dimethyl Phthalate
Di-n-butyl Phthalate
Di-n-octyl Phthalate
Ethyl Benzene
Methyl Bromide
Methyl Chloride
Dichlorodifluoromethane
Nitrobenzene
4-Nitrophenol
Pentachlorophenol
Phenol
Tetrachloroethylene
Methylene Chloride
Toluene
Trichloroethylene
Trichlorofluoromethane
Vinyl Chloride
                                   B-2

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Priority 2

Acetone
Adipic Acid
Aniline
Benzoic Acid
Benzoid Acid Salts, Sodium Benzoate
Benzyl Alcohol
Benzyl Chloride
Bisphenol A
Cumene
Cyclohexane
Cyclohexanone
Cyclohexanone/Cyclohexanol (AK oil)
Diisopropyl Benzene
D ipheny1am ine
Fumaric Acid
Maleic Anhydride
Methyl Ethyl Ketone (2-butanone)
Phthalic Anhydride
Styrene
                                   B-3

-------
Priority 3

Acenaphthene
Acenaphthylene
Acrolein
Anthracene
1,2-Benzanthracene
Benzidine
Benzo(a)pyrene (3,4-benzopyrene)
3,4-Benzofluoranthene
11,12-Benzofluoranthene
1,12-Benzoperylene
Bis(chloromethyl) Ether
Bis(2-chloroethyl) Ether
Bis(2-chloroethoxy) Methane
Bis(2-chloroisopropyl) Ether
Bromoform (tribromomethane)
4-Bromophenyl Phenyl Ether
Chlorobenzene
Chloroethane
2-Chloroethyl Vinyl Ether (mixed)
2-Chloronaphthalene
2-Chloropheno1
m-Chlorophenol
4-Chlorophenol
4-Chlorophenyl Phenyl Ether
Chlorodib romoraethane
Chrysene
1,2,5,6-Mbenzanthracene
1,2-Dichlorobenzene
1,3-Dichlorobenzene
3,3-Dichlorobenzene
Dich1orobromomethane
1,1-Dichloroethane
1,2-Dichloroethane
1,1-Dichloroethylene
1,2-trans-dichloroethylene
2,4-Dichlorophenol
1,2-Dichloropropane
1,3-Dichloropropylene (1,3-dichloropropene)
2,4-Dimethylphenol
4,6-Dinitro-o-cresol
2,4-Dinitrophenol
1,2-DiphenyIhydrazine
Fluoranthene
Fluorene
Hexachlorobenzene
Hexachlorobutadiene
Hexachlorocyclopentadiene
Hexachloroethane
Indeno(l,2,3-C,D)pyrene
Isophorone
Napthalene
2-Nitrophenol
                                   B-4

-------
3-Nitrophenol
4-Nitrophenol
N-Nitrosodimethylamine
N-Nitrosodiphenylamine-n-propylamine
Parachlorometa Cresol
Phenanthrene
Pyrene
2,3,7,8-Tetrachlorodibenzo-p-dioxin (TCDD)
1,1,2,2-Tetrachloroethane
1,2,4-Trichlorobenzene
1,1,1-Trichloroethane
1,1,2-Tr ichloroethane
2,4,6-Trichlorophenol
2,4,5-Trichlorophenol
N-nitrosodiphenylamine
                                   B-5

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Priority 4

Acetanilide
Acetphenone
Acetone Cyanohydrin
Acrylamide
Alkylnaphthalenes
Alkyl (Cg, C ) phenols

Allyl Alcohol
m-Aminobenzoic Acid (Anthranilic Acid)
o-Aminobenzoic Acid
p-Aminobenzoic Acid
Aminoethylenthanolamine
Aniline Hydrochloride
m-Anisidine
o-Anisidine
p-Anisidine
Anisole
Anthraquinone
Benzaldehyde
Benzamide
Benzoquinone
Benzenedisulfonic Acid
Benzenesulfonic Acid
Benzil
Benzilic Acid
Benzoin
Benzonitrile
Benzophenone
Benzotrichloride
Benzyl Chloride
Benzylamine
Benzyl Bichloride
Bromobenzene
B romonaphtha1enes
Chloranil
m-Chloroanaline
o-Chloroanaline
p-Chloroanaline
o-Chlorobenzaldehyde
p-Chlorobenzaldehyde
o-Chlorobenzoic Acid
p-Chlorobenzoic Acid
m-Chlorobenzyl Chloride
o-Chlorobenzyl Chloride
p-Chlorobenzyl Chloride
Chloronaphthalenes
m-Chloronitrobenzene
o-Chloronitrobenzene
p-Chloronitrobenzene
m-Chlorotoluene
o-Chlorotoluene
p-Chlorotoluene
Cyclohexanol
Cyclohexene

                                   B-6

-------
Cyclohexylamine
Decahydronaphthalenes
Diacetone Alcohol
2, 7-Diaminobenzoic Acid
3,5-Diaminobenzoic Acid
2,4-Dichloroanaline
3,4-Dichloroanaline
m-Dichlorobenzene
o-Dichlorobenzene
p-Dichlorobenzene
Dichlorohydrin
Dicyclohexylamine
Diketene
n,n-Dimethylanaline
2,3-Dimethylanaline
2,4-Dimethylanaline
2,5-D imethy1ana1ine
2,6-Dimethylanaline
3,4-Dimethylanaline
Dimethyl Sulfide
Dimethyl Sulfoxide
2,4-Dinitrotoluene
2 ,6-Dinitrotoluene
Dinitrotoluenes (mixed 2,4/2,6)
Diphenyl
Diphenyl Sulfoxide
p-DodecyIpheno1
Ethylenediamine
Ethyl Orthoformate
Glyceraldehyde
Glycerin
Glycerol
Hexalene Glycol
Hydroqu inone
Maleic Acid
Malic Acid
1-Malic Acid
+ and - Malic Acid
Mesityl Oxide
Methacrylic Acid
n-Butyl methacrylate
Methyl methacrylate
2-Methylaniline
4-Methylaniline
3-Methylaniline
n-Methylaniline
Methylcyclohexane
MethyIcyclohexano1
Methy1cyclohexanone
Methyl Isobutyl Carbinol
Alpha-Naphthalene Sulfonic Acid, Sodium Salt, & Formaldehyde Condensate
Beta-Naphthalene Sulfonic Acid, Sodium Salt, & Formaldehyde Gondensate
Alpha-Naphthol
                                   B-7

-------
Beta-Naphthol
o-Nitroanisole
p-Nitroanisole
m-Nitrobenzoic Acid
o-NitrobenzoiC Acid
p-Nitrobenzoic Acid
Nitrophenol
Nitrotoluene
Nonylphenol
Octylphenol
p-Phenetidines
Phenosulphonic Acid, Ammonium Salt, Sodium Salt, Zinc Salt, and
  Formaldehyde Condensate
m-Phenylinediamine
o-Phenylinediamine
p-Phenylinediamine
Phthalimide
Phthalimide, potassium salt
Phtholonitrile
Piperazine
Resorcinol
Sodium Phenate
Succinic Acid
Sulfanilic Acid
Tetrachlorophthalic Anhydride
1,2,3,4-Tetrahydronaphthalene
Tetrahydrophthalic Anhydride
Tetramethylethylenediamine
Toluene-2,4-diamine
Toluene diamines (2,4/2,6)
p-Toluenesulfonamide
Toluenesulfonic Acid
p-Toluenesulfonyl Chloride
Trichloroaniline
1,1,2-Trichloro-1,2,-trifluorethane
Vinylidine Chloride
Xylenes (mixed)
2,4-Xylenol
Xylidine
m,p-Xylenes
                                   B-8

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Priority 5

Acetaldehyde
Acetic Acid
Acetylene
Acrylic Acid
Adiponitrile
Amyl Acetate
Amyl Alcohols
Caprolactam
Citronellol
Dimethyl Terephthalate
Ethyl Acetate
Ethyl Amines
Ethylene
Ethylene Glycol
2-Ethylhexyl aerylate
Ethylene Oxide
Formaldehyde
Hexamethylenediamine
Isobutylene
Isopropanol
Linear alcohol ethoxylates
Methanol
M-Xylene
Mono-Methyl Amines
di-Methyl Amines
tri-Methyl Amines
Methyl Salicylate
Nylon salt
o-Xylene
n-Butanol
n-Propanol
p-Am inopheno1
o-Aminophenol
p-Cresol
p-Nitroaniline
o-Nitroaniline
p-Xylene
p-Nitrophenol and Sodium Salt
Propylene (propene)
Sec-butyl-alcohol
n-Butyl acrylate
Butylenes
Tannic Acid
Terephthalic Acid
Tetraethyl Lead
Vinyl Acetate
Acetic Acid Salts, Total
Acetic Anhydride
Aspirin
Benzoyl Peroxide
Castol Oil, Ethoxylated
                                   B-9

-------
Choline Chloride (all grades)
Cresols, total
Cresote
Diethylene Glycol
Dipropylene Glycol
Diphenylisodecyl phosphate
n-Dodecyl Mercaptans
Tert-Dodecyl Mercaptans
Ethyl acrylate
Ethyl Alcohol, Synthetic
Glutamic Acid, Monosodium Salt
Hexamethylenetetramine, Tech.
Pentaerythritol
Proprionaldehyde
Propionic Acid
Propylene Glycol (1,2-Propanediol)
Propylene Oxide
Salicyclic Acid
Triethylene Glycol
Xylenesulfonic Acid, Sodium Salt
2-Aminoethanol (monothanolamine)
2-Dimethylaminoethanol
2-Ethylhexanoic Acid (a-Ethylcaproic Acid)
2-Methoxyethanol (Monomethyl Ether)
2,2-Iminodiethanol (Diethanolamine)
5-Nitro-o-Toluenesulfonic Acid (S03H-1)
n-Propanol
iso-Butyraldehyde
n-Butyraldehyde
                                   B-10

-------
        APPENDIX C
ANALYTICAL METHODS DEVELOPMENT
     AND REVIEW OF DATA

-------
I.  INTRODUCTION

    A.   General

    Perhaps no other aspect of pollution control is more fundamental than the
definition of the pollutants to be controlled.  An important early step in
developing regulations limiting the discharge of pollutants to the environment
and in designing a treatment system to meet such limitations is the
characterization of the pollutant load by sampling and analysis.  After the
treatment system has been installed, the discharge must be regularly monitored
to evaluate the effectiveness of the treatment system and compliance with the
discharge limitations.

    In gathering data to develop and support regulations, the reliability of
the results is more important than the specific analytical methodology
employed to characterize the wastewater.  Where available, "standard" methods
should be used to eliminate the inconvenience and expense of establishing a
non-standard method suitable to the specific wastewater.  However, the notion
that data of acceptable quality is inherently associated with the use of a
"standard" method is incorrect.  If performed improperly, however, either a
standard or a non-standard method can yield faulty data.  (Taylor 1981).

    Programs to assure the reliability of analytical results should focus on
the quality of the results, not the analytical techniques employed.   If the
accuracy and precision data accompanying a reported number meet the criteria
chosen, the analytical techniques are acceptable.  (Amore 1979).

    The data produced by all analytical techniques reflect the variations in
human and equipment performance that are inherent to the analyses.  The
critical questions are:  What are the precision and accuracy of a reported
value and are these acceptable for the application use of the data?   These
questions are answered by emphasizing quality assurance in laboratory
operations and minimizing measurement errors to produce results appropriate to
how the data is to be used.

    B.   Quality Assurance/Quality Control

    Quality assurance/quality control (QA/QC) includes all of the laboratory
activities necessary to determine the precision (repeatability) and accuracy
(relationship to the true value) of an analytical measurement.   The accuracy
of the measurement is determined by adding (spiking) a known amount  of analyte
(the pollutant of interest) to a wastewater sample.  Recovery (the ratio of
the amount of spike detected to the amount that had been added) depends on the
matrix (the other pollutants and chemicals in the wastewater) and the
analytical technique, and may be used to adjust the observed value to obtain
the "true" value (observed value * recovery = true value).

    An analytical method that fails to detect an organic compound spiked into
pure water (i.e., zero recovery) is inappropriate.   When that method has been
modified so that substantial (>50%) recovery from pure water is consistent
and predictable, and the accuracy and precision have been established, the
method is validated.   If the accuracy and precision achieved in the  pure water
is also realized in varying wastewater matrices, the method can be considered
                                   C-l

-------
standardized.  Accuracy and precision in a wastewater sample usually differs
from that achieved in pure water.

    Measurements at concentrations near the detection limit for the compound
of interest (e.g. less than 10 parts per billion for most organics), create
additional problems.   The limit of detection for any pollutant is the lowest
concentration of that pollutant that is distinguishable from background
concentrations with a known degree of confidence.   Below this concentration,
the pollutant is "not detected".  The limit of determination for each
pollutant is the concentration at  which one can state with a known degree of
confidence that the pollutant is present.  Between the limit of detection and
the limit of determination, the pollutant is "detected but unconfirmed".

    Two errors affect any analysis:  operator inconsistency and matrix
interference.  Practice should reduce operator error.  Reduction of matrix
interferences is more difficult,since it is impossible to anticipate all
possible matrix interferences.  In metals analysis, most of the interfering
compounds are destroyed by acidic high temperature digestion prior to
measuring the metals concentration.  Digestion prior to the analysis of
specific organic compounds however, is not feasible, since it would alter the
individual compounds.

    Specific methods or, if appropriate, standard methods can be utilized to
reduce the interferences from a specific matrix.  Regardless of method, the
measurements should be validated with an adequate QA/AC program.  This
approach is in many cases the only practical means of accurately quantifying
organic priority pollutants in a variety of wastewater matrices.

    C.   Wastewater Analysis in the OCPSF Industry

    Each product/process employed in manufactured organic chemicals, plastics,
or synthetic fibers produces a wastewater containing priority pollutants
characteristics of the product/process.  Few manufacturing facilities in the
Organic Chemicals and Plastics/Synthetic Fibers (OCPSF) industrial category
have the same combination of product/processes, so the wastewater generated at
a single plant cannot represent the entire industrial category.  This
diversity creates a wastewater analysis challenge not found in those
industrial categories where the product/process mix and the associated
priority pollutants are more consistent throughout the industry.

    The variability of the wastewater matrices found within the OCPSF industry
suggests that a specific analytical method may not produce the same precision
and accuracy at all plants.  While an off-the-shelf "standard" method may be
more convenient to use, it may not be entirely appropriate for every
wastewater sample.  In a plant manufacturing organic chemicals, for example,
the types and amount of pollutants in the process wastewater vary with the
product/process operating conditions and with the combination of
product/processes that are being operated.  To minimize the impact of these
variations on the data, an analytical method should be selected that is
appropriate for the specific wastewater matrix that is being analyzed.  It is
also important to ensure that the samples are collected in such a way as to be
representative of the wastewater being sampled, and that the integrity of the
                                   C-2

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samples is protected during short-term storage, transport and preparation for
analysis at the receiving laboratory.

    D.   Available Analytical Methods

    At the beginning of the BAT study, EPA had no validated analytical methods
for measuring organic priority pollutant concentrations in the OCPSF
Industry.  Three analytical methodologies were available for measuring
individual organic priority pollutants at low concentrations in wastewaters.
These methodologies were (1) gas chromatography/mass spectrometry (GC/MS),  (2)
gas chromatography/conventional detector (GC/CD), and (3) high performance
liquid chromatography (HPLC).   Conventional detectors include flame ionization
(FID), electron capture (EC),  photoionization (PI), and Hall
electroconductivity.  HPLC is recently finding more frequent application,
especially in the pesticide industry.

    Both GC/MS and GC/CD use gas chromatography to separate the individual
compounds extracted from a wastewater sample.  The mass spectrometer (MS) is a
universal detector that can identify and measure organic compounds without
prior programming, whereas conventional detectors (CD) identify a particular
compound by comparing its retention time with that of a known compound under
the same column conditions.

    GC/MS is a broad-spectrum technique--a large number of compounds in a
single sample can be identified and measured.  It is generally used in
conjunction with a solid state microelectronic computer system; the mass
spectrometer repeatedly scans the mass spectrum.  Because most of the
detectable constituents of a sample can be identified from their mass spectra,
GC/MS is a very versatile method for determining pollutants in a sample
without advance knowledge of what pollutants are there.

    GC/CD is a targeted technique; it can recognize and measure only those
compounds for which it has been calibrated.  The usual method for identifying
a GC peak as a specific pollutant is to measure its absolute retention time
under strictly controlled operating conditions, or its relative retention time
compared to a standard compound under the same conditions.

    Sample preparation for either GC/CD of GC/MS can be quite complicated and
time-consuming if there are many organic compounds present in the sample
matrix.  If only a few compounds are present, the sample may be injected
directly into the GC.  If a large number of compounds are present, however,
they must be separated into broad groups by three or more extraction
procedures.  Complicated sample preparation increases the degree of pollutant
loss and sample contamination.


II. ANALYTICAL METHOLODOLOGIES AND QA/QC FOR THE BAT STUDY

    The analytical methodologies and QA/AC used in the BAT study are
summarized in TABLE C-l and discussed below.
                                   C-3

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                             NOTES TO TABLE C-l

1.  The latest EPA EMSL Cincinnati GC/CD and GC/MS methods are also shown,  for
    comparison.

3.  Date of first publication of method.

4.  Reference document for first release of method.

5.  EPA method number and name of analytical technique employed.

6.  The portion of sample to be analyzed by the method.

7.  Data or specifications for identification of specific compounds.

8.  The maximum acceptable number of mass spectrometer scans within which the
    characteristic mass spectral ions must maximize for the compound to be
    considered detected.

9.  Maximum acceptable discrepancy in GC retention time between a peak and
    that of the standard for compound identification.

10. The maximum acceptable discrepancy in the ratios of the characteristic
    mass spectral ions between the standard and those of the sample.

11. The number of characteristic mass spectral ions specified by the method.

12. Information supporting the identification of a compound and the
    measurement of its concentration.

13. The instrumental method used to calculate compound' concentration.

14. Relationship between mass of chemical injected and output signal.

15. The number of data points used for calibration.

16. How often the calibration is to be verified.

17. Criteria and specifications of procedures that support data validity.

18. Specific test which demonstrates instrument performance.

19. Compound(s) used for end-to-end system test.

20. Test which demonstrates mass spectrometer sensitivity and spectrum
    validity, relative to EMSL standard peak intensity ratios.

21. Standard deviation obtained with multiple analyses of standards (i.e.,
    replicability).

22. Requirements for initial precision evaluation.
                                   C-7

-------
                             NOTES TO TABLE C-l
                                 (continued)

23. Specifications for subsequent precision measurements .

24. Recovery of known masses of standards added to a standard sample (usually
    reagent water) or to an OCPSF sample.

25. The compounds employed for accuracy measurement.

26. The specification levied by the method.

27. Blanks required to demonstrate freedom from contamination and
    interferences.

28. Required frequency of analysis of lab blanks.

29. Blanks carried to and from the sampling site.

30. Only major differences between the methods are listed.

31. Gas chromatograph column type.

32. Analyst's flexibility in selecting alternate column.

33. Means by which sample is separated from the water.

34. Analyst's flexibility in removing interferences from sample.

35. Specified ratio of water volume to extract volume.

36. Memo from Telliard to EGD project officers through Bob Schaffer dated May
    27, 1977, entitled "Sampling and Analysis Procedures for Screening of
    Industrial Effluents for Priority Pollutants."

37. Analysis for compounds included in the "volatiles" fraction, containing 30
    specific priority pollutants.

38. NS means "no specification given" in method.

39. Employed internal standard, which uses compounds different from the
    compounds to be measured.

40. Test standard containing all compounds to be analyzed by the method in the
    particular fraction specified.

41. Decafluorotriphenylphosphine used for calibration.

42. Quality control charts showing deviation of results from true or average
    value chronologically for each standardization measurement.
                                   C-8

-------
                             NOTES TO TABLE C-l
                                 (continued)

43. Two times the standard deviation of the spike concentration that had been
    added.

44. AR means as required.

45. One required with each Sample Set (SS).

46. Not applicable; the purge and trap method does not "concentrate" the
    sample in a liquid phase.

47. The semi-volatiles (acid and base/neutral) fractions.   Some protocols also
    include GC/MS confirmation of a pesticide or PCB found by GC.

48. PGP is pentachlorophenol; Benz is benzidine.  These two compounds are
    employed to test GC column performance for the acid and base/neutral
    fractions, respectively.

49. Not required by this method.

50. Capillary columns were permitted but were seldom used.

51. Separatory funnel extraction or continuous liquid/liquid extraction.

52. Either internal (see 39) or external (which uses the compound to be
    measured) standard calibration methods could be used.

53. Required either multi-point calibration or a standard which matched
    closely the concentration(s) of the compound(s) found in the sample.

54. No precision and accuracy requirement in these methods, but a quality
    control/quality assurance program containing precision and accuracy
    requirements was suggested in the Federal Register notice.

55. Surrogate compounds -- compounds which simulate the behavior of the
    compounds being analyzed.

56. Methods were given in work statements sent by EPA to its contract
    laboratories.

57. The OCV (Organic Chemicals-Verification Phase) program was directed at
    testing for a given pollutant or group of pollutants at each plant.  Each
    analyst was allowed to fractionate the sample as seen fit in order to
    successfully analyze for the pollutant(s).

58. The specifications and requirements set at each EPA contract laboratory
    for each pollutant reflected the analytical judgment of the analysts and
    quality assurance personnel.

59. The actual priority pollutant under investigation was tested.
                                   C-9

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                             NOTES TO TABLE C-l
                                 (concluded)

60. Analytical precision was determined by analysis of duplicate samples.

61. Each OCV analytical method specifies extraction methods.   For the 5-plant
    study, EPA chose the OCV methods to be used by each contract laboratory.
    No flexibility in choosing and applying the method (other than that
    specifically permitted in the method) was allowed.

62. As required and as permitted by the method, based on the judgment of the
    analyst.

63. This GC/CD method was chosen as typical of the latest 304(h) EMSL
    Cincinnati methods.  Methods 601-613 are all similar.

64. Less than three times the standard deviation obtained by analysis of
    standards during the sample analysis.

65. Four replicate analyses of standards.

66. Within three standard deviations, combined with analysts' judgment.

67. Cowen, W.F., and J. L. Simons (Catalytic, Inc.) Analytical Methods for
    the Verification Phase of the Bat Review (for Organics and Plastics
    and Synthetics Industrial Category).  September, 1980.
                                   C-10

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    A.   Screening Phases I and II

         1.   Analytical Methods

         As noted in the Federal Register (3 December 1979, p.  69464), when
Congress passed the 1977 Clean Water Act, "...section 304(h) analytical
methods were not available in many cases....because only on rare occasions had
industry monitored or had EPA regulated (priority) pollutants."  In the fall
of 1977, the only methodology recommended by the EPA was the GC/MS screening
protocol, which EPA had not yet validated.  The Organic Chemicals Branch (OCB)
of EPA's Effluent Guidelines Division adopted this GC/MS analytical protocol
for the Screening Phase work.  Introduced by the Agency in April of 1977, this
protocol was also used extensively by other branches within the Effluent
Guidelines Division, by EPA contractors and Regional laboratories, and by
private labs.

         The analytical methods used during the Screening Phase are described
in "Sampling and Analysis Procedures for Screening of Industrial Effluents for
Priority Pollutants" (USEPA 1977).  Since the purpose of screening was to
identify all priority pollutants among a host of other compounds that may be
present in a wastewater sample, GC/MS methodology was appropriate because it
is not as subject to interferences as other analytical alternatives.  The
GC/MS screening protocol was intended for the qualitative and
semi-quantitative determination of organic priority pollutants  during EPA's
initial survey of industrial effluents.

    The screening protocol's procedure for extracting organic priority
pollutants from wastewater samples was either purge and trap, or liquid-liquid
extraction.  Some compounds may be recovered from the wastewater by either
procedure.  The efficiency of recovery depends on the vapor pressure
(volatility) and water solubility of the compound.  When a compound is
efficiently recovered by both procedures, the GC conditions determine the
procedure of choice.  In general, the GC conditions selected for the purge and
trap are not suitable for organic priority pollutants that elute from the GC
column later than chlorobenzene.

         The purge and trap recovery procedure involves purging the wastewater
sample with an inert gas (Helium) and trapping the purged organic compounds by
adsorption on a resinous substrate (Tenax-silica gel).  The trapped organic
compounds are subsequently desorbed by heating the trap and directing the
desorbate into the GC/MS system.  This method detects a group of 29 priority
pollutants, which are mostly halogenated C1-C5 hydrocarbons.  It was
recognized that the two priority pollutants acrolein and acrylonitrile are so
water-soluble that they cannot be efficiently recovered by the purge and trap
procedure.  Direct aqueous injection was recommended for these two compounds,
as well as any of the volatiles that may be present at more than one part per
million.

         For the less volatile organic priority pollutants, a liquid-liquid
extraction procedure (Webb 1978) separated them into groups that are
selectively extracted at differed pH.  Extraction with methylene chloride at
pHll removes basic and neutral compounds.  Included in this group are 46
priority pollutants:  halogenated aromatics, nitroaromatics, nitrosamines,
                                   Oil

-------
polyaromatics (PAH's) and phthalate esters.   Extraction with 15 percent
raethylene chloride in hexane at pH7 removes  neutral compounds.   Included in
this group are 26 priority pollutants:  organochlorine pesticides and
polychlorinated biphenyls (PCB's).   Extraction with methylene chloride at pH2
removes acidic compounds.  Included in  this  group of 11 phenolic priority
pollutants:  phenol, chlorophenols  and  nitrophenols.

         The solvent extract was dried  and filtered by passing it through a
short column of sodium sulfate, which had been prewashed with methylene
chloride.  After evaporating the solvent to  concentrate the extract, it was
injected into the GC/MS system.  Pesticides  were to be initially quantified
using GC/EC (electron capture detector), since that is a much more sensitive
detector than the MS and is specific for compounds containing halogens.
Pesticide identity was to be subsequently confirmed using GC/MS, when more
than 40 nanograms of the pesticide  was  injected (EC detector subject to
overload).

         Metals were determined by  flame or  flameless atomic adsorption.
Total cyanides were analyzed by a colorimetric method after distillation.
Total phenols were determined by the 4-aminoantipyrine (4-AAP)  colorimetric
method, often giving values several orders of magnitude higher than the GC/MS
value for simple phenol.  The 4-AAP procedure measures most phenols (not
para-substituted phenols) as well as various non-phenolic compounds found in
industrial wastewaters.  The 4-AAP  data accompanied metal and cyanide analyses
as part of a package of "classical  pollutants".  Since the 4-AAP test is not
compound specific for phenolic priority pollutants, such data had no further
use in this study.

         2.   Quality Assurance/Quality Control

         The following discussion refers to the April 1977 revision of the
March 1977 Screening protocol (USEPA 1977).

         The QA/QC procedures for the volatile fraction of the priority
pollutants that are explained next  include:

              a.   Analysis of blanks

              b.   Daily calibration of the GC/MS system with priority
                   pollutant and internal standards.  Daily MS tuning with
                   DFTPP (Decafluorotriphenyl phosphine).

              c.   Calibration procedure gave recovery-corrected data.

              d.   GC/MS system testing.  Quality control of data precision by
                   replicate analyses of internal standards.

              e.   No tolerance specifications for compound identification
                   criteria.

         A blank is reagent water,  i.e., water in which no priority pollutants
or interfering compounds can be detected by the analytical method being used.
A trip blank septum-sealed in a vial accompanied each shipping container of
                                   C-12

-------
samples.  The purpose of analyzing a trip blank was to test for contamination
during sampling and sample transport.   Laboratory blanks were analyzed to
demonstrate that the GC/MS system was  free of interferences and contamination.
Laboratory blanks were to be analyzed each day prior to the first sample and
between samples afterward.  While practices varied from one laboratory to
another, analysis of laboratory blanks between samples was frequently omitted
if the previous sample showed a low content of priority pollutants.

         The GC/MS system was to be calibrated daily by spiking reagent water
at a level of 20 ppb with a "cocktail" of priority pollutants and three
internal standards.   These compounds were recovered by the purge and trap
technique and analyzed by the GC/MS system.  From these results, response
factors for each priority pollutant could be calculated and used to  determine
concentration in the subsequent analyses.  Since the priority pollutants and
internal standards were recovered together from the reagent water during the
calibration procedure, concentrations  that were subsequently computed from the
calibration response factors were recovery corrected values.

         The screening protocol also called for the MS to be tuned daily with
20 nanograms of DFTPP.  Since the retention time of DF.TPP on the GC  column
used for volatiles was too long to be practical, the tuning requirement was
met by replacing the GC column used for volatiles with the one used  for
base/neutrals.  Although not allowed by the screening protocol, some analysts
introduced the DFTPP directly into the MS by means of a probe.  DFTPP has
since been replaced by p-Bromofluorobenzene, so that now the MS tuning
compound can be conveniently added with the other standards for the  daily
calibration and avoid the GC column change necessitated by the DFTPP.

         The GC/MS system was to be tested and the precision of the  purge and
trap-GC/MS procedure was to be routinely determined (frequency unspecified) by
spiking reagent water with three internal standards and performing replicate
analysis.  The three compounds were Bromochloromethane,
2-Bromo-l-chloropropane and 1,4-Dichlorobutane.  These compounds are not
priority pollutants, but were used because they span the range of GC column
retention times of the volatile priority pollutants.  Quality control charts
were to be constructed showing results as a function of time, or number of
analyses performed.

         Qualitatively, a weakness of the screening protocol for volatile
priority pollutants was the lack of specifications on compound identification
criteria.  Characteristic masses or mass ranges were tabulated and were the
only information afforded for qualitative determinations.  No tolerances were
given for relative retention time ( + minutes), or for correspondence with
published mass spectral peak height ratios ( + percent).  Most laboratories
compensated for this omission by applying the tolerance specifications that
were provided for the semi-volatile priority pollutants (see following
discussion).  If the presence or absence of a compound was in doubt, the
laboratories were instructed to report the compound as being present.
                                   C-13

-------
         The QA/QC procedures for the semi-volatile fractions of the priority
pollutants that are explained next include:

              a.   Analysis of blanks

              b.   Calibration (frequency unspecified) at two concentrations
                   with priority pollutants  and an internal standard (D10
                   anthracene).  Daily MS tuning with DFTPP.

              c.   Calibration procedure did not give recovery-corrected
                   data.

              d.   Daily GC/MS system testing with pentachlorophenol (acid GC
                   column), and with benzidine (base/neutral  GC column).  No
                   quality control of data precision by replicate analysis.

              e.   Tolerances were specified for compound identification
                   criteria.

         A trip blank was to be analyzed with each set of samples.   This blank
was obtained in the field by pumping reagent water through the sampling pump's
system of plastic tubing.  For this reason,  the trip blank was also known as a
"tubing blank."  To avoid unnecessary GC/MS  analysis of blanks, the screening
protocol allowed the extract of the blank to be run on GC/FID, using the GC
column appropriate to the acid or base/neutral fraction.  If  no peaks greater
or equal to that of the D10 anthracene internal standard appeared,  then a
GC/MS analysis of the blank was not required.

         The GC/MS system was to be calibrated at unspecified intervals by
direct injection of a "cocktail" of priority pollutants and an internal
standard (D10 anthracene) at two concentration levels, 10 and 100 ppb.   Since
the calibration standards were not carried through the extraction procedure,
the concentrations subsequently computed from the calibration response factors
were not recovery corrected.  The screening  protocol did not  require that the
semi-volatile priority pollutant data be corrected for recovery.

         The GC/MS system was to be tested each day.  To test with the GC
column used for the acid fraction (Tenax-GC), 100 nanograms of
Pentachlorophenol was to be used.  To test with the base/neutral GC column
(SP-2250), 40 nanograms of Benzidine was to  be used.  These compounds were to
be injected directly into the respective column.  If the compound could not be
detected by the GC/MS system, the GC column  was to be replaced.  There was no
requirement to maintain Quality Control charts on the precision of this
method, as was required for the purge and trap method.

         Relatively rigorous criteria were applied to the identification of
semi-volatile priority pollutants.  Three conditions were specified:

              a.   The characteristic ions for the compound must be found to
                   maximize in the same mass spectral scan.
                                   C-14

-------
              b.   The time at which the GC peak occurs must be within a
                   window of + 1 minute of the retention time of the
                   compound.

              c.   The ratio of three mass spectral peak heights must agree
                   within + 20 percent with the relative intensities given
                   for the compound.

If the presence or absence of a compound was in doubt,  the laboratories were
instructed to report the compound as being present.

    B.   Verification Phase

         1.    Background

         Although well suited for a qualitative assessment of organic priority
pollutants in wastewater samples, the GC/MS method used for the Screening
Phase--The Screening Protocol--was not appropriate for  the improved
quantitation sought in the Verification Phase.  Determination of extraction
efficiency (percent recovery) and replication to measure precision and
accuracy for many disparate waste streams would have made a substantial
increase in the number of analyses to be performed.  The continued use of the
GC/MS method with more rigorous QA/QC would have made the analytical costs
prohibitive, and there were not sufficient qualified GC/MS-equipped
laboratories available in the fall of 1977 to handle the samples.

         OCB obtained data of adequate quality at reasonable cost by
substituting conventional detectors for the mass spectrometer and modifying
existing "state-of-the-art" GC/CD methods.  GC/MS was used to confirm priority
pollutant identification, and was routinely reserved for those instances when
interferences in the sample matrix so complicated the analysis that the use of
GC/CD proved impractical.  By using the less expensive  and widely available
GC/CD methods routinely, and by using the substantially more expensive GC/MS
method for 10 to 15 percent of the samples, OCB cost-effectively combined the
two methodologies without severely compromising QA/QC.   An added benefit of
this approach was that the level of QA/QC employed and the practice of the
methods in a variety of matrices demonstrated the applicability of the GC/CD
methods for the analysis of effluents from product/processes within OCB's
assigned industries.

         The 1979 Water Pollution Control Federation literature review
(Journal WPCF, Vol. 51, 'No. 6, pp. 1134-1171) of analytical methods used in
research published during 1978 (when Verification began) showed that GC/CD was
the methodology most often used for measuring organic priority pollutants.  Of
186 published investigations involving a number of organic priority pollutants
in a wide range of sample types, 150 utilized GC/CD.  At least part of the
reason for this dominance was the GC/CD instruments were more widely available
than GC/MS at that time.

         In June of 1977, EMSL published a preliminary collection of GC/CD
methods selected from a computerized literature search by the Denver National
Enforcement Investigation Center (NEIC) of EPA.  A year later EMSL let
contracts on a program to validate some of these methods.  Although not yet
                                   C-15

-------
validated, these methods were proposed in the Federal Register (3 December
1979, p. 69532 ff).   Having already begun to use GC/CD methodology during
Verification for reasons previously discussed, OCB continued its methods
development program concurrent with the Verification Phase.   The chronologies
and milestones of the two independent GC/CD method development and validation
efforts are presented in FIGURE C-l.   EMSL's contracting laboratories began
delivery drafts of validated GC/CD methods six to nine months after OCB had
completed it own verification program.  EMSL's validated methods will be
promulgated by EPA in 1983 as the 600 series.

         Dr. C. A. Hammer of Envirodyne Engineers compiled an initial list of
proposed methods for OCB's Verification program from the EMSL selections and
the NEIC bibliography.   The literature search had focused on methods suitable
for groups of priority pollutants that would have similar responses to
extraction procedures,  chromatographic conditions, and detectors.  A method
appropriate to each of these was assembled in a loose-leaf manual and made
available to both OCB's contractor laboratories and Verification plants.

         OCB's objective was to develop site-specific (in many cases
matrix-specific) GC/CD methods by analyzing actual industry wastewater
samples.  Often sampling product/processes effluents with high matrix
interference potential, OCB's experimental approach used spiked and duplicate
sample analyses to define the validity of each measurement.

         2.   Analytical Methods

         Before the initial plant visit, a list of priority pollutants to be
verified was compiled using the analytical results of the Screening Phase (see
Section V of Volume II) and predictions from the product/processes known to be
operating at the plant.  The list and a package of appropriate methods
selected from the then current GC/CD methods manual were sent to the plant
well in advance of the initial visit to allow time for their review.  During
the initial visit, a grab sample of wastewater was taken from each location to
be sampled.  The grab samples were used by the EPA contract laboratory to tune
the proposed analytical method to the specific wastewater matrix at each
sampling location.  Extraction, cleanup, and GC conditions were modified as
necessary during three weeks of method evaluation.  At the end of that time
(approximately one week before the actual Verification sampling was to
commence), the method variation found to be most appropriate in each sample
matrix was specified.  EPA discouraged the contract laboratory from
subsequently modifying the method significantly, and informed the plant what
methods would be used.

         The purpose of discouraging further change in the methods was
primarily to offer each plant an opportunity to replicate OCB's Verification
sampling and analysis.   The benefits anticipated from replication were:

               (a)  A doubling of the number of data points.

               (b)  A chance for the plant to evaluate the analytical methods
                   for utility and cost-effectiveness, particularly in
                   comparison to GC/MS; and
                                   C-16

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-------
              (c)  An interlaboratory comparison of OCB and plant analytical
                   results would be compiled.

         Many plants elected to do no replication or to limit their
replicative participation to samples of the final effluent, or of the combined
untreated wastewater.  For self-verifying plants, the plant performed the
principal analysis and OCB's contractor performed the replicate analysis.  A
potentially important contribution to the methods development effort was
reduced by the limited plant participation.

         Seven contracting laboratories eventually participated in OCB's
Verification methods development:  Envirodyne,  Midwest Research Institute,
Southwest Research Institute, Gulf South Research Institute, Jacobs
Engineering Group (PJB Labs), Acurex Corporation, and A.D.  Little.  Beginning
in January 1979, the key analysts from each of  these laboratories met
approximately every two months to discuss developments and update methods.  As
methods were matched with the matrices at each  plant, variations (usually a
change in GC conditions or column) were forwarded to all team members and
documented in the methods manual.  This continuing update of successful
modifications avoided redundant effort and cost-effectively helped resolve new
matrix problems simultaneously encountered by members of the team.

         Verification methods for metals and cyanides were the same as those
used during the Screening phase.  For organic compounds, however, the
verification methods developed were designed to isolate, concentrate, and
quantify one or more compounds from each of the following groups of organic
priority pollutants:

              (a)  Pesticides, PCBs, and phthalates
              (b)  Phenols
              (c)  Volatile organics
              (d)  Halogenated volatile organics
              (e)  Polynuclear aromatic hydrocarbons
              (f)  Nitrosamines
              (g)  Acrolein and acrylonitrile
              (h)  Chlorobenzenes
              (i)  Haloethers
              (j)  Chlorinated hydrocarbons

         TABLE C-2 lists the analytical methods used during Verification.
Details of each analytical procedure, including precision and accuracy data,
are presented in the September 1980, report by  W. F. Cowen and J. L. Simons of
Catalytic, Inc., entitled "Analytical Methods for the Verification Phase of
the BAT Review", under EPA Contract No. 68-01-5011.  Analytical methods were
varied as required by the sample matrix and each variation was assigned a
number.  Any method used in the program was identified by a procedure code
number, a variation number, and the laboratory  that was responsible for its
initial use.  Several of the procedure codes include methods that were 'later
submitted for validation to EMSL contract laboratories.

         Dr. W. F. Cowen of Catalytic, Inc. continually summarized and studied
the precision and recovery data to determine which methods gave the most
consistent results despite a variety of wastewater matrices.  Supplementary
                                   C-18

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                                  TABLE C-2

            ANALYTICALS METHODS USED DURING THE VERIFICATION PHASE
ANALYTICAL PROCEDURE
CODE NO.
Direct Aqueous Injection Procedure for GC
   Analysis of Acrolein and Acrylonitrile

Method for Benzidine and Its Salts in Wastewater

Method for Organochlorine Pesticides and Phthalat-e
   Esters in Industrial Effluents

Total Cyanide

A-26 Resin/GC-FID Method for Phenols

Analysis of Nitrosamines

Microextraction Method for Organic Compounds in
   Industrial Effluents

Purge-and-Trap Procedures for Analysis of Volatile
   Organic Compounds in Effluents

Method for Polychlorinated Biphenyls CPCB's) in
   Industrial Effluents

Analysis of Arsenic and Selenium in Industrial Effluents by
   Flameless Atomic Adsorption Spectrophotometry and
   Hydride Generation

Analysis of Silver, Antimony, and Thallium in
   Industrial Effluents by Flameless Atomic
   Adsorption Spectrophotometry

Analysis of Beryllium, Cadmium,' Chromium, Copper,
   Nickel, Lead and Zinc in Industrial Effluents by
   Flame or Flameless Atomic Adsorption Spectrophotometry

Mercury in Water (Manual Cold Vapor - Atomic
   Adsorption Technique)

Pentane Extraction of Organics in Wastewaters
   for GC Analysis
  1*


   2

  3*


   4

   5

   6

  7*
 10*
 11*
 12*
 13*
 14*
                                   C-19

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                             TABLE C-2 (Concluded)
ANALYTICAL PROCEDURE                                                   CODE NO.
Acid Extraction Procedure for Phenols                                    15

Analysis of Nitroaromatics,  Isophorone, and                              16
   Chlorobenzene

Analysis of Polynuclear Aromatic Hydrocarbons                            17
   in Industrial Wastewater

Procedure for Vapor Equilibration (Headspace) Analysis                   18

Procedure for Determination of Phenolic Compounds                        19
   by Solvent Extraction

Procedure for the Determination of Neutral and                           20
   Basic Compounds by Solvent Extraction

Procedure for Volatile Aromatic Hydrocarbons by                          21
   Solvent Extraction
NOTE:    Code numbers 1 through 18 are the procedures initially compiled for
         OCB by Envirodyne from EMSL and NEIC information.  Procedures 19
         through 21 are modifications of procedure Number 7 (Microextraction)
         for specific groups of organic compounds.   Code numbers with an
         asterisk(*) are those 13 routinely used by OCB's contractor
         laboratories.
                                   C-20

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laboratory studies at A.D.  Little and Greenwood Labs further developed those
methods that showed promise of general applicability.   Of the methods
originally compiled, some were never practiced because the classes of priority
pollutants (e.g., pesticides, PCBs) requiring these methods were not
encountered.  From the initial compilation of 18 methods used for analyzing
organic priority pollutants, 13 were routinely used by OCB's contractor
laboratories.

         OCB's choice of GC/CD methodology during the Verification phase in
preference to the GC/MS Screening protocol resulted in the following
advantages:

              (a)  GC/CD quantification was simplified, through compound
                   spiking to generate recovery data.   GC/MS support was used
                   in a number of instances for pollutant identification.

              (b)  For the typical case of monitoring 10 to 20 compounds by
                   two to three methods, the cost using conventional detectors
                   was less than that using the mass spectrometer.  According
                   to information presented by W.L. Budde and J. W.
                   Eichelberger of EPA-EMSL in "Analytical Chemistry", Vol.
                   51, No.  6, May 1979, p. 567A, for 10 compounds, the cost
                   using conventional detectors is about one-third that using
                   mass spectrometry; for 20 compounds, GC/CD costs about 40%
                   of what GC/MS costs.

              (c)  The time required for a given analysis was reduced.  At the
                   inception of the program, GC/MS laboratories were
                   delivering analytical results three to six months after
                   receipt of the samples.  The GC/CD methodology reduced this
                   delivery time to one month.

              (d)  The wider availability of GC/CD instrumentation and
                   qualified analysts/technicians at the time facilitated the
                   analysis of the large number of samples from the many
                   product/processes studied.

         A disadvantage anticipated for GC/CD was that it would require more
clean-up of the solvent extract in order to separate subclasses of priority
pollutants from each other, as well as from other organic compounds in the
sample matrix.  In each of the wastewater samples that were examined, no more
than 20 priority pollutants were detected; generally 10 to 20 were detected.
Chromatographic resolution problems were less than expected, because those
subclasses of priority pollutants that are difficult to separate from one
another were rarely present in the same sample.

         The traditional exhaustive solvent extraction/evaporative
concentration methods used at the beginning of the program were gradually
replaced by simplified and more expeditious extraction procedures, the most
important of which was microextraction.  Volatile organic compounds were
traditionally extracted exhaustively (continuously or in multiple steps) with
excess solvent, coextracting much of the organic matrix.  Subclasses of
priority pollutants then had to be separated from interfering organic
                                   C-21

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components by sample cleanup before concentration by evaporation.   For the
simpler and faster microextraction, a small aliquot of the sample was
extracted in one step with an even smaller amount of solvent (100:1).
Partitioning of many priority pollutants into the extraction solvent (aided by
salting out) left most of the GC-interfering organic compounds in the sample.
With the right choice of GC column conditions, it was frequently unnecessary
to cleanup the extract to separate interfering organics for a satisfactory GC
analysis.  Because the extract was already concentrated, evaporative
concentration of the extraction solvent was unnecessary.  This shortened
analysis time significantly and eliminated the potential for alteration or
loss of sample components during evaporation.

         Later in the program another innovation was implemented:   static
head-space analyses of volatile organic compounds.  This technique's
advantages for measuring volatile organics are analogous to the advantages of
microextraction for measuring extractable organics.  Its original purpose was
to prevent the loss of volatile compounds in cases where it was necessary to
open the septum-sealed vial for transfer to a purge and trap apparatus, or for
compositing.

         Another change from traditional methodology was the use of liquid
crystal and capillary GC columns for separation of polycyclic aromatic
hydrocarbons.

         Analysts were allowed to use any method that they considered
applicable to a particular sample, as long as it did not require routine use
of the GC/MS.   The analysts were, however, required to execute QA/QC
procedures adequate to validate the method used.

         3.   Quality Assurance/Quality Control

         The QA/QC program for verification evolved in three stages.  In 1978
(Stage 1), the first six plants were verified with a QA/QC program consisting
of a blind spike on the Day 2 composite sample.  In the next set of five
plants (Stage 2), spikes were added at 2 to 5 times the concentrations
detected in the grab samples taken at the pre-sampling meeting.  In addition,
duplicates of 10 percent of the Day 2 and Day 3 samples were analyzed.  When
plant personnel collected and analyzed the samples (self-verification), an OCB
contract laboratory collected split samples and analyzed them, spiking samples
collected on Day 1 of the verification exercise to a concentration double that
detected in the unspiked sample.  Stage 3 was the program indicated in FIGURE
C-2, in which a designed set of spike and duplicate samples were taken.  An
unspiked, stored control sample (taken on Day 3) was required only in cases of
prolonged storage (greater than 48 hours) before spiking.  This control was
rarely required.

         Before adding the spike, it was necessary to wait for the results of
the unspiked sample analyses, so that the spike level could be made
appropriate for accurate calculation of the recovery of the added spike.
Recovery was calculated as:

0/ _          ,,.,. .. [Detected in Spiked Sample] -  [Detected in Unspike Sample] X
% Recovery = 100 X a	—	—^	, A .j j	i—r,—;	c	c—
         3                              [Added as Spike]
                                   C-22

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                         FIGURE C-2

   VERIFICATION QUALITY ASSURANCE/QUALITY CONTROL PROGRAM
DAY 1
                           EXTRACT
                           EXTRACT
                     ANALYZE
                     ANALYZE
DAY 2
                           EXTRACT
                            HOLD,
                            SPIKE
                     ANALYZE
                     EXTRACT
                       AND
                     ANALYZE
                           EXTRACT
                     ANALYZE
DAY 3
HOLD,
SPIKE
                            HOLD
EXTRACT
  AND
ANALYZE

EXTRACT
  AND
ANALYZE
                       C-23

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where [] denotes concentration.

         The formula assumes that the volume of the added spike was small
compared to the sample volume.   Otherwise,  corrections must be made to account
for the added volume.

         During the Verification program,  the recommended concentrations to
add for spiking were:

              (a)  Twenty times  the instrument-response detection limit, if
                   the sample concentration was less than 10 times the
                   instrument-detection limit; or

              (b)  Two times sample concentration,  if the sample concentration
                   was at least  10 times the instrument-detection limit.

         Ten percent of the samples analyzed for metals and cyanide were
spiked, and duplicate analyses  were performed on 10 percent.

         The purpose of determining spike recoveries on two of the three
samples collected at each site  during verification was to calculate the
efficiency of solvent extraction procedures.  Measured concentration may be
adjusted for spike recovery.  For example,  if only 50 percent of the phenol
that had been added was detected, the unspiked sample concentration of phenol
detected was assumed to be 50 percent of the correct concentration.
Correction of the measured concentration may be made by the following equation:

            ...  .   , „     .   . .      -, ™ v   Measured Concentration
            Adjusted Concentration = 100 X -	—^	7-——	
              J                            Percent Recovery of Spike

         In the case of metals  and cyanides, which were not extracted by
liquid/liquid partitioning, no  adjustments were made to the raw data, although
spike recovery data was reported by some of the analytical laboratories.
Recovery efficiency and consistency were useful to the analysts during
verification in judging whether or not an extraction procedure was appropriate
to the sample matrix.

         It should be noted that the proposed effluent limitations are based
on measured concentrations that were reported by individual laboratories.
These concentrations were not further adjusted mathematically for recovery of
spike, as indicated above.  Exceptions to this are concentration values
measured by a system that was calibrated by adding the internal standard
directly to the wastewater sample (matrix).  When calibration response factors
were determined by this procedure, concentrations measured were automatically
recovery-corrected.

    C.   CMA Five-Plant Study

    Samples were analyzed for a selected group of priority organic pollutants
that were characteristic of each plant, together with certain conventional and
nonconventional pollutants.  All organic priority pollutants included in this
study were not analyzed at all five plants.  Analyses were not run for
pesticides, polychlorinated biphenyls, or metals.
                                   C-24

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    EPA's contract laboratories analyzed all influent and effluent samples for
selected organic priority pollutants using GC/MS or GC/CD procedures (44 FR
69464 et. seq.,  December 3, 1979,  or variations acceptable to the EPA
Effluent Guidelines Division).   For example, one EPA laboratory used GC
coupled with flame ionization detection (GC/FID).   Approximately 25 percent of
the influent and effluent samples  collected at each participating plant were
analyzed by the CMA contractor using the GC/MS procedures cited above.   The
variations in the analytical procedures used by the EPA contract laboratories
and the CMA laboratory during this study are summarized in Appendix A of the
April 1982 Engineering-Science report entitled "CMA/EPA Five-Plant Study," as
are the sampling protocols for each of the five plants.

    Each participant provided daily analyses of the convention/nonconventional
pollutants in their influent and effluent wastewaters, using the methods found
in "Methods for Chemical Analysis  of Water and Wastes," EPA 600/4-79-020,
March 1979.  Additionally, four of the participants analyzed from 25 to 100
percent of the samples collected by EPA for the same organic priority
pollutants that were evaluated by  the Agency.  At a minimum, those analyses
included duplication of the CMA contractor's analyses.
III.  REVIEW OF DATA FROM SAMPLING STUDIES

    A.   Introduction

    In June, 1982, the EPA requested the Environmental Engineering Committee
of its Science Advisory Board (SAB) to review portions of the Contractor's
Engineering Report on the Analysis of the Organic Chemicals and
Plastics/Synthetic Fibers Industries.  Such reviews help EPA realize its goal
of developing regulations based on data obtained by credible scientific
methods.  The SAB was asked to address three major issues in its review of the
analytical methods and data used in developing the proposed BAT effluent
limits.

         1.   The adequacy of the overall experimental plan, the analytical
              methods used and the application of those methods.

         2.   The quality of the data presented, particularly with respect to
              whether compounds were adequately identified and whether
              accuracy and precision were determined.

         3.   The adequacy of the data for drawing reasonable conclusions from
              which defensible effluent guidelines could be developed.

    At the time of the request, the EPA had not yet completed its summary of
the Verification data upon which the proposed BAT effluent limits are based.
The SAB was, therefore, unable to address issues (b) and (c).  The material
available for SAB's review included:

         1.   A description of the technical approach that was used by EPA and
              its contract laboratories in developing analytical methods
              during Verification (see Part I of this Appendix).
                                   C-25

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         2.   The analytical methods with multiple variations that were
              developed and carefully documented during Verification,
              accompanied by a summary of the recoveries obtained with these
              methods in a wide variety of OCPSF wastewater matrices.

         3.   The QA/QC methodology that had been employed during Verification
              to establish the precision and accuracy of the analytical
              results.

The SAB criticized the dominant use of GC/CD methodology during verification
on grounds that compound identification had not been adequately confirmed.
The SAB also criticized the QA/QC methodology as being insufficient.
Subsequent to the SAB criticisms, the OCPSF Industry also criticized the
verification analytical methodology on similar grounds.   At SAB meetings,
however, representatives of the OCPSF Industry have stated that during
Verification the EPA:

         1.   Used state-of-the-art GC/CD methods.

         2.   Used more QA/QC than the OCPSF Industry could have afforded.

    In response to these criticisms, EPA has conducted an extensive review of
all organic priority pollutant analytical data that it has used in support of
the proposed regulations.  A similar review for the metal priority pollutant
data was unnecessary, since neither the SAB nor the OCPSF Industry were
critical of that analytical methodology.  The review will be completed prior
to promulgation of a final rule.  All data not meeting the standards of
quality described in the following sections are being deleted from that
database being used to develop the regulations.

    In the following sections, the method by which the analytical data was
reviewed and its quality assessed is described for the three data collection
programs:

         1.   Screening Phases I and II
         2.   Verification
         3.   CMA Five-Plant Study

    B.   Screening Phases I and II

         1.   Description of the Review

         Section II.1 of this Appendix described the analytical methods
employed in Phase I and II Screening.  Screening data was from one-day
composited samples of both treated and untreated wastewaters from over 143
OCPSF manufacturing plants.  These studies were the first comprehensive
analysis of OCPSF Industry wastewaters and EPA's first large scale field use
of GC/MS analytical procedures.  At that time, the Agency did not have an
existing database on priority pollutants for the OCPSF Industry, nor had a
predictive scheme been worked out to show the relationship between
product/process chemistry and the occurrence of priority pollutants.  Thus,
there was nothing available with which the screening results could be
compared.   Since QA/QC was not extensive in the screening protocol, there was
                                   C-26

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no systematic means of detecting problems with the analytical procedures with
which the data was being acquired.

         2.   Use of Phase I and II Data

         Screening data from a plant, plus additional priority pollutants that
were suggested by the raw materials and process chemistry of the products
being manufactured at the plant, were used during the verification program to
develop a presumptive list of priority pollutants that were to be verified at
that plant.  These considerations were also part of the priority pollutant
selection criteria for plants in the EPA/CMA Five-Plant Study.

         The OCPSF plants that were selected for screening during Phases I and
II, represent a broad coverage of the product classes listed under the
corresponding SIC Codes for these two industrial categories.  Thus a
compilation of the priority pollutants that were identified during screening
of the combined untreated contact process wastewater of all of these plants
constitutes a universe of priority pollutants that characteristically occurs
within the industry.

         The screening data were also used in a multivariate statistical
analysis to confirm subcategories.  This application of the screening data
recognizes the semi-quantitative nature of the data (see Appendix F,
"Subcategorization Multivariate Analysis").

    C.   Verification Phase

         1.   Background

         The Environmental Engineering Committee of EPA's Science Advisory
Board (SAB) reviewed the technical approach to wastewater analysis for
priority pollutants that had been used during Verification, but not the raw
data.  The "Report of Meeting in Chapel Hill, N.C. June 24-25, 1982" included
in those minutes the findings of the SAB's analytical consultants.  This
review is still underway and will be completed before publication of the final
rule.

         2.   1982 Data Review by Original Contract Laboratories

         EPA employed six contract laboratories to analyze samples from 29
direct discharge plants in the 1978 to 1980 Verification Study.  SAB's major
concern was that all the laboratories had used GC/CD (gas chromatography with
conventional detectors) methods, which SAB felt needed confirmation by GC/MS
(gas chromatography with mass spectroscopy detection) and more extensive
QA/AC.  The results from three plants were not reviewed extensively because
all GC/CD data from the EPA contract laboratories that analyzed samples from
these plants had been confirmed by GC/MS during Verification.  At two of these
three plants, samples had been split and analyzed by both a laboratory under
contract to the plant and the plant laboratory.  The plant laboratory data
agreed with its contract laboratory data within the limits considered normal
for these analyses, which obviated a need for extensive review of the data
from these plants.
                                   C-27

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         The remaining four EPA contract laboratories performed analyses for
samples from the remaining 26 plants.   The analysts that had been responsible
for the Verification analytical work at the four laboratories met in October,
1982, to adopt a uniform approach to validating the GC/CD data and to attempt
to locate all data that might be of some use in confirming the Verification
GC/CD data.

         From October, 1982, to March,  1983, all of the former EPA contract
laboratories and principal analytical chemists from the Verification program
cooperated in a review of the data, using the review procedure that had been
developed at the October meeting.  The analysts examined laboratory notebooks,
chromatograms, mass spectral tapes and other information that documented the
methods that had been used during Verification.  EXHIBIT C-l (at the end of
the Appendix) is a copy of the form used for this review.  Every data point
obtained by the four laboratories has been or will be reviewed.  Pending
completion of the review, the data bank for these proposed effluent
limitations, which was frozen in December, 1982, has been made available in
summary format as part of the public record.

         3.   Results of the Review

              (a)  GC/MS Confirmation of GC/CD Data.  The presence of many
priority pollutants that had been detected by GC/CD during the analysis of
Verification Samples was confirmed by GC/MS, or had been confirmed by GC/MS in
a preliminary grab sample.  These confirmations were encoded into the
December, 1982, BAT data summary.  While EPA limited the use of GC/MS by its
contract laboratories during Verification, the laboratories eventually applied
GC/MS confirmation to more than 10 percent of the total samples that were
analyzed.

              (b)  GC/CD Data Qualitation.  The criteria EPA applied during
its recent review of Verification GC data to eliminate questionable data
points were more rigorous than those that were proposed in the 600-series
methods (Federal Register, Vol. 44, No. 1233, pp. 69464 to 69552, December
3, 1979), and are nearly identical to published revisions of the 600-series
GC/CD methods (EMSL, Cincinnati, EPA-600/4-82-057, July 1982).  The only major
difference is the criterion for retention time agreement between standard and
sample.  The 1979 600-series methods do not specify the maximum retention time
discrepancy that is acceptable for the identification of a specific compound.
The EMSL's July, 1982 revision of these methods proposes "three times the
standard deviation of a retention time for a compound"..."based upon
measurements of actual retention time variations of standards over the course
of a day", and "... the experience of the analyst should weigh heavily in the
interpretation of chromatograms".  For confirmation of Verification results,
EPA's review contractor measured the retention time difference between GC
charts with a millimeter scale (aided by overlaying the charts on a light
table at some laboratories), or by integrator.  EPA's contractors thus applied
1982 criteria to their qualitative review of the GC/CD Verification data.

              (c)  GC/CD Data Quantitation.  Quantitative measurements at
EPA's contract laboratories employed multi-point calibration over the working
range of the detection system for compounds with non-linear responses, and
single-point calibration for those compounds with a linear response.  These
                                    C-28

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calibration procedures are the same as those proposed by EPA in 1979 (Federal
Register, Vol. 44, No. 1233, pp.  69464 to 69552,  December 3, 1979) and in the
July 1982 EMSL methods (EPA-600/4-82-057).

              (d)  Interlaboratory Comparisons.   During Verification at
several plants, duplicate samples were analyzed by the plant's laboratory, by
a commercial laboratory under contract to the plant,  or by the EPA contract
laboratory.  The data from these analyses offers  both qualitative and
quantitative comparisons between labs using the same  methodology, or where one
laboratory used GC/CD while the other laboratory used GC/MS.  Such comparisons
can be made, when all of the information garnered from the review has been
encoded.

         4.   Effect of the Review on the OCPSF Industry Database

         Data for organic priority pollutants that were collected from six
plants during Verification have already been deleted  from the statistical
analysis to determine BAT effluent limitations.   These plants were sampled
early in the Verification program, when blind spiking was used in the QA/QC
procedure.  In those instances in which an inappropriate spiking level was
used, the data would certainly be quantitatively unreliable and may often be
qualitatively suspicious.  Since this data was of variable quality, a decision
was made to exclude all of it from the statistical analysis.

         Since the review will provide GC/MS confirmation for many GC/CD data
points, it is expected to enhance the overall quality of the database and
justify retainage of most of those influent-effluent  data pairs with a
significant difference in concentration.  In general, the review of the
Verification data focused on influent-effluent data pairs where the influent
concentration was greater than about 30 ppb.

    D.   CMA Five-Plant Study

         1.   Description of the Review

         Section V of Volume II describes the Five-Plant Study.  Late in 1982,
EPA staff and contractors reviewed the data by comparing results from analyses
of the same samples at (1) EPA contract laboratories, (2) CMA contract
laboratories, and (3) the plant laboratory or plant contract laboratory.
Errors in transcription and encoding and in application of GC analyses were
found and corrected.  This section gives details of this review.

         2.   Transcribing and Encoding Errors

         In the Five-Plant Study, laboratories used GC/MS or GC/CD analytical
methods.  The data were transcribed from instrument readouts to data sheets
and, in some cases, from data sheets to typewritten report forms.  EPA then
encoded the data from the typewritten forms and data sheets into its
Five-Plant computer database.  The Agency's 1982 review of printouts from this
database revealed occasional disparities between the printout and results that
had been reported by laboratories.  Typical errors were the transposition of
results from treated and untreated effluent streams,  typographical errors, and
encoding errors.  Copies of printouts with suspect values noted were sent to
                                   C-29

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the original EPA contract laboratories and to the original participating CMA
laboratories for confirmation.  Confirmed transcription and encoding errors
were corrected.  In a few instances, laboratories corrected the GC/MS results
after re-examining the original analytical data recorded on magnetic tape.
The laboratory originally responsible for each data point made the final
decision on correcting that data point.

         3.   Errors from Improper Application of GC/CD Methods

         When the Five-Plant Study began, EPA sent samples to an EPA
contractor laboratory for analysis using GC/MS methods.  From these results,
EPA determined which GC/CD methods its contractor laboratory should employ for
monitoring the treated and untreated wastewaters at three of the five plants
for the 30-day period.  In contrast to the flexibility afforded EPA contractor
laboratories during the Verification Phase, EPA contractor laboratories in the
Five-Plant study were not permitted to modify the selected GC/CD methods or
employ alternate methods, if an interference was suspected.  EPA now admits
this approach was faulty.  The contractor laboratories should have been
permitted the same flexibility in response to GC/CD interferences, or only
GC/MS methods should have been employed.

         For each plant, a technical contractor's review compared GC/CD data
from EPA's contract laboratory with GC/MS results from the CMA plant
laboratory, or CMA contract laboratory.   These data showed significant
disparities.  EPA was then faced with determining which data were acceptable.
Two approaches were applied:  (1) the GC/CD and GC/MS results were compared
statistically; and (2) the technical contractor's review of the GC/CD data
evaluated concerns such as the potential interference with GC/CD peaks by
non-priority pollutant compounds.  The EPA review staff and technical
contractor reviewed the chromatograms supporting the GC/CD data at the IFB
contractor's facility.  In addition, the IFB contractor reviewed the
chromatograms and detection limits data and subsequently recommended some of
the major changes described next.

         The results of the statistical comparison, a paired-sample T-test,
were inconclusive because of a shortage of both GC/CD and GC/MS analyses from
split samples.  EPA's review contractor recommended removal of all GC/CD data
from the CMA Five-Plant database because of the disparities with GC/MS
results, the impossibility of determining which GC/CD data points were valid,
and the failure to use the interference elimination options which had been
employed in Verification Phase GC/CD methods.

         Following the review contractor's technical recommendation and on its
own technical evaluation, EPA decided to delete all GC/CD data from the
Five-Plant database.  Deletion of GC/CD data reduces the total number of data
points by approximately 60 percent.  However, GC/MS data exist for all the
pollutants detected by GC/CD at all plants.  EPA has determined from
interlaboratory comparisons that the remaining GC/MS data are adequately
precise and accurate for developing the proposed BAT effluent limits.
Therefore, all GC/MS data from the Five-Plant database have been retained.
                                   C-30

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                                 EXHIBIT C-l
              ORGANIC CHEMICALS VERIFICATION  (OCV) PROGRAM
METHOD VALIDATION FORM
                           LABORATORY:
1.  APPLICABLE OCV DATA
    METHOD 	  PLANT
    POLLUTANT
                                               STREAM
    METHOD SUMMARY
    2.1  Extraction:
    2.2  Column:  Length _
                  Packing
    2.3  Detector: „	
                                 I.D.
Plates
Est
    CONFIRMATORY DATA
    3.1  Confirmed by GCMS
         Other 	
         3.1.1  Qual confirm:   Yes
         3.1.2  Quant confirm:  Yes
                GC 	 ug/1    GCMS
                                  2nd Column

                                      _  No _
                                      _  No _
                                      _ ug/1
     2nd Temp
    3.2  Describe "other" confirmatory technique
    3.3  Describe how confirmatory technique was applied:
4.  QUALITATIVE DETAILS (not required if results are confirmed both
    qualitatively and quantitatively by GCMS)
    4.1  Retention time window as compared to standard
         4.1.1  Absolute ± 	 sec   Est 	   Meas 	
         4.1.2  Relative ± 	   Est 	   Meas 	  Int Sd 	
         4.1.3  Specification applied?  Yes 	  No 	  Est 	
                                C-31

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    4.2  Peak width @ half height
         4.2.1  Of standard:   	 mm
         4.2.2  Before spike:  	 mm     Interference present?
         4.2.3  After spike:   	 mm       Yes 	   No 	
    4.3  Specific detector/interferences
         4.3.1  Nature of potential interferences
                Responsive 	
                Non-responsive
         4.3.2  Specificity ratio (response to pollutant divided
                by response to interference:  FID = 1.0)
                Responsive 	      Est 	  Meas 	
                Non-responsive 	  Est 	  Meas 	
         4.3.3  Other evidence that only a single compound was measured

    4.4  Methodology to remove interferences
5.  QUANTITATIVE DETAILS
    5.1  Calibration
         5.1.1  Int Std 	    Ext Std 	
         5.1.2  Number of initial calibration points 	
         5.1.3  Frequency of calibration check 	
    5.2  Detector Range
         5.2.1   Within upper linear limit?   Yes 	   No 	
         5.2.2   Within calibration limit?    Yes 	   No 	
         5.2.3   Pollutant level measured:  	 ug/1
         5.2.4   Detection limit:  	 ug/1   Est 	   Meas
         5.2.5   Signal-to-noise ratio of pollutant measurement

6.  STATISTICS
    6.1  Replicates
         6.1.1  Initial number:  	   % MD 	  Est 	  Meas .
         6.1.2  Ongoing:  	  % RSD 	  Est 	  Meas 	
         6.1.3  Control limits:  Upper: 	   Lower: 	
                               C-32

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    6.2  Inter-lab comparisons:  % RSD 	   Est 	  Meas
         List other labs 	
7.  COMPARISON WITH 1979 FEDERAL REGISTER 600 SERIES METHODS (if method
    used was 600 series method, skip this section)
    7.1  Nearest 600 series method:  	
    7.2  Expected comparison
         7.2.1  Detection limit:  Yes 	  No 	  Est 	  Meas 	
         7.2.2  Linear range:     Yes 	  No 	  Est 	  Meas 	
         7.2.3  Specificity:      Yes 	  No 	  Est 	  Meas 	
         7.2.4  Reproducibility:  Yes 	  No 	  Est 	  Meas 	
    7.3  Was 600 series method available at the time this sample
         was analyzed?  Yes 	  No 	
    7.4  Do you feel that the method used produced data comparable
         to the 600 series method on this sample?
         Yes 	 No 	
         If no, why not? 	

8.  RECONCILIATION WITH PRODUCT/PROCESS
    8.1  Is pollutant presence consistent?  Yes 	  No 	
    8.2  Was pollutant found in raw water or blanks?
         Yes 	 No 	
    8.3  Evidence that matrix was constant:
9.   REGULATORY
    I believe the pollutant reported on this form was
    qualitated and quantitated accurately.
    Yes 	  No 	

10. PERFORMANCE EVALUATION:  Date 	
                              C-33

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11. Other comments
Signature:	    Date:
    Print:	
                               C-34

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                                 REFERENCES
AMORE, F.  1979.  Good analytical practices.  Analytical Chemistry 51:1105a.

TAYLOR, J.K.  1981.  Coordination for chemical measurement assurance and
voluntary standardization.  Center for Analytical Chemistry, U.S.  Department
of Commerce, National Bureau of Standards, Washington, B.C.   From a letter to
OCB, September 3, 1981.

U.S. ENVIRONMENTAL PROTECTION AGENCY (USEPA).   1977.   Sampling and Analysis
Procedures for Screening of Industrial Effluents for Priority Pollutants.
USEPA, Environmental Monitoring and Support Laboratory, Cincinnati, Ohio.
March 1977 (revised April 1977).

WEBB, R.G.  1978.  Solvent extraction of organic water pollutants.  J.
Environmental Anal. Chem. 5 (3):239-252.
                                   C-35

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       APPENDIX D
ACTIVATED CARBON AND STEAM



 STRIPPING QUESTIONNAIRES

-------
ACTIVATED CARBON QUESTIONNAIRE
            D-l

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                              Company
                             Location
                                 Date
          U.S. ENVIRONMENTAL PROTECTION AGENCY
                ORGANIC CHEMICALS BRANCH
              EFFLUENT GUIDELINES DIVISION
   SURVEY OF ACTIVATED CARBON WASTE WATER TREATMENT SYSTEMS

The purpose of this survey is to gather data on activated carbon
treatment for the removal of priority pollutants from waste water
discharges.  Of particular interest are the procedure for design
of systems and the availability of procedures for predicting the
performance of activated carbon on priority pollutants, especi-
ally when other adsorbable or nonadsorbable compounds are present

Relatively simple and short responses to the questions will
generally suffice.  However, any amplification or additional
comments will be appreciated.
                          D-2

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                                  Company
                                 Location
                                     Date
PART I:   SYSTEM IDENTIFICATION
1.   Company
2.   Location
     Person responding or to whom further questions should be sent
3.   Do you have an activated carbon system (ACS)  operating on a
     vaste water stream containing one or more of the priority
     pollutants listed in Table I attached?
           Yes ___ If the answer is yes, please continue with
                   this questionnaire.  If more than one instal-
                   lation is involved, copy this questionnaire
                   and complete one set for each installation.

           No  ___ If the answer is no, please return the
                   questionnaire; no further data are required.
                               D-3

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                                Company
                                Location
                                   Date
PART II:   SYSTEM DESCRIPTION

1.   Please diagram the treatment system using gross blocks for
     pretreatment and post-treatment (if used) and more detail
     for the activated carbon system (see examples).

2.   Give flow rate of waste water                  Ib/hr
     Temperature                                    *F
     Composition (at entrance to ACS contact)
3.   Effluent composition after ACS contact.
4.   AC  loadings (by component, if available)
           	lb/100 Ib AC
5.   Residual on AC after regeneration or reactivation  (if used)
                            D-4

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                                  Company

                                 Location

                                     Date
PART ZI:  EXAMPLE DIAGRAMS
 Waste
 Water
 Source]
                                      off line carbon    r~~T_
                                     \bed & regeneration I   {Scrubber
                                                       ||   |
                     FIXED BED SYSTEM
                                                          .fter Burner
                                                       nace   /
                                                             /

Pzetieaonsit
(Filter)
etc

rS- -

5?

^/
V ^
\ ^
_ .V..**
Carbon
Bed(s)
L
y
^.
/
/
/
/

/
/
Post-treatsnen-
(aeration
chlorination)
etc
i
Effluent
waste
Water
Source
•*—!
— \r\
v^y





|K
P

,

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                              Company
                             Location
                                 Date
FAX? Ill:   DESIGN BASIS

1.   Has system bench scale tested or piloted before design?
                     Yes
                     No

2a.  If answer to 1 is yes:
     Describe tests and note whether individual components, a
     synthetic mixture, or the authentic plant effluent was used,

2b.  If answer to 1 is no:
     Describe basis for design of plant unit.
                            D-6

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                                Company
                               Location
                                   Date
FAST IV:   COMMENTARY
Based on experience with the unit described,  comment on the
following:

1.   Can AC systems be specified from available design parameters
     without need for tests?
2.   If testing is believed necessary, describe briefly minimum
     program to assure meeting effluent guidelines.
3.   How does the actual performance of the unit described corre-
     spond with the predicted performance?  If available, give
     quantitative results for individual components.
4.   By hindsight, how would you modify  the procedure used  for
     •pecif/ing and designing  the  subject  systemr
                            D-7

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STEAM STRIPPING  QUESTIONNAIRE
              D-8

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                                           Form Approved
                                           OMB No. 158-R0160
                                          Company

                                         Location

                                             Date
                           STEAK  STKIPrING


Copy and answer Parts I through IV of this  questionnaire for  each
steam stripper used to reduce the raw waste  loading  prior to  direct
discharge or discharge to an end-ol-pipe  treatment system  (wnether it
be a publicly owr.ed treatment worns, a regional industrial  treatment
system, your own on-site treatment system,  cr otner  system  such  as a
nearby refinery's biological treatment system).
                                 PART  1
1.  List the names ot all process(es) whose  waste water  discharges
constitute a portion of the  feed  (charge)  to the steam stripper.  In
the event more than one process waste water  str^ax  manes up the  ccarge
(feed) to the stripper, give the approximate percentage  or  eacn  stream
on a flow or weight rate basis.  Please  place tne percentages  or  each
stream in the table below.
    Stripper Feed Source                *Percer.tage  of  feed

1.	          1.    	

2.	2.    	

3.                                 3.          „____	
    Total feed
    tlow  (gpffi)            and/or        weight (Ib/hr)
* Indicate whether basis is  weight  (Ib/hr)  or  flow (gpm)


                                 D-9

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                                          Company

                                         Location

                                             Date
                               Part II
This part of the survey requests information adequate to assemble a
trial material balance around the stripper.  Operating data is the
preferred source of information requested in this part.  Flow or
stream composition data based on lindted monitoring or calculations
(engineering estimates) is required as an alternative.

1.  Please attach a process flow diagram of the steam stripper.
Kindly numoer and label all waste streams that are associated with tne
operation of the stripper such as the charge (feeJ), reflux, overhead
product, decanter water, bottoms, etc.  Indicate in your drawing major
equipment items such as pumps, heat exchangers, etc.  A sample sketcn
has been provided for reference.

2.  Complete the attached Table I with the information requested for
each stream numbered in the sketch prepared in (1)  above.  Note that
two sets of information are requested.  One set consists of general
Stream characterization parameters such as flow, temperature, pH, BOO,
Toe, etc. with spaces for additional or different characteristics, and
organic or inorganic compounds known to be present.  The second set
labeled "component" refers to priority pollutants identified or
indicated to be present in the waste waters associated with the
stripper.
                                  D-IO

-------
         Company



        Location



            Dare
D-ll

-------

!
I Par* II
|
!





Sampl



e Process FT
••Steam Str-


ew 'Diagram
pping

I
!
1
!




                                                    _ J.. ...
                                                      Cujt
>S
fad1 (charge)
                 fred

                   ,
                   I
                         fecoverfc* hue/ro car Joan
                                           or
                              — •!-  /
                                                    D-12

-------


-------
                                          Company
                                         Location
                                             Date
                               Part III
This part of the survey requests information essential to evaluate the
operating performance of the stripper and the energy consumption of
the opera tier per unit of pollutant remove a from the waste water.,
1.  Utility Requirements
    A.   Steam Requirements
              Pressure
              Temperature _ °i
              Rate _ Its/hr
Is open steam used or does the coluirn utilize a reooiler?
    ______________ Cpen Steam               Re toiler

    B.   Cooling Water Use
              Condenser Influent Temperature   _ °F
              'Condenser Effluent Temperature   _ °£
              flow Rate _ gai/hr.
    C.   Other Energy Requirements
              Electricity         _ *wh
              Compressed air                          scf m
              Inert gas                               scf m

2.  Column Specifics
    (The sketch called for in 11(1) aoove can be  expanded upon to provide
    the following information) .
                                  D-14

-------
                                        Company

                                       Location

                                           Do re
Part

A.

fi.

C.
Ill  (Continued)

Feed  Rate 	
feed  Temperature
Opera-ting Pressure

       Top _
           Bottom
D.
Operating Temperature

       Top 	
           Bottom
L.

F,
Column  Diameter
Nuii.ber  of  Theoretical
Trays  (if  known)	
                                   No.
    Actual Number of Installed
    Trays  or Packing Height,
           Trays
           Packing.
                                  D-15
.Ib./hr.
                                               usia
                                                °F
 ft.
fi.
I.
J.
K.
L.
K.
N.
O.
P.
Type of
Iray Sp
Overall
Reflux
Reflux
Reflux
Bottoms
Bottoms
Materia
Trays or Packing
acina ft.
Column Height ft.
Ratio* (if anv)
Rate Ib./hr
Temperature ° F
flow Rate Ib./hr.
Temperature °F
Is of Construction
                                         No. or ft.  (specify)
*Use overhead flow rate as the basis of this value

-------
                                          Company

                                         Location

                                             Dare
    Part III (Continued)

              Column or Vessel
3.  Specify the ultimate disposition ot column overhtaac  (i.e.,
incineration, returned to process, etc.) tor both the aqueous and -the
organic phases.
4.  Specify the method of disposition of column bottoms.   (i.e.,
discharged to biological treatment, discharged directly  to surface
waters, re use a as cooling tower max.e-up, etc.)
5.  Are there any substances presenfiT* "the  influer.t a LI- can -co the
steam stripper that interfere with the removal  of  the pollutant(&)
listed in  (2) above.   (i.e., maximum  coiling azeotropes,  pn
adjustment, foaming, scaling, necessity  to equalize  flow or fefei
concentration, etc.).  If so, please  list  and exj-Iair -...- r.ature of
the interferences and  any methods devised  tc minimi2•=• -ir eliminate
these interferences.   Also explain how successful  these methods have
been.
                                D-16

-------
                                          Location

                                              Date
    Part III (Continued)
6.  Operating Specifics


    A.  Is the steam  stripper  operated in a continuous or uatc^ rr.cie?
    If batch, explain.
    B.  Explain the  method of treatment of th-= process was.ze»atfcr  t**
    as normally discnaiged to the strijper >»h2r. tnr stra:.  striper i
    dcwn for repair.
                                    D-17

-------
                                          Company

                                         Location

                                             Date
                               Part IV
your responses to the following questions will be used to determine
the desireability of additional fcllow-u{. relating to capital and
operating costs associated with the steam stripper.

    A.   Was the steam stripper installed as a new piece of
         equipment?
         Yes 	  No
    B.   When was the steam stripper installed?
    C.   Do you have detailed cost information (both capital and
         operating) relating to the steam stripper as a separate unit?
         Yes 	     No
    D.   Are you willing to share this cost information with ZPA to be
         used to verify the cost of the installation of steam
         strippers for the treatment of waste water.
         Yes 	     No 	

    £.  Operating Labor

           Direct Operating	work-days/yr.

           Maintenance	worx-days/yr.

           Supervisory	_woric-days/yr.

    F.   Do you have V-L equilibrium data which was used to design
         the stripper from your own experiments, or Henry's Law
         Constants, or vapor pressure data, or activity coeificient
         data, or otner correlations?

         No	     Yes	     Identify which one       	
                                  D-18

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                                       Company

                                      Location

                                          Dare
Part IV (Continued)
G.    Do you  have information regarding the cost impacts of
      installing the stripper or. tne following off-site activities?
      (check  either  Yes or No, or indicate (a) , (b) or  (c) as appro-
      priate)

                                         Yes     No

      a.    Steam generation or a
           major revision in dis-
           tribution

      b.    electrical substation
           capacity

      c.    Instrument air capacity

      d.    Valve/Fiping/wiring
           systems to supply a,
           b,  or c                        (a)  (b) {c)     (a) (h> ic)
                                D-19

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    APPENDIX E
TREATABILITY STUDIES

-------
                                 APPENDIX E
                           TREATABILITY STUDIES*
GENERAL

    The  following  is  a  summary  of  treatability  studies  sponsored  by  the
Organic  Chemicals Branch  on activated sludge,  activated  carbon  adsorption,
steam  stripping,  and organic resin  adsorption  processes.   The  intent  of the
research was to collect data  on  biological  and  physical  constants for specific
priority  pollutants  and   derive  methods   for  predicting   the  removal   of
pollutants  in  single  and  multi-component   waste  streams.   These data  were
intended for use  in  benchmarking  the  Agency's computer Model  (see  Appendix
K).

BIOLOGICAL TREATMENT

Introduction
    Activated sludge treatment is perhaps the most common treatment technology
practiced by industry.  To determine which  pollutants are  effectively removed
by  this technology in  real systems,  the Organic Chemicals Branch developed  a
pollutant-based  treatability  model  for activated  sludge treatment.  Beyond the
evaluation  and application of  existing  models  of biological  processes,   data
for  specific  priority  pollutants   were  required  to  accurately   predict  their
susceptibility to  removal,  their  effects on  the  biological treatment process,
and their fate during the treatment process.
*From  U. S.  Environmental  Protection  Agency.  1981.  Contractors Engineering
Report  Analysis  of Organic Chemicals  and Plastics/Synthetic Fibers Industries,
Effluent Guidelines Division,  Contract No. 68-01-6024,  Chapter 3.
                                   E-1

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         Biological  treatment  involves the  breakdown  and  stabilization of  organic



material by  aerobic or anaerobic  microorganisms.   Organic matter is removed from



wastewater by microbial oxidation and cell synthesis, essentially accelerating the natural



water  purification mechanisms.  Bacteria  are  the primary organisms  involved  in  the



transformation  of waste  constituents  ultimately  into  carbon  dioxide, water,  cellular



building  blocks, and energy.  Treatment processes available for industrial application



include:  variations  of the activated sludge process, aerated lagoon systems, oxidation or



contact  stabilization ponds,  trickling filters,  rotating  biological discs, and  anaerobic



lagoons,  or  digesters.   Historically,  the activated  sludge process,  in which  aerobic



microorganisms are  mixed with the influent wastewater and subsequently removed as a



sludge, has had the  broadest application to  industrial wastes.  The toxicity of the waste,



the biodegradability of the waste  (typically judged by  the BOD/COO ratio), and  the



metabolic  rate of  the microorganisms  (i.e.,  the effective removal  rate)  all influence



process efficiency.



         Basic environmental conditions (i.e., proper microbial growth conditions) must be



met for  microbial metabolism and  stabilization of the waste organics to occur.   These



conditions include (I) oxygen availability, (2) near neutral pH, (3) available growth-limiting



nutrients, nitrogen  and phosphorus, (4) absence of toxic materials,  and  (5) adequate



mixing.  Further, biological processes can be designed to operate optimally by properly



controlling the following rate-controlling variables:  (I) microorganism concentration,  (2)



bacterial acclimation or adaptation, (3) temperature level, (4) contact duration and mode,



and (5) organic feed  concentration.



         The activated sludge process was chosen for the  modeling  effort conducted by



Catalytic,  Inc., because it  has proven  to be cost-effective in treating relatively  low



concentrations of organics found in  industrial wastes, and can be designed to provide more



operational  flexibility than other types of biological treatment.  A  flow diagram  for a
                                        E-2

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typical activated sludge  process, in  which aerobic microorganisms are mixed  with  the

influent wastewater and subsequently removed as sludge, is shown in Figure E-l.


                                   FIGURE E-l

                      TYPICAL ACTIVATED SLUDGE PROCESS

                              ACTIVATED
                              SLUDGE
                              REACTOR
 RAW
 WASTE
 WATER
           PRIMARY
          CLARIFIER
          (optional)
                                                              FINAL
                                                            CLARIFIER
 WASTE
.SLUDGE
 TREATMENT
                                 SLUDGE RECYCLE

SOURCE: Kinconnon and Gaudy, no date.

Biokinetic Models

         The theoretical approach used in the design of biological treatment systems is to

develop mathematical models which depict relationships between parameters that control

efficiency of microbial growth and substrate removal.  The purpose of these design models

is  to  provide predictive  equations consistent with the underlying  metabolic  principles

governing the waste treatment process.  The general approach to developing  biokinetic

models is to write mass balance equations describing the mass rate of change !n substrate

(i.e., organic pollutants) and in biomass of the microorganisms.  The models incorporate

various assumptions regarding fundamental relationships governing microbial growth, and

factors derived from laboratory bench scale or pilot plant studies.

         Various models,  or  kinetic approaches,  are available for use  in  designing

activated  sludge  processes.    The  basic   formulas for  four well-known  models—

Eckenfelder's,  McKinney's, Lawrence  and  McCarty's, and Gaudy's—are  presented  in

Table E-l. A materials balance for  substrate (S) can be  derived, as shown in Table E-2

from each equation.
                                       E-J

-------
                                 TABLE E-l

         KINETIC APPROACHES FOR THE ACTIVATED SLUDGE PROCESS
Design Approoch

Eckenf elder
              Basic Formula
                       -  Se) F

                        S  X
                               si
-------
                               TABLE E-l (Continued)

k .      = Maintenance energy coefficient (all models)
6       = Sludge retention time (mean cell retention time)
a       = Recycle flow rate

SOURCE:  Kincannon, 1979.
                                       E~5

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Gaudy
                                  TABLE E-2

                    MATERIALS BALANCE FOR SUBSTRATE, S
Balance

Model
Eckenfelder
McKinney
Lawrence-
McCarty
Mass Rate
of
Change
H- -
H -v •
dS T,
dt -v -
Mass Rate
due to
Inflow
F.S. -
F.S. -

F.S. -
Mass Rate
due to
Outflow
F.Se -
F.Se -

F.Se -
Mass Rate
due to
Metabolism
KeX.Se.V
Ve'7
S.
KV .^M^^H^^ '
* • v AC *
                                -Pi
Where:

V
X

F

F
 w
 t
 se

 "m
K
  max
 f
  t
  Volume of the reactor

  Influent BODj

  Effluent BOD5

  MLSS or MLVSS

  Influent flow rate

  Solids wastage flow rate

  Eckenfelder's 1st order substrate removal rate constant

  McKinney's substrate removal rate constant

  Maximum substrate utilization rate (Lawrence and
McCarty)

  Saturation constant (Lawrence and McCarty, Gaudy)

  Maximum specific growth rate (Gaudy)

  True cell yield (all  models)

  Recycle flow rate
SOURCE:  Kincannon, 1979.
                                      E-6

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         Based on an comparison of these four models by Kincannon and Gaudy (no date)



and Kincannon (1979), certain relationships are held  in common in each  of the mass



balance equations:



         I.    The mass  rate of change of substrate in the reactor is equal to the rate of



              change in concentration of substrate (dS/dt)  multiplied by the volume of



              the reactor (V).



         2.    The rate of change of substrate concentration is increased by the inflow of



              the substrate.



         3.    The rate of  change of substrate concentration is decreased by the flow of



              substrate  concentration out of  the  reactor, and  by  the  rate at which



              substrate is utilized for growth of the microorganisms in the reactor.
                                        E-7

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        Eckenfelder's ond McKinney's Models


        Eckenfelder's and McKinney's models are developed assuming that the irate of


substrate removal is a first order reaction. The models differ in the relationship used to


describe the substrate utilization rate.  In McKinney's model, this term is dependent only


upon the substrate concentration in the reactor (Sg) and a substrate removal rate constant


0
-------
         Goudy's Model



         Gaudy's model, also based on  Monod kinetics, differs from the above three as a



result of writing the mass  balance around the bioreactor  rather than  around the whole



activated sludge process. This approach separates the biological unit process of biological



growth  and substrate utilization  occurring  in the  activated sludge tank from  the  unit



operation of physical separation  accomplished  in  the  clarifier  (see Figure E-2). As  a



consequence of writing the balance around the bioreactor,  the effect of a (a  factor



related  to solids recycling)  on the substrate  balance is noted.  The mass rate of substrate



utilization  is related to the growth of  the biomass and  the biomass "constants", i.e., the



maximum specific growth rate (ymax), the saturation constant (K ), and the  "true" cell



yield (Yf).
                                         E-9

-------
                                    FIGURE E-2

            FLOW DIAGRAM, ACTIVATED SLUDGE PROCESS SHOWING
                   NOTATION AND MASS BALANCE ENVELOPES

. 1 —1
1 I
1
lS,.P.X0l
1 j
1
1

1
1
1
1
1
1
1

St,x

V
BIOREACTOR

/ — x
1 / \
n*0)p ' . f njin 	 VIP-PW), X..S.

\ J
\ ^>*~^ ^^r


Of, X.

?m i X» , S«

         I	
SOURCE:  Kinconnon, 1979.

Doto Development for Siokinetic Models

        One feature common to all of the kinetic approaches described above is  the

inclusion of biokinetic  constants, or K-rates.  Reliable biokinetic constants,  values

determined empirically  in wastewater  treatability studies, are necessary  if the design

models are to have an accurate predictive application.

        In the  Catalytic modeling approach, kinetic  formulas  are used to calculate

removal of organic  matter by  the activated sludge process.  As  Catalytic's approach

involved the determination of rate coefficients for each product/process waste load, two

types of treatability data were required:

        I.    Reaction rate constants for BOD, and

        2.    K-rates specific to the pollutant regardless of its product/process source.

The individual  process stream data identified during field sampling were used to calculate

a  weighted-average  reaction  rate for  the  summation  of the  BOD  load  from  the
                                       E-10

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contributing product/processes.  Thus, the activated sludge process design  was based on

that weighted-average BOD reaction rate (K-rate) that describes  the total plant waste.

For the development of pollutant-specific K-rates,  treatability data requirements  were

two   fold:    the  biological  reaction   rate  (K-factor),   and  the  lowest  attainable

concentration.

         Based on  data obtained  from OCB's screening and  verification  sampling and

analysis program, from EPA's 308 questionnaires,

and from Catalytic's laboratory test results, treatability

factors for individual  pollutants were calculated using the following  equation:


                                    K -  So-sose
                                          TXSe


where:

         K = Treatability factor for any priority pollutant (day~ )

         S   « Influent concentration (mg/l) of the priority pollutant

         S   s Effluent concentration (mg/l) of the priority pollutant

         X = Mixed liquor volatile suspended solids (mg/l)

         T s. Basin detention time (days).
 For a more complete discussion of the development of the treatability factors used in
the Catalytic computer model,  see the 1980 Catalytic Report.  The treatability data
developed by Catalytic during the 1980 analysis of the applicability of activated sludge
appear in the Parameter and Treatment Selection file (Catalytic, 1980).


                                         E-ll

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The  minimum  attainable value  for  a priority  pollutant  in  the treated  effluent was



considered to be the  lowest value observed in an effluent for  which data was considered



acceptable.  Of the 115 organic priority pollutants,  biological  treatability factors for  86



pollutants were established in this manner.



         For 20 other priority pollutants, the biological treatability factor was estimated



by using Eckenfelder's Modified (zero-order) Equation:
                                           xt




where:



         S  = Influent concentration, mg/liter



         S  = Effluent concentration, mg/liter



          X = Mixed liquor volatile suspended solids concentration



            (MLVSS), mg/liter



          t = Hydraulic retention time, days



          K = Reaction rate constant, day" .





         However,  there were several areas where information was needed to support the



computer modeling effort relative to biological treatment.  Specifically, more data were



needed  on  the  relative treatability of certain compounds, compound  groups,  priority



pollutants and process raw  waste loads.  More work was needed relative  to finding  and



supporting the best predictive mathematical process model.  As such, a main objective of



the Catalytic work was to refine or continue to verify the method of combining kinetic



factors of components of a mix to determine  the overall treatability of the wastewater.



To have  run laboratory studies in  order to  determine  biokinetic  constants  for  every



possible combination of organic chemicals would  have been prohibitively expensive  and



time consuming. However,  the  determination of biological constants for wastes contain-



ing single compounds was feasible; and from this data constants could be combined to give
                                        E-12

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a single constant for wastes containing a mix of organic compounds.   Grau-type K values

as high as  20 day" have been encountered  and values between  2 and 10 day"  have been

determined for other chemicals.  There is, however, a lower range of K's for which data is

lacking.  Systems  utilizing chemicals with low K values are the most difficult  to operate

because upsets are easier to  provoke and the slowly degradable organic chemicals often

present handling problems.

         Methodology Development

         To  address the  problem  of an inadequate  data  base,  Catalytic, Inc.,  under

contract to  Effluent Guidelines Division's Organic Chemical  Branch has developed a

methodology for bench-scale  biological studies to evaluate treatability factors (K-factors)

of selected organic compounds.  The treatability of various classes of organic  chemicals

had  previously  been  grouped  through  the use  of   literature  surveys  according  to

degradability.  As such, five general classes of degradability were established, as shown

in Table E-3



                                     TABLE E-3

                            CLASSES OF DEGRADABILITY
CLASS K RATE
1. Highly degradable
II. Easily degradable
III. Moderately degradable
IV. Slowly degradable
V. Biostatic or biotoxic
20
10
2
0.5
0
 The best method of combining K values (e.g., straight average, rate limiting K, weighted
average, etc.) has not yet  been deter-mined.   Presently, the average of component K
factors is being used.

 Chemicals were classified by existing degradation data or by structural analysis.
                                        E-13

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         InitiaLwork to gain more precise information on specific treatability factors and



on combining K-rates was performed by Catalytic from 1976 to 1978 (Catalytic, I979b). In



these initial experimental systems, the chemical or chemicals of interest were used as the



sole source of carbon for the bacteria.  This  type of  laboratory operation represents an



artificial  situation which is not  likely  to  occur in a full scale chemical plant.  Also,



because of the very specific biological population which develops under these conditions,



operational problems were encountered.



         Thus, a new laboratory methodology was devised as part of a Phase 2 study to



overcome some  of these  operational problems.  The new systems used sludge age  as a



variable, since this parameter is  required to  evaluate all the current biological  models.



Another significant change from the earlier work was  that a portion of the feed for  each



system was made up of a  mixture of readily biodegradable organic compounds, in addition



to the chemical  of interest.   This  "base mix" was composed of  ethylene glycol,  ethyl



alcohol,  glucose, glutamic acid, acetic acid, phenol, and nutrients  (ammonium  sulfate,



phosphoric acid and salts) as required.  In addition to  stabilizing the bench scale  system,



the  impact of non-biodegradable  and/or slightly  biodegradable compounds on biokinetic



rates could then be evaluated.



         The  kinetic  equation  used in  the  Catalytic system  is  the Grau  model (or



Eckenfelder's second  order equation).  This approach has enjoyed acceptance by industry



and  allows more  flexibility in predicting  effluent quality  under varying influent  con-



centrations, which typically occur in industrial biological treatment systems, than does a



first order equation.   Other kinetic models such  as those utilizing solids retention  time



(SRT) as a primary variable (which  includes the Lawrence and McCarty models  and the



Gaudy model), were  considered less extensively  verified.  The  Grau  equation is shown



below:
                                      E-14

-------

                              e        xt


where:

         K = kinetic constant

         S  = BOD influent concentration (mg/liter)

         S  = BOD effluent concentration (mg/liter)

         X = MLVSS (mg/liter)

         t = Aeration time (days)


         Gaudy (I960) has pointed out some limitations of the Grau model; it is not a good

mechanistic relationship because it combines at least four separate biokinetic constants

known to be determining factors in characterizing the behavior of activated sludge into

one "constant",  and combines  separate engineering  control parameters which indepen-

dently affect S . Further, operating conditions such as net specific growth rate which can

affect the performance of an activated sludge system, are  not built into this model for

assessing removal  of priority  pollutants.   However, Gaudy also noted that industrial

information expressed in terms of the Grau model was more readily available, and that

the model  would prove  useful for estimating effluent  guidelines relating to biological

treatment for a broad group of combinations of compounds.  He has recommended the

gathering of kinetic data applicable to the testing of a variety of models in order to verify

or modify values used in the  Catalytic computer model; such research is presently in

progress at Oklahoma State University (see the following section).

         To obtain  a K value for a specific chemical  based on the Grau model, Catalytic

ran several bench-scale  systems to  obtain  different effluent BODs.  The values of

 o  o" e   were plotted versus the effluent BOD values; the slope of the  resultant line
    Xt
equaled the K  value for the chemical in question.
                                       E-15

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        From  Catalytic's Phase 2 experimental  work  came  kinetic  information  on 15



compounds,  tested with "base mix" only and in combination, and run at various loadings.



Compounds selected for study represented known raw materials, products and by-products



expected in  industrial effluents, groups of chemical  compounds for which little biotreat-



ability information was available, and priority pollutants where possible.  Other primary



considerations in selecting compounds for  study included solubility,  volatility, chemical



stability in  water,  toxicity,  carcinogenicity, odor, flammability, chemical  compatibility



with the other chemicals in a mix, availability, and  cost.  See Table E-A for a list of



compounds studied according to the Catalytic methodology.  Results of this experimental



work are present in the Catalytic files (Catalytic, I979b).



        Oklahoma State University Studies



        The methodology for  determination of biokinetic constants in activated sludge



models  developed by  OCB  and their  contractor,  Catalytic  is also  being applied by



researchers  at Oklahoma State University.  An EPA-sponsored  study by Kincannon is now



in progress with objectives consistent with those of the Catalytic study:



         I.    To  determine biokinetic  constants for  wastewaters containing 24 major



              organic compounds



         2.    To determine a  method  for combining biological constants for  evaluating



              complex waste streams.



Biokinetic constants are being determined  for design models  developed by Eckenfelder,



McKinney, Lawrence and McCarty, and Gaudy.  To develop a methodology for combining



K-rates, three  compounds  are run individually and  in  combination,  with pilot  plants



operated at three different sludge  ages  for each compound or  combination. In addition,



specific compounds in the off gases from the pilot plants are being measured to determine



the strippability of volatile organic compounds.  Preliminary results  for  four sets of



priority  pollutants  (three pollutants run  individually  and  in  combination) have  been
                                        E-16

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                          TABLE E-4
               ORGANIC COMPOUNDS STUDIED IN
    CATALYTIC'S PHASE II BENCH-SCALE BIOLOGICAL SYSTEM
N-Butyl  Phthalate (nBP)   75%, Base Mix*  25%
0-Nitrophenol  (ONP)** 75%,  Base Mix 25%
Maleic Acid 75%,  Base Mix  25%
Acetonitrile 75%, Base Mix 25%
Acetonitrile 25%, ONP 25%, Maleic Acid 25%, Base Mix 25%
Base Mix (with and without phenol** in the mix)
Butyl Acetate 75%, Base Mix  25%
Methyl. Cellulose 75%, Base Mix 25%
Methyl Formate 75%, Base  Mix 25%
Melamine 75%,  Base Mix 25%
Catechol 75%,  Base Mix 25%
Formamide 75%, Base Mix 25%
Ethanol  75%, Base Mix 25%
Ethanol  (denatured) 75%,  Base Mix 25%
Isophorone ** 75%, Base Mix  25%
Ethylene Dichloride** 75%, Base Mix 25%
2-Naphthol-3,6-disulfonic  Acid 75%, Base Mix 25%
l-Phenyl-2 thiourea 75%,  Base Mix 25%
Base Mix without Glutamic  Acid 100%
Base Mix without Ethanol  100%
Base Mix without Glucose  100%
Methyl Formate 25%, Formamide 25%, Maleic Acid 25%, Base Mix  25%
*Base mix is composed  of ethylene glycol, ethyl  alcohol,  glucose,
 acid, acetic acid,  and  phenol.
**Priority pollutant.
                             E-17

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reported in four quarterly reports (Kincannon, I980a and I980b, and Kincannon and Stover,
I98la and I98lb). See Table E-5 *or the list of compounds studied.
Effect of Priority Pollutants on Biological Treatment
         The optimal operation of an activated sludge process  is subject  to change as a
result of a number of environmental conditions, including the presence of compounds toxic
to the system's microbial population.  These several  conditions acting simultaneously on
the biological system make it difficult to determine whether a particular chemical, or a
combination  of toxic compounds,  is responsible for an observed malfunction of a waste
treatment  process.  Such a data base is essential to the  development of pre-treatment
requirements  for  industrial  wastes containing priority pollutants to treatment works
employing the activated sludge process.
         The effect  of 2k priority pollutants on the performance of batch and continuous
flow  bench-scale  activated  sludge pilot  plants  was studied  by Gaudy et  a[.  (1979).
Additionally, • erght  of  these compounds were studied  in continuous flow pilot plants
operated at a net  specific growth rate (u ) of 0.2"  (9  = 5 days); four of the eight were
also studied in extended aeration pilot plants. See Table  3-9 for a list of those  priority
pollutants  tested.   Each test  compound was added to the feed  at  dosage levels  that
increased from 5 mg/liter to 20 or 25 mg/liter  to 50 mg/liter.  Following a  period of
operation at  a steady dosage level of  50 mg/liter, the unit was subjected to  daily cycling
or pulsing of  the concentration of test compound (e.g., 25 to 0 to 25 mg/liter).
         The following  conclusions with respect to the effects of the 24 priority pollu-
tants  on the  pilot  plant  performance were  drawn after a  two-year experimental period.
Results are  also summarized  in Table E-6 .  An evaluation of plant performance  was
based on a comparison of the residual soluble COD and effluent suspended  solids in the
test unit and the control unit.
                                        E-18

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                                  TABLE E-5

                       PRIORITY POLLUTANTS STUDIED
                  IN OSU'S BENCH-SCALE BIOLOGICAL SYSTEM
        Compounds Studied  (with  Percent Total COD)^

        Set 1:   Individual  Feed
                   1,1,2,2-Tetrachloroethane (TCE) 9%
                   Nitrobenzene  (NB) 33%
                   2,4-Dichlorophenol  (DCP) 21%

                Combined Feed
                   TCE 2%,  NB  14%,  DCP 75%

        Set 2:   Individual  Feed
                   Acrolein (Ac) 66%
                   Acrylonitrile (Aery) 66%
                   1,2-Dichloropropane (DCP) 2%

                Combined Feed
                   Ac 22%,  Aery  22%, DCP  1%

        Set 3:   Individual  Feed
                   Methylene Chloride  (MC) 5%
                   Benzene (BEN) 67%
                   Ethyl acetate (EA)  67%

                Combined Feed
                   MC 2%,  BEN  22%,  EA  32%

        Set 4:   Individual  Feed
                   1,2-Dichloroethane  (DCE) 13%
                   Phenol  (Ph) 85%
                   1,2-Dichlorobenzene (DCB) 33%
                Combined Feed
                   DEC 3%,  Ph 34%,  DCB  3%
     remaining COD was contributed  by  "base mix," a readily biodegradable
 synthetic wastewater.
SOURCE: Kincannon, I980aand ! 980b, and Kincannon and Stover, 1981 a and I98lb.
                                     E-19

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                                          TABLE E-6

                     SUMMARY OF EFFECTS OF PRIORITY POLLUTANTS
                           OSU BENCH-SCALE BIOLOGICAL SYSTEM
—
PARAMETER
BATCH UNIT
DOSAGE (rag/1)
CONTINUOUS riCM UNIT
(in » O.2 EXTENDED AERATION
DOSVZ fug/liter) DOSATE (mg/liter)
0 5 20/25 50 CYCLIC 0 5
20/25 50 CYCLIC 0 5 20/25 50 CYCLI
PENDCHLOPCPHEtCX.
1,2-OICHLCJCETHWa
NZTfOBEitEENE
TRICHLORCenniENE
JCIWLEKE CHLORIDE
PHENOL
2-CHLORQPHENOL
4^LOtO-3-MEIHtt
PHENOL
O • Performance saws
X • Performance poor
7 • Performance poor
BLank indicates par*
The following priorit
Anthracene
Benzene*
CODE 0 X X X X
nrm; OOOO OOOO
SSE 0 O X X
CODE OOOOOOOOOO
SSE O 0 0 0 X
ODE OOOOOOOOOX
SSE 0 O 0 0 X
gne OOOOOOOOOO
SSE 0 X X X X
SSE 0 X X X X
CODE OXXXOOOOOO
SSE 0 O O X X
CODE OOXX 000?
SSE OOOO
as control
compared with control
in both control and test system
inter not measured
y pollutants, tested in the batch unit, did not affect performance:
Hexacnlorobenzene
Hexactiloreetnane


O 0 0 O 0
00000
Oy v y y
A A A A
0 0 0 X X
0 O 0 O O
O O 0 O O
OOO?
OOOO







       Carbon Tetrachlorioe
       Chlordaenzene
       Chloroform
       Ethylbenzene
       Fluorene

•Also >••«••* in continuous flew unit
 Naphthalene
 2-Nitrcphenol
 Tetrachloroethane
 Tetrachloroethylene
 1,1,2-Trichlorcethane
 Toluene

un » 0.2 day  j
     SOURCE:  Gaudy et d., 1979
                                             E-20

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I.       Of the 24 compounds studied in batch systems, only two compounds (pentachloro-
        phenol and 2-chlorophenol) gave evidence of causing metabolic  stress to  the
        system,  as  judged by comparison of residual  soluble COD in the test  unit  and
        control unit at a daily feed concentration of 5 mg/l.  At higher concentrations
        (20 to 25 and  50 mg/l), there was evidence of metabolic disturbance for only  one
        additional compound, 4-chloro-3-methylphenol.
2.      For the eight compounds tested in the continuous-flow  activated sludge pilot
        plant operated at  w   = 0.2 days , there was no evidence of increased soluble
        COD in  the effluent at the 5 mg/l  dose. At this dose, however, there was an
        increase in suspended solids in the effluent of pilot plants dosed with phenol  and
        methylene chloride.  In addition, at higher dosage levels, there was  an increase in
        soluble COD  and suspended solids in the effluent for the pilot  plant dosed with
        phenol.  For the units dosed with 2-chlorophenol at the 50 mg/l  dose, methylene
        chloride at the 5 mg/l dose and dichloroethane at the 25 mg/l dose, soluble COD
        in the effluent was not affected but there was an increase in effluent suspended
        solids concentration. Under alternating concentration levels (daily changes from
        25 to 50 to 25 mg/l  followed by 0 to 25 to  0 mg/l)  there was increased soluble
        COD and  suspended solids in the effluent  for the unit dosed with trichloro-
        ethylene.   For  the  pilot plants  dosed with  nitrobenzene,   2-chloro-phenol,
        methylene  chloride  and  1,2-dichloroethane, cyclic  loading led  to increased
        suspended solids in the effluent.
3.      For the four  compounds tested  in the  extended aeration pilot  plant, increased
        soluble COD  in the effluent was reported only for the unit dosed with phenol at
        the 5 mg/l  dosage level.  There was no increase in  effluent suspended  solids in
        any of the four systems at this dosage  level.  At the higher dose levels (20  and
        50 mg/l) and  during the period of cyclic loading of the test compound, the units
        dosed with phenol showed increased soluble COD and  suspended solids.
                                        E-21

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FATE OF PRIORITY POLLUTANTS

Introduction

        In  developing predictive models for biological  treatment  of  specific  organic

compounds  found  in  industrial  effluents, an  important distinction  needs to be made

between treatability and removability of the specific compounds.  Removability describes

the change in concentration of the compound between entering and leaving the treatment

process.  Treatability is a more specific term, relating to the treatment mechanism by

which compounds can be evaluated (biodegradation, air stripping of  volatile compounds,

adsorption on sludge, etc.) and compared to other compounds (Kincannon e£a[., 1981).

        To date, most design models have originated from a  simplified mass balance for

the substrate, represented as:



        CHANGE OF        MASS               MASS LEAVING      MASS
        MASS IN        =    ENTERING    -      REACTORIN     -   CONSUMED
        REACTOR           REACTOR           EFFLUENT          BIOLOGICALLY


As adsorption and stripping  are not included in  this mass  balance equation, treatability

data derived on this basis may:

        I.    Incorrectly determine biokinetic constants (and  thus inaccurately pjredict

             substrate treatability by giving biological processes credit for removal).

        2.    Leave unrecognized air and solid waste pollution problems, resulting from

             stripping and adsorption of the various

             organic compounds.

A more correct substrate mass balance would thus be (Kincannon and Stover, 1981):
CHANGE       MASS          MASS          MASS           MASS          MASS
OF MASS   =   ENTERING -   LEAVING   -   STRIPPED  -    ADSORBED -   CONSUMEC
INRE-         REACTOR     REACTOR                      ON            BIOLOGIC^
ACTOR        IN EFFLUENT                                 SLUDGE
                                     E-22

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This approach, that is  considering the multiple pathways by which  pollutants can  be

removed during biological treatment, is used in the following section.

Multimedia Models Of Biological Treotability

        Hwang Model

        Hwang (1980a) has  developed a  model  describing the dynamics of substrate

removal in a continuous activated sludge process  with sludge recycle, incorporating the

mechanisms of biodegradation, air stripping, and adsorption on sludge.  The components of

Hwang's model are described briefly below.

        Several models describing the kinetics of biological degradation were evaluated

in the development of the Hwang Model, including those using first  order kinetics for the

substrate reaction (e.g., Eckenfelder and McKinney), those which apply Monod kinetics in

their material balance formulations  (e.g.,  Lawrence and  McCarty, and Gaudy), and the

Grau model (which treats the substrate  removal rate as a  function  of  the  remaining

substrate concentration as compared to the original concentration).   Experimental data

from several  sources  served as  the basis  for judging  the  suitability of each  of the

treatability  models to  predict  removal of  the specific toxic compounds from  waste

streams. The Grau method best described  the data and, as a result, is used in the Hwang

multimedia  model to describe the biodegradation of  priority pollutants; this model is

represented  by:

                             - dS              [S ]n
                                dt  " *n(s)



where:

        S = substrate concentration,  g/liter

        t = time, days
 Data  were  obtained  from  the following sources: EPA, Cincinnati,   Union Carbide
Corporation, Catalytic, Inc., and the literature.
                                       E-23

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         'n(s)
= rate constant in the Grau equation, I/day when n=l
         S  = initial substrate concentration,  yg/liter.
         To describe air stripping kinetics in the Hwang model, experimental data on air



stripping rate constants are used where available.  The expression  for  air stripping  of



volatile components is represented as:
                                              k s
                                       at     a
where:
         k  = air stripping rate constant, I/day
         S = substrate concentration in the liquid,  ug/liter.



Where experimental data on air stripping rate constants are not available, rates can be



determined by combining the individual liquid and gas phase mass-transfer constants as



follows:
where:



         k  = air stripping rate constant, I/day



         k i  = individual liquid mass-transfer constant




          aG = individual gas mass-transfer constant



         K  = equilibrium distribution coefficient.






         Adsorption on activated sludge provides an additional route of removal for some



organic pollutants, cyanides, and  metals.   Adsorbed toxic compounds are removed from



the biological system when  the activated sludge is wasted. In Hwang's model, removal of



a specific toxic pollutant in sludge is represented by the multicomponent Langmuir type
                                         E-24

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adsorption  equation,  which  is  based  on the  concept of  binary characterization of

wastewater adsorption:
                                          K,  X1  S
                          IB'SJ  =   . ^  /  e ^  t
where:

         y*B*S¥z = concentration of a substrate in sludge, Ug/Iiter

         S = substrate concentration in the liquid, P g/liter

         S = concentration of total substrates minus substrate

              S under consideration, u g/liter

         K., K-j- = adsorption constants

         X' = the maximum amount of the substrate adsorbed on

              sludge, yg/liter.


         Hwang's  unified  model  (see Figure E-3) for removal  of toxic chemicals by

multimedia pathways incorporates the above three mechanisms.  The model  is described

below  in  terms of the  schematic of the activated sludge  process and by the equations

which follow.
                                       E-25

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                              FIGURE E-3
             A SCHEMATIC OF THE ACTIVATED SLUDGE PROCESS
         Q_  littrt/d«y
Q. - Qw liters/day
ii s£«

>
r
Biological
Treatment
V

A.

J S. //g/liter
Q liters/day
L 	 Z 	 ^
SOURCE:  Hwang, I960.
                                  F.-26

-------
S  = substrate concentration in influent,  y g/liter
 o
S  = substrate concentration in effluent,  y g/liter
X  , X  , X0 = concentration of substrate  on sludge in influent,
 o  e  r\
              effluent, and return sludge, respectively, y g/liter
V = bioreactor volume, liter
r = recycle ratio, volume flow rate recycle/volume flow rate
         feed
Q  r flow rate to biological treatment (=(kr)Qp), liter/day
Qp. = flow rate of the fresh feed
Q.II = flow  rate of the waste sludge.

        QFSO -  UP  ' Qw>se  «  *1(s)*  Se   v  *  ka  s   v
                                           so           a   e
                                         Q   Kl  X>  Se
                                              1  * Vr  * Klse
or
                    _   e
                     Q  se   «         e
                                       So
                                                 Se
                                                      *  K1Se    Q
where:
         tc = hydraulic residence time, day
         X s sludge concentration in the reactor, y g/liter
         X' = maximum concentration of a substrate on sludge,  yg/Iiter
         k./ v = rate constant in the Grau equation, I/day when n=l
         kQ = air stripping rate constant, I/day
         Ki and Kj = adsorption constants
         S  =  concentration of total substrates minus substrate S under consideration,
         y g/liter.
                                        E-27

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        Using the relationship Qp =  i	, one gets
    SQ -  (1 - W(l+r))Se   ,  _1	^e_  (i+r)tc +  ka Se(l+r)tc
                                         o
                                         kl X'  Se
                                           t  KTSr  * KlSe
where W=Qw/Qp (waste sludge flow/fresh feed flow).


        Since Hwang found the W(Ur) term to be small, the equation may be reduced to:
           {so "  Se}   »   1(s)s	£(Hr)tc + ka(l+r)Se  tc
                                  o

                                               u  y'  e
                                               Kl x   se
                                               i + KTsr *  Klse
        Monsanto Model
        In addition to the Hwang model, a number of other models have been developed


to describe the removal of organic compounds  by multiple pathways  during biological


treatment. Monsanto Company has described an approach for use in predicting the rate of


air stripping and biological degradation (Freeman, 1979).  Mathematical predictions based


on the Monsanto model  for the  treatability of the priority pollutant ccrylonitrile  were


verified using an experimental activated sludge system (Freeman et a[., 1980).


        In the Monsanto model, the biological oxidation component is represented by the


model of Gerber.   This model involves  the solution of  the following three simultaneous


non-linear  equations  in  three   unknowns; solution  by  use  of a digital computer is


recommended by the authors.  Use of the Gerber model  to describe biological treatability
                                      E-28

-------
differs from  the  one constant  Grau model used by Hwang; further,  the  Gerber mode!

accounts for the impact of substrate, oxygen, and biota concentrations.


                    r      -                k5Boco°o
                                 °o  * K02Ks  + Co°o + K02Co
                                   Mw
                             tr

where:

        TQ   s Rate of oxygen use, Ib/hr-ft  ,
          2                                       3
        TQ  s  Rate of microorganism growth, Ib/hr-ft ,

        r *  =  Rate of organic disappearance, Ib/hr-ft ,

        B  =  Concentration of microorganisms from the basin, Ib/ft ,

        CQ   = Concentration of organics from the basin, Ib/ft  >

        0   = Oxygen concentration in the basin liquid, Ib/ft ,

 k. and kc  = Reaction rate constants,

KQ  and K  =  Constants,

        t  =  Oxygen use factor, Ib mole C^H

               mole oxygen  used,

        S   s Substrate use factor, Ib mole Ce

               mole substrate  consumed, and
                                                produced/lb




                                                   produced/lb
                                       E-29

-------
      j MWg, = molecular weights of the organic compound, micro



 and (V\WQ     organisms, and oxygen, respectively, Ib/lb mole.
        The rate of air stripping in the model is represented by the following equation, in



which the rate of stripping to the atmosphere varies with the organic concentration in the



liquid phase.
    N   s    "...  NK   (X   •> X  *1  +  fA  —
    Na       4   N*a  lxa    xa '  *  
-------
         The treatability of acrylonitrile was studied to verify the  predictability of this



model.  The model indicated that if sufficient aeration  capacity is maintained (2 ppm or



above),  99 percent of the feed acrylonitrile  will be biodegraded and less than I percent



will be  air stripped  (Freeman, 1979).  These  results were confirmed in series of bench-



scale  continuous flow activated sludge treatment systems, in which biological  treatability



efficiencies of greater than 99.9 percent were  found (Freeman et  aU, 1980).  When the



treatment system was run under  sterile conditions (i.e., no seed microorganisms  were



present), it was found that 18 percent of the acrylonitrile was air stripped.



Data  Development for Multimedia Models



         Indicatory Fate Study



         The data base for predicting the fate of individual  compounds by multiple routes



is presently limited.  One of the first attempts to determine the fate of specific priority



pollutants as they pass through a biological system was conducted in the EPA-sponsored



Indicatory Fate Study (EPA, I979a).  Three plants belonging to the organics and plastics



industries participated in  a screening study  to  provide an  indication of  the  removal of



specific priority pollutants via  air, water,  or residuals  routes.  The types  of treatment



processes used to treat the industrial effluents are shown in Appendix G.  Analyses  were



conducted for priority pollutants  which had  been identified in previous  screening and



verification sampling under the  direction of  EPA's Effluent  Guidelines  Division, Organic



Chemical Branch.  Analyses were performed on composite samples (influent, effluent, air,



and residuals) and on grab samples (influent and effluent}. The data generated from these



analyses provide only an indication of the route of removal of specific priority pollutants,



and were  not intended  to represent a mass balance across a biological treatment system.



Analysis  for organic compounds in the three  plants  sampled revealed no  discernible



patterns concerning  the fate of specific organic compounds or classes of compounds in the



effluent, sludge/sediment, or air.  Heavy metals occurred at  the highest  concentrations in
                                         E-31

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all three plants  in the activated return sludge or the sediment of aerated lagoons.   The



heavy metals" included arsenic, copper, chromium, nickel, zinc, and lead  in return sludge,



and additionally selenium, cadmium, beryllium, antimony, silver, and  thallium in lagoon



sediments.



         EPA-Sponsored Bench-Scale Studies



         Kincannon e£  a[. (1981) and  Kincannon and  Stover  (I98lc), in  work supported in



part by the EPA, have evaluated the  removal of priority pollutants by biodegradation and



stripping.   Experimental  results were obtained  using  a bench  scale-continuous  flow



activated sludge reactor used to treat a synthetic  wastewater containing selected priority



pollutants. The reactor was operated as a nonbiological system to determine the strippa-



bility of the chemical compound, and  as a biological activated sludge system to determine



biodegradation  and stripping,  and adsorption for a limited number of compounds. These



results are summarized in Table  E-7.



         Total percent  removal of the specific compounds varied from  93 to 99.9 percent.



Stripping   during  biological   treatment   accounted   for   essentially  all  of   the



tetrachloroethane,  1,2-dichloropropane,  and 1,2-dichloroethane removed.  These studies



show that volatile  organic compounds  can be  removed by  concurrent  stripping  and



biological oxidation.  Further, the results indicate that the failure to recognize stripping



as a removal mechanism  will  affect  the  experimentally derived biokinetic constants for



pollutants.



         It is  interesting to note that the stripping that takes place in a nonbiological



system does not necessarily predict the degree of stripping in a biological system. While



approximately  100 percent  of  1,2-dichloropropane,  methylene chloride,  benzene,  and



1,2-dichlorobenzene  are stripped in  nonbiological systems,  only  1,2-dichloropropcne is



highly stripped during treatment with the biological systems.
                                        E-32

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                            TABLE E-7
                   FATE OF SPECIFIC POLLUTANTS


Compound
Tetrachloro-
ethane
Nitrobenzene
2,4-Dichloro-
phenol
Acrolein
Acrylonitrile
1,2-Dichloro-
propane
Methylene
Chloride
Ethyl Acetate
Benzene
1,2-Dichloro-
ethane
Phenol
1,2-Dichloro-
benzene

Total
Percent
Removed
93
97
94
99.9
99.9
99.9
99.5
99.8
99.9
98.5
99.9
99.9
Biological

Percent
Stripped
93
0
0
0
0
99
5
17
15
97.5
0
24
System* Nonbiological
SvstemD

Percent Percent Percent
Adsorbed Degraded Stripped
0
97.0
94.0
99.9
99.9
0 98.8
94.5 99.4
82.8 81.9
84.9 99.3
1 0 96.1
0 99.9 1.9
0 75.9 84.7
SOURCE:  Kinconnon and Stover, 1981 c.
SOURCE:  Kincannonetd., 1981.
                               E-33

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         A limited evaluation  of  the fate of  priority pollutants in batch and continous



flow bench-scale activated sludge pilot plants was performed by Gaudy et aJ. (1979) in



their study of the effects of 24 priority pollutants on  the activated sludge process.  S»See



Biological Treatability Studies—Toxicity of Priority Pollutants for a discussion of  the test



methods used.fe The results of these analyses  appear in Appendix H.  Although the data



are  limited,  most  compounds   were  removed   effectively  (with  the  exception  of



nitrobenzene, 2-chlorophenol and  3-methylphenol  under  certain experimental conditions).



Anthracene  and  fluorene  concentrations were  high  in  the  mixed  liquor  while



concentrations were low in the settled effluent.  This indicates that the compounds were



present as part of the  biological solids, possibly adsorbed to the surface.  Although these



analyses do  not provide specific information on the removal  routes of  the  priority



pollutants, the results indicate there was  no  evidence for massive pass-through in the



effluents  of  any of  the compounds.   Small quantities  of some of the compounds  were



detected in the effluents, however;  more detailed analytical procedures are needed to



adequately address the question of pass-through  of small concentrations of the  priority



pollutants.



         Fate of Priority Pollutants in Publicly Owned Treatment Works



         The fate of priority pollutants in publicly owned  treatment works  (POTW) was



presented in  an interim report, in  which the preliminary results from 20 of the 40 POTW's



selected by  the EPA's Effluent Guideline Division were reported  (Feiler,  I960).  The



treatment processes included among the 20 plants were conventional activated sludge and



modifications of activated sludge such as contact stabilization, Kraus, and pure oxygen, as



well as some advanced waste treatment processes, notably mixed media filters.  Samples



of  influent,   effluent, and  sludge  streams   were  analyzed for  conventional,  non-



conventional, and priority pollutants.  Based on their analyses of 93 priority pollutants,
                                        E-34

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the  following  preliminary  findings  relating  to  the  fate  of  priority  pollutants  were



reported:



I.        For five of the treatment plants  (four activated sludge and one trickling filter)



         where the mass balances were assumed to be  relatively accurate it was observed



         that metallic priority pollutant mass balance  was good, but some organic priority



         pollutants in the  influent were  always  not  accounted for in  the effluent or



         sludges.  This indicates that,  in general, a portion  of organic priority pollutants



         are biodegraded or, in the case of  volatiles, stripped out of the wastewater.



2.       Based on the 20 POTW data base, half of secondary treatment plants achieved at



         least  76 percent  reduction  of   total  priority  pollutant  metals,  85 percent



         reduction  of  total volatile priority pollutants, and  70 percent reduction of total



         acid-base-neutral  priority pollutants.   Tertiary treatment was slightly  more



         effective  than secondary treatment in reducing priority pollutants, and primary



         treatment the least effective.



3.       For  many conventional  and  priority  pollutants,  as  influent concentrations



         increased, effluent concentrations also increased.  This trend held for  all metals



         (except for mercury) with correlation coefficients  ranging  from 0.204 to 0.995,



         and, in general, for volatile priority pollutants, correlation coefficients ranging



         from 0.262 to 0.937.



4.       Some pollutants  not  measured in POTW influents were regularly measured at



         high levels in the corresponding sludge streams. This phenomenon  was observed



         for 25  priority  pollutants, including metals  and organic compounds.   This



         observation was most likely due  to concentration of the pollutant  in the sludge



         stream to detectable levels.



5.       Eleven  priority pollutant chlorinated hydrocarbons increased in concentration



         during chlorine disinfection.
                                         E-35

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Conclusions
         The  complexities  of  the  removal  of organic  pollutants  during  biological
treatment are receiving greater attention, both  in terms of modeling and the design of
experimental protocols to determine treatability  constants for pollutants during biological
treatment.  The multimedia models reflect the recognition  that biological treatment not
only involves oxidation of organic compounds, but removal through air stripping and waste
sludge as well.  Failure to incorporate these additional routes of pollutant removal  can
result in inaccurate determination of biokinetic constants  and failure to predict possible
air  and solid waste pollution problems.  Thus, a model of  the activated sludge  process
which incorporates a single biokinetic constant is not an accurate mechanistic model of
the complete treatment  process.  Further  experimental  work is required  in order to
determine accurate kinetic constants for each of the competing treatability mechanisms
that occur during biological treatment.
                                        E-36

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 ACTIVATED CARBON ADSORPTION



Introduction



         Adsorption  processes can  be  used to  remove  contaminants  from  aqueous



wastewaters  by  the  preferential  adsorption  (either  physical  or  chemical) of  the



contaminants  on solid  surfaces.   Pollution parameters affected  by activated carbon



include BOD, COD, TOC, specific organic priority pollutants, and to a lesser degree four



specific non-organics: cadmium, chromium, cyanide, and mercury.



         There are approximately 100  large scale industrial or municipal wastewater



activated carbon treatment systems in domestic  use  (Hydroscience, 1981).  Large scale



industrial activated carbon treatment systems require extensive pilot plant study before



scaling up to optimize the system and assure compatibility between the system and the



characteristics of the waste stream.  This is due, in part, to the competition among



individual components in a  multicomponent stream  for  active adsorption sites.   For



example,  the  adsorptive capacity of  a particular system  with respect to  a specific



compound  may  be  lessened if  another  compound  is added  to  the waste stream.



Additionally, system  designers must  consider the best economic  configuration of the



adsorption process itself and, if used in  conjunction with other treatment modules (e.g.,



biological treatment), the optimal configuration of the entire treatment scheme.  This is



especially true for multicomponent wastestreams where target pollution parameters are



of the utmost concern. Recent EPA research efforts have been directed toward modeling



systems  to assess the applicability of activated  carbon treatment systems to differing



waste stream types and to provide preliminary design data for scaling up.



Background



         Activated carbon  adsorption  treatment  systems  may be implemented on a



commercial  scale in several differing design modes using either granulated or powdered



carbon.  The most common type of system in use will be discussed here.  That system uses
                                       E-37

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granulated carbon  in  a fixed bed.   The design  criteria of a  system  are numerous:



consideration must  be given to the presence of suspended solids in the wastestream, the



potential for biological growth  in the adsorper, carbon regeneration costs,  and cycling



time.  The  most critical design parameter is the  adsorptive capacity of the bed which



dictates the performance of the system.



         The effectiveness of  granular carbon in removing a given pollutant from solution



is  typically evaluated  in  terms of  its adsorption capacity  at  constant temperature.



Adsorption capacity measures the amount of solute adsorbed per unit weight of adsorbent



as a function of solute (pollutant) concentration in bulk solution.



         The actual selection  of  the adsorber configuration is  dependent on the required



carbon dosage and contact time  (flow rate/adsorber volume), which requires bench and/or



pilot scale testing to determine  the rate of adsorption. By dynamic column testing over a



range of contact times, the concentration of solute (contaminant) remaining in solution



(C/C  ) can be plotted versus volume of solution (wastewater) through the column to give



the breakthrough curve.  Depending on the complexity of the wastewater, the shape of the



breakthrough curve may vary but,  it is characteristically "S-shaped."  The breakpoint



represents the point on the curve at which the column is in equilibrium with  the influent



wastewater,  and little additional removal of the contaminant(s) will occur.  Generally,



time to breakpoint  may be extended by increasing the  carbon bed depth and  lowering the



flow rate; however, several other factors, such as the characteristics and concentration of



the solute, the pH of the solution, and the characteristics of the carbon selected influence



the overall  capacity of the adsorption system (i.e., height and rate of movement of the



mass  transfer zone, capacity of  adsorbent, etc.). The  objective, in any application, is to



design a system  in which the most economical, yet practicable, carbon exhaustion  rates



(the time necessary to reach the breakpoint) can be achieved.
                                        E-38

-------
         Another major consideration in the design and operation of a carbon adsorption



system  is  the  means of replacing exhausted  carbon.   This may be  accomplished  by



removing the carbon from the adsorber for permanent disposal (i.e., throwaway carbon),



or more typically, for reactivation.  Reactivation is  any means by which the carbon is



restored to its original adsorptive capacity.  Organic  impurities may be removed  by



thermal, alkaline, acid, hot gas (steam), solvent, or biological regeneration. However, in



treating wastewaters containing  a  mixture  of organics, thermal regeneration of  the



carbon  in either multihearth  or  rotary  tube  furnaces provides  the  most  reliable



reactivation process and, thus, is  the most widely  applied. Thermal regeneration may be



carried out on-site  or off-site depending on the scale of operations.   As a result  of



handling and reactivation, attrition losses, requiring fresh make-up carbon, will typically



range from 5 to 15 percent by weight.



         Under certain conditions  (e.g., the presence of  biodegradable organics, favorable



pH ranges,  etc.) biological activity may occur  in the carbon adsorption column.   In



general, anaerobic growth not only results in HUS  production, but reduces the adsorption



capacity of the column and therefore should be discouraged. Aerobic bacterial activity,



depending  on  the concentration  and composition  of  the waste loading, may enhance



treatment efficiency.  In certain  cases, biological  degradation of organic contaminants



complements the adsorption process, increasing adsorption capacity and providing partial



regeneration of the carbon.



State of the Art



         As indicated above,  the  most  critical design parameter  for carbon  adsorption



treatment systems is the adsorption  capacity of the carbon which determines the cycle



time of the adsorption bed.  The length of the adsorption cycle can be determined by two



lab techniques and pilot scale  tests.  The lab scale tests are the use of isotherms  and the



Dynamic Mini-column Adsorption Technique (DMCAT).
                                         E-39

-------
         Isotherms  are usually  determined  under static  conditions  which assume the



resistance to mass transfer to be neglible.  EPA (1980) has adopted an alternate approach,



DMCAT, that considers non-equilibrium effects  to take into account the nature of the



driving  forces  which control  the  transport  phenomena  of  solutes  from  solution.



Breakthrough  curves  for  complex  waste streams with nonlinear isotherms are  usually



empirically  determined.    Recent efforts   have  focused  on  modeling  efforts  for



multicomponent wastestreams using psuedo-contaminant parameters which represent an



empirical theoretical approach to the problem of optimizing dynamic adsorbent systems.



         Data gathered through isotherm and DMCAT testing can be extended in some




cases through the use of mathematic models  which simulate the kinetics of adsorption  in



full scale systems.  The  lumped parameter  model combines the diffusional  resistances



described by a pore diffusion model and homogeneous solid diffusion model into a single



parameter.  This model has been developed based on data  from full scale operations and



pilot plant  data on several priority pollutants (EPA, 1980).  Adsorption occurs through a



four-step process:



         I.     Transport of a solute from bulk liquid to solid interface



         2.    Transport across the interface



         3.    Transport from  the interface into the solids



         4.    Adsorption  on the active sites.



Each one of these steps represents a resistance to mass transfer from the bulk liquid to



the active sites.  Equilibrium models assume  the resistance to mass transfer due to steps



I,  2 and 3  to  be neglible and  that the  bulk concentrations of the  two phases are  in



equilibrium which is unrealistic (i.e., equilibrium is not attained in practical systems).



         The lumped parameter model is developed by c fundamental material balance for



each step in the adsorption process.  The mass transfer equations that result from such an



analysis  are solved numerically and combined into a single mass transfer coefficient.  A
                                       E-40

-------
brief treatment of this concept is presented below, the reader is referred to Appendices I
and J and to EPA (I979b) for a detailed discussion of the lumped parameter model.
         In  order to utilize  the  principles of  any  model  it is  necessary  to obtain
experimental data to estimate mass transfer parameters.  This requires dynamic column
testing to generate breakthrough curves which, when done in a pilot plant scale column, is
a timely and  costly procedure.  This is  particularly  true of requisite  data  on specific
organic compounds.  The Dynamic Mini-column Adsorption Technique (DMCAT) is capable
of rapidly generating necessary design data to nominally assess  the performance of an
adsorption system for single and multi-component wastestreams.
         This  technique,  described  by Beaudet et pj. (1980), utilizes  a high  pressure
precision metering pump to pass wastewaters through a very small  column at pressures up
to 6,000 PSI.  Meticulous care must be  taken  to avoid contamination of the absorbent
during  assembly  of the   apparatus  to  assure  accurate  and   reproducible  results.
Additionally, influent and effluent samples must also be protected from contamination by
ambient airborne organics.
         Beaudet e£ a[. (1980) conducted several tests  with the DMCAT on several single
and multi-components,  and  "real world" wastestreams and  them  compared their results
with those from  pilot scale tests.  Their  results were  congruent with pilot  scale results.
The utility of DMCAT is to rapidly obtain  reproducible  data that can be used to determine
the amenability  of a particular wastestream to  carbon adsorption  and carbon usage rates
to estimate  system economics.
Applications of Activated Carbon Adsorption
         In  one  laboratory  study  (Walk, Haydel,  I980a),  two commercially  available
adsorbents  were  tested on an unspecified industrial wastestream  in a  laboratory study.
The  wastestream was  from  a multi-product  effluent  that  contained  five  priority
pollutants; chlorobenzene (8.8 ppm), p-dichlorobenzene (360 ppm), nitrobenzene (166 ppm),
                                       E-41

-------
dinitrotoluene (7.9 ppm),  and phenol (30.8 ppm).   Carbon adsorption  was  found to be



effective, exhibiting effluent concentrations of O.I ppm or less for each of the  priority



pollutants.  These results are based on equilibrium and dynamic testing.  Walk,  Haydel,



(I980b) also  compiled data on commercially operating systems in a  limited survey. These



data are presented in Table  E-8. Hydroscience (1981) conducted a more extensive survey



of facilities using carbon absorption, to treat process wastewaters.   Approximately 50



plants  primarily engaged in  organic  chemicals or pesticide manufacture were queried.



Other  facilities  included in  the  survey were  those  expected  to  generate  process



wastewaters that may be amenable to  carbon  adsorption  treatment, such  as  refineries,



coke plants, and detergent manufacturers. The design characteristics of these full scale



adsorption systems are presented in Table E-9  and the performance of these systems  in



removing priority pollutants  is summarized in Table E-10.



         The utility of these data are somewhat limited because survey respondents often



provided incomplete data.   For example, most  facilities  reported  influent streams  in



terms of BOD, COD, and only  one  or two  priority pollutants.  In some survey responses,



only influent or only effluent concentrations of pollutants were reported.   However, as



noted elsewhere, a  particular plant in  the organic chemicals  industry  will only have a



small number of priority pollutants  in its wastestream  in addition to conventional  organic



pollutants. Because the specific wastestream components were not sufficiently  identified



in this  survey, the impact of specific priority pollutants on systems removal performance



can only be  inferred.  In  particular, data are inadequate to assess the competition among



individual pollutants for  active adsorption sites in a multicomponent stream.  Of the



systems surveyed by Hydroscience (1981), many  were effective in the removal of specific



priority pollutants.
                                        E-42

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                            TABLE E-9
      DESIGN CHARACTERISTICS AND OPERATIONAL PARAMETERS FOR
    FULL-SCALE GRANULAR ACTIVATED-CARBON ADSORPTION SYSTEMS

01
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t
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SOURCE: Hydroscience, 1981.
                               E-44

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                              E-51

-------
Although carbon  adsorption  systems require extensive lab and  scale  up testing en  a



particular wastestream the results of ^he survey suggest that such systems ere a vicoie



and acceptable technology for use m priority pollutant removal  from  multi-componenf



wastestrecms generated by full scale plants.



         A  daily  sampling  effort  was  conducted  by EPA  at  an  organic chemicals



manufacturing plant (5?A, l?3lc).  Effluent concentrations  from a carbon  adsorption unit




used to treat process waste-waters are presented in Table E-ll*These results are from one



laboratory only and  exhibit some pronounced variability among parameters.  Parameters



were selected on  the basis of the process chemistry and are expected to be present !n  the




effluent.  During the  study,  two other labs also 'conducted sample analysis  which also



exhibited a  degree of  variability.  Whether  these differences are attributable to system



pertubations or ancl/tical  deviations is not known because  a statistical  analysis of these



data is not  yet available.  EPA is currently conducting such en  analysis  which will better



define this particular system's performance.
                                        E-52

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E-53

-------
STEAM  STRIPPING



Introduction



         Steam stripping  is a  mass transfer operation that is used  to  remove  volatile



organic contaminants from dilute  solutions.  It is essentially a distillation  that uses live



steam  as its energy source and is  typically used  for liquids that ere immiscible in water.



Steam  stripping  may  be employed for  binary  distillations,  and is also  amenable  to



multicomponent streams.  Design  equations and criteria are well established and  in some



cases there is  little need for extensive pilot plant studies prior to installing a large scale



unit.



Background



         Steam stripping  is accomplished by injecting live steam into  a  vertical mass



transfer column.  Steam distillation, a batch process, is commonly used  to  distil!  organic



liquids, which  might decompose if heated to temperatures high enough to cause them  to



boil in  the absence of steam. Stripping columns may be packed, sieve tray, or bubble cap



tray.   Packed columns are  preferred  because they maximize the  interfacial  surfaces



available  for   mess  transfer;  however,  they  may  not  be  the  rncst economical.



Consideration  must also be given to  the compatibility of the mixture to be separated with



the materials used to construct the column in order to assess the expected lifetime of the



packing. Additionally,  throughput rate, energy requirements, maintenance, end operating



costs may dictate a column design  of either the sieve tray or valve tray type. Subble cap



tray columns  ere seldom used  today  because they have  been replaced by valve  trays.



Either  choice is about twice as expensive (capital cost) as sieve tray columns.



         Regardless  of the  column  design the  principle  cf  separation of  mixture



components is the same.  Once the  column is in  a steady  state condition, a temperature



gradien; and a congruent series of gas-liquid equilibrium stages are established. Standard



design  equations  that  relate the  vcpor pressure,  activity coefficients,  and equilibrium
                                         E-54

-------
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-------
                            TABLE E-13

STEAM STRIPPING OF ORGANIC PRIORITY POLLUTANTS WITH AQUEOUS REFLUX
                   (inlet concentration = solubility limit)
                            STEAM STRIPPER          NO  OF  TH~OR£TICAT
POLLUTANT               OUTLET CONCENTRATION         '               "
                             10 6 g/L(ppb)
Acrolein
Acrylonitrile
Benzene
Carbon Tetrachlor ide
(tetrachlor one thane)
Chlorobenzene
1,2, 4-Tr i.chlor obenzene
Hex a chlorobenzene
1, 2- Di chloroe thane
1,1,1-lri chloroe thane
Kexachloroe thane
1,1- Di chloroe thane
1, 1, 2 -ir i chloroe thane
1, 1,2, 2- Tetr a chloroe thane
Chloroe thane
Bis (chlorome rjyl) ether
2- Chloroe thy i vinyl
ether (mixei).
Chloroform
(trichloror thane)
1, 2-Dichior-. ,/nzene
l,3-Dichlcrcr.-,-r.zene
1,4-DichiorcLer.zene
1, 2- Tr an s-di chloroe thy lene
1,2-Dichloropropane
1,3-Dichloropropylene
(1,3-Dichloropropene)
2,4-Dinitrotoluene*
2, 6-Dinitrotoluene
Ethylbenzene
Bis (2-chloroisopropyl) ether
Kethylene chloride"
(dichlorome thane)
Methyl chloride (chlorome thane)
50
50
50

50
50
50
50
50
50
50
50
50
50
50


50

50
50
50
50
50
50

50
50
50
50
50

50
50
19
13
5

4
5
4
3
6
6
3
6
5
5
7


6

6
4
3
4

5

5
10
» V
10
3
9

g
6
                              E-57

-------
                       TABLE E-13  (Continued)
                            STEAK STRIPPER
POLLUTANT               OUTLET CONCENTRATION
                             10 * 9/L(ppb)
Methyl bromide (bromoine thane)
Sronoforni (tribromomethane
Dichiorobromome thane
Trichlorofluorome thane
D i ch lor odifluorome thane
Chlorodibroror.e thane
Eexachlorobutsdiene
Kexachlorocyclopentafiiene
Nitrobenzene
Tetrachloroethylene
Toluene
Trichloroethyler.e
Vinyl chloride (chloroethylene)
SO
50
50
50
50
50
50
50
50
50
50
50
50
3
6
€
3
1
6
1
2
19
4


4
                               E-58

-------





















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                                                             E-60

-------
constants to the material balance in the staged column  (with  and without reflux)  are



presented in Appendix K.



         Volatile  organic  components  having  a  partial  pressure  at  a  particular



temperature evaporate or distill  and are removed at  the top of the  column while  the



"stripped" liquid phase water is discharged from the bottom.  The presence of steam in the



vapor phase reduces the partial pressure of the other components at  a fixed  total  pressure



and thus lowers the saturation temperature of the  liquid to be distilled.  The column tops



may be  incinerated,  partially condensed, or  totally condensed.   The water from  the



column tops may be refluxed to  the column depending  on the economic utility  of




refluxing. Refluxing offers the advantage of recovering organics as  a liquid and increases



the degree  of  separation of  the  column.  It  also increases the steam requirements  to



satisfy  the  overall  heat  balance  for  the  column.    Again, as  with  the   column



design, selection of refluxing options are based upon economic considerations.



State-of-the-Art



         Standard design  equations that relate the vapor  pressure,  activity coefficients,



and equilibrium constants to the material balance in the staged column (with and without



reflux) can  be  used  to predict the column performance.  Hwang and Fahrenthold (1980)



have  compiled  thermodynamic data pertaining to 99  (of  the 129) priority pollutants



potentially amenable to steam stripping.  These data were extracted from  the literature



or calculated from solubility and other data.  Data on compounds normally subject  to



steam stripping have been summarized and are presented  in Table E-12  Tables  E-13ond



E-14  present calculated column  efficiencies,  tray and  steam  requirements, and  outlet



concentrations  of the priority pollutants  based upon data from  five commercial  steam



stripping columns, several pilot plant studies, and  laboratory data.  These are calculated



data assuming the inlet concentration to the stripper is the solubility limit of the specific



pollutant.   Additionally,  the calculations assume ideal behavior for mixtures  (i.e., no
                                        E-61

-------
intermolecular interactions among components).   Pollutants that require more than 20
trays to effect an outlet concentration of 50 ppb or less were excluded because they may
not be economically justifiable for wastewater treatment.
         In a  recent  controlled and comparatjve bench scale study, the validity of the
estimated thermodynamic  data  presented in Table E-12was examined (EPA, I98lb).   A
water solution saturated with three nonpriority pollutants was steam stripped and the
effluent concentrations were measured. These results were compared to predicted results
that are calculated by assuming  five theoretical  plates.   The measured and calculated
results   compared  favorably  (see  Table E-15}  although  the  measured   effluent
concentrations are slightly lower suggesting that the assumption of five theoretical plates
was  incorrect  (i.e., the column has more  than five plates).  The calculated  effluent
concentrations were based on K values of these nonpriority pollutants that were derived
from published vapor-liquid equilibrium data.  As noted earlier, the average K  values for
priority pollutants presented in Table E-12are more or less based on solubility data rather
than vapor-liquid  equilibrium data.  The experiment was  repeated with the  calibrated
column  using  six priority pollutants (benzene,  chlorobenzene,  1,1,2,2-tetrachlorobenzene,
chloroform, ethylbenzene, and tetrachloroethylene).
         Saturated aqueous  solutions  of the six priority  pollutants were  also  stripped
individually and in combination with each other. The calculated effluent  concentrations,
assuming  one theoretical  plate, were  much lower (in some cases up to four orders of
magnitude)  than  the measured  values (see  Table E-16).  The calculated  values  in
Table E.I6 for priority pollutants were based on the estimated average K values presented
in Table E-12. The assumption of one  theoretical  plate reduces  the system to a simple
single  stage  vapor-liquid  equilibrium.   These   data  suggest   that, although column
efficiencies for the priority pollutant may be less than those of the nonpriority pollutants
examined in  this study,  the accuracy  of the estimated K values  presented in Table E-12
                                        E-62

-------
                          TABLE E-15


      CALCULATED RESULTS FOR STEAM STRIPPING OF SOLUBLE
NONPRIORITY POLLUTANTS ASSUMING A 5 THEORETICAL TRAY COLUMN
                                               Calculated
                  Hole Fraction  Hole Fraction  Hole  Fraction
     Component	Feed X 1CT    Bottoms X 1(T  Bottoms X 1CT

     Acetone          2,470           .329           SI. 2

     2-Propanol       2,110           .122           12.9

     Methanol	4,610	1,520	2.489
                              E-63

-------
TABLE E-16
CALCULATED RESULTS FOR STEAM STRIPPING OF
POLLUTANTS ASSUMING A 1 THEORETICAL TRAY
Mole Fraction
Component Feed X 10
Benzene 5.53
Chloroform 39.8
1,1.2,2-Tetrachloroethane 29.1
Chlorobenzene 3.59
Ethyl Benzene 1.96
Tetrachloroethylene 15.4
Ethyl benzene .952
1,1,2,2-Tetrachloroethane 11.2
1,1,2,2-Tetrachloroethane 16.4
Benzene 3.01
Chloroform 2.53
Ethyl benzene .391
Chlorobenzene 1.51
Tetrachloroethylene .468
Chlorobenzene 1.32
Ethyl benzene .204
Tetrachloroethylene .174
1,1,2,2-Tetrachloroethane 6.79
Chlorobenzene .899
Chloroform 9.52
1,1,2,2-Tetrachloroethane 4.49
Chloroform 9.10
Ethylbenzene .170
Tetrachloroethylene .105
1,1,2,2-Tetrachloroethane 3.38
Benzene .809
Chlorobenzene .513
Ethylbenzene .117
1,1,2,2-TetracMoroethane 3.27
Benzene 3.08
Chlorobenzene .257
Ethylbenzene .199
Tetrachloroethylene .0557
Chloroform .324
Mole Fraction
Bottoms X 10 •
.303
.0876
.364
.437
.130
.365
.102
.692
.200
.0733
-.0062
.140
.0166
.315
.0296
.0129
.0693
.0175
.149
.192
.139
.00334
.00107
.118
.0859
.0184
.00372
.00258
.0555
.00876
.00297
.000357
.00364
PRIORITY
COLUMN
Calculated
Mole Fraction
Bottoms X 103
.000298
.00833
.0875
.000794
.000179
.0000905
.000101
.0446
.0452
.000138
.000431
.0000409
.000238
.00000318
.000283
.0000280
.00000162
.0222
.00000137
.00190
.0188
.00233
.0000213
.000000833
.00932
.0000374
.0000658
.00000959
.00975
.000153
.0000355
.0000176
.000000344
.0000588
 E-64

-------
may be somewhat limited in the range of influent concentrations investigated in this study



and that calculations predicated  oh these data should be viewed in the context of these



limitations.



         Column  efficiencies  are among the most critical of design parameters in that



they predict the actual number of trays for a tray column or the height of the packing for



a packed column.  The efficiency of any column is dependent on several  phenomena:  the



degree of mixing  of the liquid, entrainment  of liquid in the vapor phase, and the contact



time between phases.  They are always empirically determined  and essentially assess the



performance capabilities of the column.



         More recentfy Hwang has investigated tray and packing efficiencies in a follow-



up study for mixtures at extremely low  contaminant concentrations,  utilizing pilot plant



data and predictive correlations to revise and expand his earlier model (Hwang,  I980b). In



this latter  study,  Hwang has suggested the grouping of volatile  organic compounds based



on common parameters (e.g.,  functional groups and molecular weight) to streamline the



model.  EPA has solicited industry  for additional  data concerning priority pollutants that



are separated by  steam strippers  in order to assess the validity and  accuracy  of the



correlations  used for  column  design   and modeling.   These performance  data  on



commercially operating wastewater steam stripping columns are presented in Table E-17.
                                        E-65

-------







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ORGANIC ADSORPTION RESINS
Introduction
         Organic adsorption  resins  are  a relatively new system  for  removing organic
chemicals from  aqueous streams.  Resin adsorption performs like activated carbon:  a
waste  stream passes  through  a bed  of resin  beads,  which pick up  dissolved organic
molecules and colloidally suspended organic particles from the waste stream by means of
the Van  der Wools attraction between the resin and the organic molecules or particles.
Resin adsorption has been shown to reduce organic priority pollutant levels well below the
parts-per-million  range, performing  nearly  as well   as  activated  carbon.   Its  most
attractive feature is the ease with which a resin bed can be  returned to its original
adsorption capabilities after use—the major disadvantages of resin adsorption are the high
capital  cost of  the resin units and the problems of  disposing  of contaminated, spent
regenerant.
         Organic resin adsorption can be characterized as producing the same result as
activated carbon—removing trace organic priority pollutants from a waste stream, and
using the same equipment as ion exchange—columns of polymer  resin beads. An organic
adsorption resin  unit is generally a bed of small beads. Each bead is an aggregate of many
                                        -4
tiny microbeads of resin, ranging from  10   mm to I mm in diameter.  These resin beds
consist of agglomerated microbeads; the channels between these tiny  spheres provide a
large surface area—between 100 and 700  m  /g per bed,  depending on the type of resin—on
which adsorption can occur.  Some types of resin beads used in  organic adsorption  have
the same structure as the resin  beads used in ion exchange.  Resin beads  which do not
have the ionic functional sites are also  effective  in removing organic compounds  from
aqueous  solution.   These beads  consist  of a polymer  framework, or  matrix (generally
styrene-diviny!benzene  copolymer,  phenol-formaldehyde  copolymer   or  acrylic  ester
polymer) which bears ionic acidic or basic functional groups. Figure E-4  shows the  most
                                       E-70

-------
                                        FIGURE  E-4

                        WIDELY USED POLYMER MATRICES AND
                                  FUNCTIONAL GROUPS
                                        MotriCM
                        Styrene-
                        Divinylbenzene
                         ( Ml )
                                                       -CH,- C - CH, - C -
                                                          2  I    z  I
                                                                     c«o
                                                  OH
          Formaldehyde
            (M2)
                             I
                             0
                             i
                             CH,
                                                                     I
                                                                     0
Acrylic Ester
  (M3)
Anton Eicnonqe functional  Groupt
                        i
         ru             rw
         Vrr»»            wrlM
                       CH,
                       CH,

                      HydroMde
                      Form
                            Strong BOK
                     Quoternory Ammonium Group
                             (Al)
ffCHV Cl"
CH,
Chloride
Form
-N
H
Free BOM
Form
-N H*. cr
H
Acid Chloride
Form
                          Weak BOM
                      Secondary Amine Group
                           (A2)
                                 Cotton E«chqnce Functionol Groupt

                             -SOj, H*                -COOH
                             Stronq Acid
                             Sulfonote Group
                             Hydrogen Ion Form
                             ( Cl )
                     Weak Acid
                     Carboxyl Group
                     Hydrogen Ion Form
                      (C2 )
                              -Matrixes  and functional  groups  of  resins  com-
                                monly used for water purification.
SOURCE:  Kim etoL, 1976.
                                          E-71

-------
widely used polymer matrices and functional groups.  Polymeric adsorbents have the same



basic structure without the functional groups.



         In addition to polymeric  adsorption  resins, there is another  set of  adsorption



materials.  These are carbonaceous adsorbents, which consist of black spheres roughly  10



mm  in diameter,  intermediate  in  composition between  activated carbon and polymeric



resin adsorbents. Several  types of carbonaceous adsorbents ("Ambersorb" trade name) are



included in the investigations by Rohm and Haas which are discussed later in this report.



         For  polymeric adsorbents  the  polymer matrix is the site of organic adsorption.



Organic  molecules are attracted to the resin's organic matrix by Van  der Waals forces.



Attractive forces between the adsorbed organic molecules and the adsorbent resin matrix



are  relatively  weak, weaker than  the  attractive forces in activated carbon adsorption.



This means that the resins can be effectively regenerated by solvent elution.  The role of



the polymer's ionic functionalities, weak  and strong acid and base groups, is a secondary



one of attracting particular types of polar organic molecules to  the surface of the beads



to facilitate their adsorption onto the resin  matrix.  The actual driving force of the



adsorption process, howeve'r, is the affinity between an organic pollutant molecule and the



hydrophobic polymer resin matrix.  Adsorption occurs when this affinity is greater than



the  affinity  between  the organic pollutant  molecule  and  the  aqueous waste stream.



Therefore, organic adsorption  resins are  most effective in  situations  where a nonpolar



organic  pollutant is to  be  removed  from an aqueous  stream; the presence of ionic



functional  groups  acts  to  increase  the resin's affinity for slightly  charged organic



molecules by introducing electrostatic attraction.



         The pH of the aqueous stream being treated affects the degree to which slightly



polar organic molecules are adsorbed onto the  resin matrix.  pH  determines the extent to



which  an ionizable  organic molecule  will be polarized.  Therefore, since a hydrophobic



molecule will  be  more  strongly  attracted  to  the hydrophobic resin  matrix than  a
                                        E-72

-------
hydrophilic molecule, a weak organic acid (such as  phenol) will be best adsorbed from an



acid solution, where the organic acid will be present in its less water soluble nonionized



form—this is the phenomenon known as "salting out."



         Nonionic  resins  have been  shown to be particularly  effective in removing



chlorinated pesticides, detergent compounds, emulsifiers, wetting agents, dispersants and



all types of textile dyes.  These resins consist of a  polymer matrix and do not  include any



functional ionic groups; they are  regenerated with methanol, acetone,  isopropanol  and



similar solvents.



         Weakly basic  resins have been  shown to be effective  in  removing phenolics,



anionic surfactants, carbpxylic acids,  proteins, anionic  textile dyes and kraftpaper  waste



color bodies; weakly  basic resins with phenol-formaldehyde polymer matrices remove



phenolic organics particularly well.  Sodium hydroxide solutions regenerate these resins.



         Strongly acidic and strongly basic resins do not perform as well as weakly  acidic



and weakly  basic resins in  terms of removing organic molecules.  Furthermore, strongly



ionic resins  must be eluted  with large amounts of acid or base; and disposing of these



eluents requires special facilities.



         Organic adsorption resins generally are effective in the same situations  where



activated carbon adsorption is effective.  Resin adsorption differs from carbon adsorption



in that  resins can be  manufactured  to adsorb  specific types  of organic molecules by



selecting the appropriate ionic functionality on the  resin matrix and in that  the attractive



forces between adsorbent and pollutant molecule are weaker for  resin adsorption than for



activated carbon adsorption.  The fact that pollutants are  less  strongly  adsorbed onto



resin than onto activated carbon has  two significant implications:  first, the effluent



stream from a resin unit will have a  higher  concentration  of residual organic pollutants



than  an  effluent  from an equivalent  activated carbon unit and secondly, resin can be
                                        E-73

-------
regenerated with solvents or steam while activated carbon requires expensive thermal



regeneration.



         Although regeneration by elution restores the resin bed to most of its original



effectiveness  the elution  stream presents a disposal problem.   The  net  effect  of an



adsorption-elution cycle is to transfer pollutants from the waste stream to an  eluent



stream.  A technique frequently used is to isolate the first portion of eluent to come out



of the resin during elution. This eluent stream  is relatively concentrated and can be sent



to incineration or treated to recover the pollutant.  The second portion of eluent will



emerge from the resin bed with  a lower pollutant concentration.  This  eluent stream can



be recycled into  the waste stream entering the resin bed, or it can be used as the first



portion in the next elution.



         Elution regeneration, nevertheless, effectively restores resin  function.  Fox, of



Rohm  and Haas, describes a commercial phenolic  removal and  recovery  system using



Amerlite XAD-Aj "After 2 l/4-years of operation, the original resin performed the same



as it did during startup. Resin capacity measurements made in the laboratory  show the



used resin has  98 percent of its original capacity for phenol even after 1,300 load,  regen-



eration cycles" (Fox, 1978).



         Rohm and Haas applications for their commercial resins are given iri-TSble  E-18.
                                        E-74

-------
                               TABLE E-18

               ROHM AND HAAS COMMERCIAL RESIN APPLICATIONS
                           Adsorbent/Reoenerant in Wastewater Treatment
Waste Stream/Process

phenols  (BPA and others)


brine  (phenols and others)
pesticides  (cl-, NO--
  phenols)
nitroacromatics  (TDI
  and others

amines  (alkyl and
  aromatic)

grease  (misc. hydro-
  carbons

dyes

chlorinated organics
unidentified
   US (14 sites)

XAD-4/Methanol
XAD-4,XAD-7/Methanol

XAD-7/Methanol
XAD-74% Caustic
XAD-2,XAD-4/Methanol

XAD-4/Methanol
XAD-4/Isopropanol
XAD-4/2% Caustic

XAD-4/Acetone
XAD-2/Methanol
XAD-2/4% Caustic

XAD-2/steam
XAD-4/acetone

XAD-7/Methanol
XAD-4/4% Caustic
Foreign (13 sites)

IRA-93/Methanol
XAD-4/Acetone  (3)
XAD-2/4% Caustic



XAD-4/Methanol


XAD-4/Toluene  (2)


CAD-4/steam  (2)


CAD-4/Methanol

XAD-4(?)/steam (2)
                                  E-75

-------
Rohm  and Haas is a  leading  manufacturer  and  distributor of  commercial  organic



adsorption  resins; therefore, these listings  describe a significant portion of world-wide



resin use.



         Organic adsorption resins  are also used commercially to treat paper mill kraft



washes and are placed upstream to ion exchangers to prevent resin fouling.  The  latter



application exploits the affinity between resins and organic pollutants which caused the



fouling problem in the first place.



Preliminary Development of Resin Performance Data



         Rohm and Haas Studies



         Research aimed at developing reliable equations to predict the performance of



any synthetic resin by means of parameters easily obtained experimentally is currently



under way; no definitive design/performance equations have yet been developed.  Rohm



and Haas, a major commercial manufacturer of organic adsorption resins, has undertaken



a testing program to develop a simple laboratory test which will evaluate the performance



and cost of various  synthetic resins in removing organic  pollutants from industrial  waste



streams.  This laboratory test  is  intended to establish applicability of synthetic resin



adsorbents for removal of organic  pollutants from industrial  waste streams, to  identify



the most useful  resin or combination of  resins  and suitable regenerants  for them, and to



allow estimation of approximate  treatment costs.   Results of these  tests have been



presented by  Rohm and Haas as a series of quarterly reports entitled  "Synthetic  Resin



Adsorbents in Treatment of Industrial Waste Streams" (1980, 1981).



         The test evaluated in the Rohm and Haas study was the Batch/Rate Test,  which



measured both the amount of pollutant removed  by a known mass of a certain resin  and



the rate at which the pollutant  was adsorbed onto the resin.  The Batch/Rate tests were



performed on a variety of resins, including  resins manufactured by  Rohm and  Haas,



Mitsubishi, Diamond-Shamrock, Montedison, Calgon, and  Dow Chemical.  Batch/Rate test
                                        E-76

-------
results were supplemented by data from adsorption isotherm studies, and also by column



loading/regeneration  studies.  In the column loading/regeneration studies, the effluent



concentration  of  a  pollutant-bearing  stream  passing  through  a  resin  column  was



monitored.  Then, when the resin had been saturated with the pollutant, regenerant was



sent through  the column and analyzed as it was collected leaving the column to give the



cumulative amount  of  pollutant eluted as a function of the volume of eluent  pumped



through  the  bed.    The  resins used  in  this  project  are  listed  and  characterized in



Table E-12.  The synthetic  waste streams used were single-solute aqueous solutions of 2-



nitrophenol, tetrachloroethylene, 1,2-dichloropropane and  2,4-dinitrotoluene.



         Pilot  columns,  routinely  used  to  evaluate the adsorption  performance of



activated carbon,  cannot  be  effectively  used to evaluate  organic adsorption  resins,



because  synthetic resins are manufactured in a wide variety of resin types, with a broad



range of performance characteristics, amenable to regeneration  with numerous eluent



solvents. Determining  the  optimum adsorbent/regenerant pair from all the combinations



available would require  a  prohibitively  expensive and  time-consuming set  of  column



experiments.



         The first step in the Batch/Rate test is compiling adsorption  isotherms for the



adsorbents and waste streams being studied.



         The Batch/Rate studies measure the capacity  of a resin  to  adsorb  pollutants



from a stream and the rate at which  this adsorption rakes place.  In the Batch phase of



the Batch/Rate tests, the adsorbent is saturated with a  pollutant in a stream,  which is a



solution  of one of the four priority pollutants studied.   The saturated  adsorbent is then



eluted with a regenerant solution (acetone or rnethanol), and the eluent is analyzed for the



pollutant.  In the Rate part  of the Batch/Rate test, the adsorbent is exposed to the  waste



stream as it  is in  the Batch test.  However, small portions of the resin are taken out of



the waste at  regular intervals, while the resin is still being saturated with pollutant.  The
                                         E-77

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-------
portions of resin removed are eluted with regenerant  and the eluents  are analyzed for



pollutants; rate  test results are presented as adsorption capacity (mg pollutant adsorbed



per g of resin) determined as a function of the length of time the resin  has been exposed



to the pollutant.



        The Batch/Rate  tests were supplemented by column tests which were somewhat



analogous in design to the Batch/Rate tests.  Columns were packed with resin to construct



a bench-scale resin adsorption unit,  and column loading  and column regeneration tests



were performed.  Column loading tests consisted of passing pollutant streams (synthetic



single-solute solutions of  one  of four organic priority pollutants—2-nitrophenol, 2,4-dini-



trotoluene,  1,2-dichloropropane  and  tetrachloroethylene)  through  a  resin  bed   and



monitoring the  effluent  pollutant concentration.   In column  regeneration  tests,  the



columns that were saturated with pollutant  in the column loading tests are eluted  with



regenerant. The regenerant leaving the column is analyzed for pollutant.



        The    adsorption    data    from    isotherm,   Batch/Rate,    and   column



loading/regeneration studies are summarized in Table E-20 . The batch test has proven to



be a very  good predictor of saturation column capacity for single component streams. It



not only gives a more accurate saturation value  than the isotherm test, it also is a much



simpler test, requiring a single analysis after  exposure to the  influent waste stream.



        Equations which will predict resin  effectiveness  in removing organic pollutants



from industrial waste streams  by means of easily  determined parameters do not yet exist.



However,  Rohm and Haas* study represents the first steps towards these equations.   The



limitations of the  body of data assembled to  date (up to and  including the third quarterly



report, released by Rohm and Haas in August 1981) reflect  the fact that synthetic resin



adsorption is a new technology in the earliest stages of application.



        The most significant  limitation of the resin performance data  is that no studies



have been yet published  which describe  the performance of systems  in the course of
                                        E-7-9

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  E-80

-------
multiple saturation-regeneration cycles.   Therefore, estimates  of  an adsorbent's useful



lifetime cannot be made,  nor can the effectiveness of a multiply regenerated resin be



predicted as a function of the number of  its regeneration cycles. Because the ease with



which  resins can  be  regenerated is  one  of their most attractive  features, a complete



quantitative evaluation of resin performance will  include examining the performances of



resins which have been subject to more than one regeneration cycle.



         A second limitation  of the  studies is  that they were all  performed on  single-



solute  synthetic solutions of one of  four organic  priority pollutants.   Performance data



obtained  from streams more closely resembling industrial  waste  streams will more



reliably characterize resin performance in industrial application.



         Although no equations have yet been developed to  predict  resin peformance,



Rohm and Haas' investigation  included a preliminary evaluation of the  mathematical bases



of resin adsorption capacities  and rates, considered together with capacity and rate data



from the Batch/Rate  tests.  This evaluation is the  beginning of the development of a



theory of resin adsorption kinetics and equilibria to be applied to resin system design and



economics; it is  not  yet a reliable means of  quantitatively predicting resin adsorption



performance.



         Walk, Haydel Studies



         In addition, a  treatability study comparing carbon and  resin adsorption was run



by Walk, Haydel (I980a) in which equilibrium and dynamic studies on organic resin systems



were  performed.   Five organic  priority  pollutants  were  monitored:   chlorobenzene,



p-dichlorobenzene, nitrobenzene, dinitrotoluene,  and  phenol.   The  equilibrium  studies



were batch operations at three pH levels; it was found that adsorption performance  was



higher  at pH 6 than at pH 9 and  that the resin  had a low  adsorption capacity  at  low



pollutant concentrations, adsorption  capacity  increased with  the strength of the waste



stream.  Resin was found to be more effective than carbon for priority pollutant removal
                                        E-81

-------
at high pollutant concentrations, while carbon performed better than resin with a dilute



waste stream; resin performance was  more sensitive to waste stream concentration than



carbon performance.



         The dynamic studies  of  resin adsorption consisted  of six  runs  with methanol



regeneration between runs.  Constant leakage, 3 percent of the organic components of the



waste stream, was observed almost  from the beginning of the runs.  Table E-21 presents



an economic analysis, based on regenerability observations.   The Walk,  Haydel studies



concluded that resin adsorption of organic contaminants from an industrial wastewater is



technically  feasible,  and that  the  economic justification  rests  on a combination of



wastewater  cleanup and specific compound recovery.



Conclusion



         The conclusion to be drawn from the experimental studies by Rohm and Haas and



Walk, Haydel  is that  synthetic resin adsorption may be equivalent  to activated carbon



adsorption in effectiveness  in removing organic priority pollutants from industrial waste



streams.  The  absence of quantitative data  describing adsorption  capacities and resin



regenerability  prevents  a direct  comparison  between  the two methods.  However,  if



subsequent research indicates that resins can  retain their original adsorption capacities



after multiple saturation/regeneration cycles,  the  demonstrated effectiveness  of resin



priority pollutant adsorption plus the ease with which the regeneration operation can be



performed suggest  that  resin adsorption  may be a  valuable means of removing organic



pollutants from industrial waste streams.
                                         E-82

-------
                                    TABLE E-21
                   TREATMENT COSTS FOR RESIN ADSORPTION
        Basis: 1,130 1/min (300 gpm) treatment to 1 ppm {jrdicniorobenzene.
        Investment $1,700,000
Working Capital $ 370,000
Materials Cost
Streams units/vr S/unit
Resin ,
Replacement 28.3raa 1,833.92
Royalty ,
On Resin 28.3m' 424.03
Metbanol 1,239,840 1 0.17
Subtotal
Processing Cost
Labor Directed;
Direct taoor
Supervision 10% Direct Labor
Plant Overhead 100% Direct Labor
Subtotal
Investment Directed:
Amortization Cost*
Taxes ft Insurance £2% tnv.
Maintenance (§4% Inv.
Supplies I§1% to*.
Subtotal
Throughout Directed:
Steam $0.77/100 kg
Other Utilities
Subtotal
Total Treatment Cost
Treatment Costs
S/yr S/l.QOO I
290,000
12,000
213.000
47i,000 0.80
105,000
10,000
105.000
220,000 0.37
351,000
34,000
•8,000
17.000
47(T,Oub1 0.79
478,000
51,000
536.000 0.90
1,701,000 JUb .
        •Based on 12 years and IS percent intent.
SOURCE: Walk, Haydel,  I980a.
                                       E-83

-------
METALS REMOVED



         The two processes most  widely used in  industry to remove heavy metals are



precipitation, followed by coagulation and  flocculation,  and  ion  exchange;  both are



effective in removing the metallic priority pollutants from waste streams.  Precipitation-



cotogulation-flocculation uses relatively  cheap and  simple  equipment and  reagents to



reduce high influent metals concentrations (e.g., 100 mg/liter) to concentrations near the



ppm level.   Ion exchange systems on the other hand can remove metals originally present



at low concentrations (e.g., 1-2 ppm),  but is  complicated and expensive.   Moreover, in



many cases, the  stream entering the ion exchange  unit must be pretreated to remove



contaminants that would damage the ion-exchange resin.



Precipitation



         Precipitation is  a common  metals removal process based on the  solubility of



metal salts.  While a particular  salt of  a  given metal may be relatively soluble  in water,



another salt of the same metal may be  much less soluble in water.  An example is the



silver ion:  at pH  10, the silver cation in a solution of AgOH has a solubility of 10 g/liter,



while the silver cation in a solution of Ag2$  has a solubility of  10"   g/liter. Therefore,



introducing sulfide to a solution of AgOH (at pH 10) reduces the solubility  of  silver by



17 orders of magnitude.  Silver is precipated as Ag2S, an insoluble salt.



         The solubility of  a salt  is described quantitatively by its solubility product



constant K   .
For a salt solution in  equilibrium with its solid precipitate, K   = (M*)m(Xm~)n where m



and n are the stoichiometric coefficients of each species.
                                       E-84

-------
         Precipitation is, therefore, the process of introducing to a solution of metal ions



a particular anionic specie to form insoluble salts of those metal  ions, thus removing them



from  solution.  The choice of  the  particular anionic species that will  most effectively



precipitate pollutant metals, however, is rarely straightforward.  Industrial waste streams



often contain many ions, each  of which has a specific solubility  product.  Additionally,



industrial wastewaters often contain species that form water-soluble complexes with



metal  ions,  thus  increasing  their  resistance  to precipitation.   Amphoteric  metals,



berryllium,  cadmium,  chromium, copper, lead,  nickel,  and  zinc, form stable,  solvated



complexes at both high and low pH.  There is therefore  a narrow range of solution pH for



each metal in which hydroxide precipitation is most effective as shown in Figure E-5..



         Four types of chemicals are widely used industrially as precipitants:  hydroxides,



ferrites, sulfides and xanthates.  Metal hydroxides are the most  widely used precipitants.



Typically  lime   [Ca(OH)J  and caustic soda  (NaOH) are used.   Though hydroxide



precipitation  is  a  relatively simple and  inexpensive  procedure, it is limited  by  its



effectiveness in metal  removal:  soluble  metallic complexes  form at high pH and, in



general,  metal concentrations  range from several parts per billion  to parts per million.



Other  disadvantages  are that  hydroxide  precipitates tend  to  form  stable colloidal



suspensions and  that hydroxide precipitate sludge is bulky and presents a disposal problem.



         Ferrite coprecipitation can be used to precipitate zinc, cadmium, copper, nickel,



lead, and chromium from acidic wastewater.  In one ferrite coprecipitation procedure, a



ferrous salt  is added  to the heavy metal  containing waste stream; the stream is then



neutralized and the resulting heavy metal  ferrous hydroxide precipitate oxidized  to  the



stable ferrite coprecipitate.   Large particles  are formed by this procedure  and  the



resulting  sludges are  stable enough for safe landfill  disposal.   Another more energy-



intensive ferrite-coprecipitation procedure has been used in Japan primarily for removing
                                         E-85

-------
                        FIGURE E-5

        METAL SULFIDE AND HYDROXIDE SOLUBILITIES
                   AS A FUNCTION OF pH
10
10
10
10
10
10
  -10
10
  -12
      0  1
9  10   U 12  13  14
                            E-86

-------
chromium from acidic waste streams.  Chromium is electrolytically reduced from Cr(VI)



to Cr(lll) in  the  presence  of iron salts  and  forms  insoluble chromium  ferrite  (iron



chromite). The magnetized ferrites can be recovered from sludge by magnetic separation.



         Sulfide precipitation is similar to  hydroxide precipitation  in   principle  and



procedure.   Figure E-5  and Table E-22 show that  for  the metal  priority  pollutants



cadmium, copper,  lead, mercury, silver, nickel, and zinc, the metal sulfide is considerably



less soluble than the metal  hydroxide;  additionally, soluble metallic complexes are not



formed at high pH. Therefore, adding sulfide ions to  a metal-bearing waste stream  will



precipitate  larger  quantities of  metal from solution  than will hydroxide ions, and  will



result  in an  effluent containing  significantly  less  metal.   Despite  this  advantage,



hydroxide precipitation is more common  because lime  and  caustic soda are less expensive



than sodium  or ferrous sulfide, and also  because sulfide forms hydrogen sulfide (a severe



acute health hazard) if introduced to an acidic stream.  Thus use of sulfide precipitation is



largely limited to  a polishing  step  following hydroxide precipitation, when effluent



concentrations below those obtainable by hydroxide precipitation are required.  Treatment



systems  for  sulfide precipitation and for hydroxide precipitation  are similar, generally



consisting of a pH adjustment tank, a  flash mixer, a flocculator, settling units  with flash



storage,  and a dual media filter.  A pH adjustment to  pH 7 to 8 is critical because of the



risk of hydrogen sulfide generation.
                                        E-87

-------
                                   TABLE E-22

                  SOLUBILITY PRODUCTS OF TRACE METALS AS
                    HYDROXIDES, SULFIDES AND XANTHATES
Solubility Product
Constant (-log K )
Metal
Cadmium, Cd
Copper, Cu
Ferrous, Fe*
Lead, Pb
Mercury, Hg
Nickel, Ni
Zinz, Zn
Chromium (VI), Cr*6
Metal
Hydroxide
13.6
18.6
15.3
16.1
25.4
14.8
15.7
8.9
Metal
Sulfide
26.1
35.2
P6.9
26.6
52.2
25.7
25.2
-
Ethyl
Xanthate
13.6

7.1
16.9
37.8
11.9
8.3

        Xanthate  precipitation combines  aspects  of ion exchange  with a  chemical

precipitation process.   Xanthates  are  long-chain  starch molecules that bear  functional

groups capable of forming insoluble complexes with metals.  They can be generated by

mixing starch or cellulose with carbon disulfide  in a caustic medium.  .Three types of

xanthates have been studied:  soluble starch xanthate with a cationic polymer, insoluble

starch xanthate and fibrous cellulose  xanthate.   These were tested for their ability to

remove cadmium,  chromium(III), copper, lead, mercury,  nickel,  silver,  and  zinc.   In

general, xanthates  were found to be effective in removing metals over a wide pH range,

from 3 to II, with optimum performance between pH 7 and 9. The studies also concluded
                                      E-88

-------
that while cellulose xanthate and  starch xanthate were similarly effective in removing



trace metals, cellulose xanthate is superior to starch xanthate in terms of sludge settling



characteristics, filterability, and handling.  Xanthate may also  be used as a complexing



agent to prevent insoluble hydroxides of amphoteric metals from forming soluble anions as



the pH of the stream changes.



         Xanthate precipitation, however, is a new technology; reagents, therefore,  are



not yet available in commercial quantities,  and data has not been  gathered on dosage



rates  in  continuous  flow  xanthate  precipitation  operations.    Table E-23 presents



qualitative characterizations of the behavior of priority  pollutants during treatment by



precipitation.
                                        E-89

-------
                                   TABLE E-23
                     QUALITATIVE CHARACTERIZATIONS OF
                          PRIORITY POLLUTANT METAL
                            IONS FOR PRECIPITATION
BERYLLIUM:


CHROMIUM:




ANTIMONY:
Cr*
SbH
ZINC:



SELENIUM:


ARSENIC
Se<
                hydroxide  is  amphoteric,  sulfide  decomposes
                aqueous solution, sulfate is water soluble
                                               in
"hydroxide"  is  hydrated  oxide,  is amphoteric and
dissolves  in  excess  strong  base,   approximate
solubility = 0.00064 mg/liter.    Sulfide  cannot  be
made in aqueous solution, sulfate is water soluble

oxide is amphoteric, sulftde can be formed in acid
solution  (to  pH 6)  with solubility  0.0018 g/liter
(1.3 mg/liter  Sb), sulfide is  soluble  in  neutral to
alkaline solutions and  solutions  with  excess alkali
sulfide

amphoteric  hydroxide  gelatinous precipitate  when
formed in aqueous solution.
Kspof ZnS = 2xlO~14

oxide is very  water soluble, sulfide insoluble in
water, but dissolves in excess sulfide reagent

oxides soluble in water, As (V) sulfide
water solubility 0.0014 g/Iiter (0.6 mg/liter As)
As(lll) sulfide  water solubility 0.0005 g/liter  (0.3
mg/liter As).  Both sulfides soluble at pH 6 and in
excess alkali metal sulfide
                                       E-9-0

-------
Coaqulation-Flocculation



         Coagulation-fiocculation  is a  physical  treatment process  designed  to remove



suspended particulate matter known as  colloids and as such is an integral  part  of metal



removal  processes. Colloids exist because solids in water are always electrically charged;



one side of the solid-water interface assumes a positive or negative net electrostatic



charge.  This causes an equivalent number  of oppositely charged ions to form  a diffuse



layer  in the aqueous phase immediately  surrounding the metal particle. The electrostatic



repulsion between the diffuse outer layers surrounding the metal particles keeps the metal



particles in colloidal  suspension  and  precludes  their  agglomeration  and  subsequent



precipitation.  Removing  the  metal species from  colloidal suspension requires that the



charged  cloud surrounding the metal ion be destabilized.



         Coagulation is, therefore, the  process of destabilizing colloids suspended in the



waste stream by neutralizing the repulsive forces between them. This destabilization is



carried out  by adding certain ionic species known as chemical coagulants—generally low



molecular weight salts of multivalent inorganic ions, usually aluminum salts, iron salts or-



polyelectrolytes—and then gently stirring the suspension to facilitate contact between the



newly destabilized colloids. The result of the coagulation process is that the  colloidal



particles agglomerate into floes.



         Adding charged species to the waste  stream  destabilize colloids in two ways.



First, raising the electrolyte concentration in  the  aqueous  medium  lowers the diffuse



outer layers surrounding  each metal  particle, so the range  of electrostatic repulsion



decreases and  the short-range electrostatic attractive forces take  over.  Because this



phenomenon results   from  simple  electrostatic  attraction,  the  minimum  coagulant



concentration  required  to  destabilize  the  colloid is  independent of  the chemical



composition of the colloid. Therefore, quantitative data are not  available to describe the



response of each  individual priority pollutant  to coagulation and flocculation.  Second,
                                        E-91

-------
cations can bring the negatively charged layers surrounding each metal ion closer together



by  bridging  them  electrostatically.   Multivalent cations  are especially  effective in



bridging  heavy metal  colloids; a  trivalent  ion may be  1,000  times as effective as  a



monovalent ion.



         Flocculation is the process of getting these floes to coalesce still further to form



settleable  agglomerates.  Like coagulation, this  process involves  adding flocculants—



cations that  bridge small  floes  together  by  bridging  the negatively charged layers



surrounding each floe—and then mixing the suspension intensely but not violently.



         The two processes,  therefore, involve the same procedure:  ion  addition followed



by mild agitation.  Alum salts and iron salts are widely  used  both  as coagulants and as



flocculants; cationic polyelectrolytes can be used as coagulants,  but they are especially



effective as flocculants because they are long molecules containing  multiple ionic groups



and  are  therefore structurally  ideal  for  bridging  floes.    Agitation  is  generally



accomplished  by slow stirring with  long thin blades;  a coagulation/flocculation  unit is



usually a tank with  blades arranged inside as stators and rotors, equipped with meters to



dispense measured  quantities of  coagulants  and  flocculants.   TableE-24  presents  a



summary  (EPA,  I979c) of several coagulation-flocculation-precipitation processes  and



their effectiveness in treating the  metal priority pollutants.  Table  E-25presents typical



performances for some of these treatment processes as 30-day  average  effluent metal



concentrations.



Ion Exchange



         Ion  exchange  removes metal ions  from water by transferring them to  a solid



material, the ion exchanger, which accepts these undesirable  species at acidic or basic



exchange sites,  giving back  to the  aqueous phase an  equivalent number of a  similarly



charged  species  (usually H"1"  or OH") stored on the ion exchanger  skeleton.  When  the



exchange sites become  saturated  with the undesirable  ions,  the ion exchanger  is washed
                                         E-92

-------
                         TABLE E-24

               PERFORMANCE DATA SUMMARIES
               ANTIMONY AND ARSENIC REMOVAL

Treateent Technology
AntijTony
lire/Filter
Ferric chloride/Tilter
Alum/Filter
Arsenic
Lime Softening
Sulfide/Filter
Lime (260 ing/l) /Filter
Lowe (600 mg/1) /Filter
Ferric sulfate
Ferric sulfate
Line/Ferric Chloride/
Filter
Activated alunijia
(2 mg/1)
Activated carbon
ES

11.5
6.2
6.4
mf
6-7
10.0
11.5
5-7.5
6.0
10.3
6.8
3.1-3.6
Initial
Concen-
tration
(mg/1)

0.6
0.5
0.6
0.2
-
5.0
5.0
0.05
5.0
3.0
0.4-10
0.4-10
Final
Concen-
tration
(mg/1)

0.4
0.2
0.2
0.03
0.05
1.0
1.4
0.005
0.5
0.05
<0.4
<4.0
Rsroval

28
65
62
85
-
80
72
90
90
98
96-99+
63-97
  (3

Ferric Chloride

Ferric Chloride
  0.3      0.05

0.6-0.9   <0.13
98
                            E-93

-------
      TABLE  E-24 (Continued)



BERYLLIUM AND CADMIUM REMOVAL

Treat-rent Technology
Beryllium
Lire/Filter
Cadmium
Lime (260 mg/1) /Filter
Lire (600 mg/1) /Filter
Line Softening
Line/Sulfice 8
Ferrous Sulfide (Sulfex)
Ferrite coprecipitation/
Filter
pH

11.5
10.0
11.5
5-6.5
.5-11.3
8.5-9.0
neutral
Initial
Concen-
tration
•(mg/1)

0.1
5.0
5.0
0.44-1.0
0.3-10
4.0
240
Final
Concen-
tration
(irg/1)

0.006
0.25
0.10
0.008
0.006
<0.01
0.008
Reroval
(%)

99.4
95
98
92-98
98+
99+
99+
              E-94

-------
         TABLE  E-24 (Continued)



CHROMIUM 111 AND CHROMIUM VI REMOVAL
_«-_
Chraritn
Lire (260 mg/1) /Filter
lane (600 sq/I) /Filter
Red^^rv^
Reduction/line
Lire Scfierinj
lira/niter
Line
liae
Ferrite ecpracipitaticrv'
Filter
Ferric sulf ate
Ferric sulfate/TUter
ftrarian VI
Activated na:tm
(pulverized, ?iets-
bur?ft type 1C)
Ssre as above
Acsivaud «*-» ••* • "
Ferrite ceprecipitaucn
Sulfur rfirri<> reduction
Bisulfite reduffiisr.
-
10.0
u.s
7-8
7-8
10.6-11.3
7-9
9.5
9.5
—
6.5-9.3
—

3.0
2.0
6.0
	
—
	
Initial
Conoen-
traticn
(eg/I}
5.0
5.0
140 (as
Cr VI)
1300 (as
Or VI)
—
—
IS
3.2
25
—
5.0

10
10
3
0.5
—
—
Final
Cacea-
traticn
(mg/l)
0.1
0.1
1.0
0.06 CrIIX
0.15
0.05
0.1
<0.1
0.01
—
0.05

1.5
0.4
0.05
not
detectable
0.01-0.1
0.05-1.0
Ascv.il
98
98
—
—
98*
	
	
	
—
98*
99

85
96
98
	
—
—
                   E-95

-------
TABLE  E-24 (Continued)



 COPPER REMOVAL
Treatment Technology
Line/Tilter 8
Lime (260 mg/1) /Filter
Lime (600 mg/1) /Filter
Ferric sulfate/Filter
PH
.5-9.0
10.0
11.5
6.0
Loire >8.5
Lire
Alun 6
Lire/Sulfide 5
Ferrous sulfide (Sulfex) 8
Ferrous sulfide (Sulfex) 8
Ferrite Coprecipitation/
Filter
9.5
.5-7.0
.0-6.5
.5-9.0
.5-9.0

Initial
Concen-
tration
(mg/1)
3.2
5.0
5.0
5.0
10-20
3.0
3.0
50-130
3.2
4.0

Final
Concen-
tration
(mg/l)
0.07
0.4
0.5
0.3
1-2
0.2
0.2
<0.5
0.02
0.01
0.01
Renewal
(%)
98
92
91
95
90
93
93
-
99
99+
99-1-
       E-96

-------
                      TABLE E-24 (Continued)




                        LEAD REMOVAL

Treat-rent Technology
Line (260 mg/1)
Lime/filter
Lire (260 mg/1) /Filter
Lire (600 mg/1) /Filter
Ferrous sulfate/Filter
Sodium hydroxide (1 hour
settling)
Sodium hydroxide (24 hour
settling)
Sodium hydroxide/Filter
Sodium carbonate/Filter
Sodium carbonate/Filter
Sodium carbonate/Filter
Ferrous sulfide (Sulfex)
Ferrite coprecipitation/
pH
10.0
8.5-9.0
10.0
11.5
6.0
5.5
7.0
10.5
10.1
6.4-8.7
9.0-9.5
8.5-9.0
	
Initial
Concen-
tration
tmg/l)
5.0
189
5.0
5.0
5.0
—
— —
1700
1260
10.2-70.0
5.0
189
480
Final
Concen-
tration
(mg/1)
0.25
0.1
0.075
0.10
0.075
1.6
0.04
0.60
0.60
0.2-3.6
0.01-0.03
0.1
0.01-0.05
Removal
(%)
95.0
99.9
98.5
98.0
98.5
—
	
99+
99+
82-99+
99+
99.9
99.9
Filter
                             E-97

-------
 TABLE E-24 Continued)



MERCURY II REMOVAL
Treatment Technology pH
Sulfide
Sulfide 10.0
Sulfide/Filter 5.5
Sulfide/Filter 4.0
Sulfide/Filter 5.8-8.0
Ferrite ccprecipitation/
Filter
Activated Carbon
Activated Carbon/Alum
Activated Carbon
Initial
Concen-
tration
(ng/1)
0.3-50.0
10.0
16.0
36.0
0.3-6.0
6.0-7.4
0.01-0.05
0.02-0.03
0.06-0.09
Final
Concen-
tration
(ng/1)
0.01-0.12
1.8
0.04
0.06
0.01-0.125
o.ooi-o. ops
< 0.0005
0.009
0.006
Removal
(%)
-
96.4
99
99.8
87-99.2
99.9
-
-
—
         E-98

-------
TABLE E-24 (Continued)




  NICKEL REMOVAL

Treatment Technology
Liiie
Lire (260 mg/1) /Filter
Lime (600 mg/1) /Filter
Caustic Soda/Filter
Ferrous sulfide (Sulfex)
Ferrite coprecipitation
PH
8.5-9.0
10.0
11.5
11.0
8.5-9.0
—
Initial
Concen-
tration
(mg/1)
75
5.0
5.0
-
75
1000
Final
Concen-
tration
(mg/1)
1.5
0.3
0.15
0.3
0.05
0.20
Removal
(%)
93
94
97
-
99.9
99.9
       E-99

-------
                      TABLE E-24 (Continued)

                        SILVER REMOVAL
Treatment Technology
Scdium hydroxide
Ferric sulfate (30 ng/1)
Lime Softening
Chloride precioitation
PH
9.0
6-9
9.0-11.5
-
Initial
Concen-
tration
(mg/l)
54
0.15
0.15
105-250
Final
Concen-
tration
(mg/1)
15
0.03-0.04
0.01-0.03
1.0-3.5
Removal
(%)
72
72-83
80-93
97+
(alkaline chlorination
 in the presence of
 cyanide)
Ferric chloride/Filter
Sulf ide precipitation
6.2 0.5
5-11
0.04 98.2
- verv hich
* \ •"
                               E-100

-------
      TABLE £-24 (Continued)



SELENIUM AND THALLIUM REMOVAL

Treatment Technology
Selenium
Ferric chlorice/^Tilter
Ferric chloride/Tilter
Alum/Filter
Ferric sulfate
Ferric sulfate
Lime/Filter
Lime/Filter
Thallium
Lire/Filter
Ferric chloride/Filter
AlurVFilter
PH
6.2
6.2
6.4
5.5
7.0
11.5
11.5
11.5
6.2
6.4
Initial
Concen-
tration
(ng/1)
0.1
0.05
0.5
0.10
0.10
0.5
0.06
0.5
.0.6
0.6
Final
Concen-
tration
(rrg/1)
0.03
0.01
0.26
0.02
0.03
0.3
0.04
0.2
0.4
0.4
Raraoval
(%)
75
80
48
82
75
35
38
60
30
31
             E-101

-------
TABLE E-24  (Continued)



   ZINC REMOVAL
Treatment Technology
Line/Filter
Lime (260 mg/1)
Lime (260 mg/D/Filter
Lime (600 mg/1)
Lime (600 mg/1) /Filter
Lime/Filter
Sodium hydroxide
Sulfide
Ferrous sulfide (Sulfex)
Ferrite coprecipitation
pH Initial
Concen-
tration
(mg/1)
8.5-9.0
10.0
10.0
11.5
11.5
-
9.0
-
8.5-9.0
-
3.6
5.0
5.0
5.0
5.0
16
33
42
3.6
18
Final
Concen-
tration
(mg/1)
0.25
0.85
0.80
0.35
1.2
0.02-0.23
1.0
1.2
0.02
0.02
Removal
(%)
93
83
84
93
77
-
97
97
99+
99+
         E-102

-------










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 W
                     
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with regenerant, a  strong solution of  the ion originally present on  the  resin—usually



mineral acid or caustic soda. The pollutant species accumulated on the resin are replaced



by the original species of  ions from the regenerant  and the exchanger is returned  to its




original usable condition.



         The  ion exchanger is almost always a three-dimensionally cross-linked polymer



resin to which particular ionic function-alities are attached.  There are four categories of



ion-exchange  resin,  each  with a  characteristic set  of functional groups, which interact



most  strongly with  a particular  type of charged species.  First  are the strongly acid



cation-exchange resins.  Their general formula is Res-SO^-H"1" where "Res" represents the




polymeric resin structure.   Most typically, strongly acid-cation exchange resins consist of



polystyrene sulfonic acid  cross-linked  with  divinylbenzene.   Second, there are weakly



acidic cation-exchange  resins:   Res-CC^-H.  These  are generally  polyacrylic  acid or



polymethacrylic acid  cross-linked with divinylbenzene.  Third,  there  are  strongly basic



an ion-exchange  resins:  Res-NR«-OH, where R is an  aliphatic or aryl-aliphatic  radical.



Strongly basic an ion-exchange resins  generally are  polyvinylbenzyl trimethyl-ammonium



hydroxide cross-linked with divinylbenzene.   And fourth,  there  are weakly basic anion-



exchange resins: Res-NR2«  Several varieties of these are available; all contain tertiary



aliphatic  or aryl-aliphatic amine function-alities  on  resin matrices  ranging from  the



polystyrene type through polyacrylate to aliphatic polyamine condensation products.



         The  selectivity of a particular resin is a function of the size and charge of the



ions  to  be  exchanged—an  exchange  resin prefers  highly charged multivalent  ions.



Knowledgeable choice of  a particular  ion exchange  material  from  the wide range of



selective  resins commercially available can often allow selective separation of  one ion



from  another, allowing  selective  removal of an undesirable ion from a stream  bearing



many other ions.  The affinity of a particular ion exchange resin for a particular ion is a



function of several  factors, including ion size and charge, the composition of  the  waste
                                        E-105

-------
stream,  and the  functional  group and  polymer  structure  of the  resin.   Extensive



commercial literature is available  for the engineer intending to design an ion-exchange



system to remove particular metals from a particular waste stream.



         Commercially available ion exchangers operate in one of  two modes:  fixed bed



or continuous.  (Figure E-6 presents their flow diagrams.) Fixed bed  units perform  in a



four-operation cycle.  First, service wastewater flows  through the ion  exchange unit until



the point of exhaustion is reached where all available ion-exchange sites are occupied by



pollutant ions.  Second, backwash water is pumped through the bed in  the direction oppo-



site to that of the waste stream during the service phase.  Third, regeneration occurs in




which a strong solution of the ion originally occupying the exchange sites on the resin is



pumped through the bed to dislodge the pollutant ions and  return the resin to its original



composition. And fourth, the resin is rinsed with water. The backwash phase is necessary



to flush  out extraneous  particles from between the resin beads.   Fixed bed units can



operate cocurrently—the regenerant is pumped through the unit in the same direction the



waste stream flowed-or counter currently—the regenerant  flows in  the opposite direction



from  the waste stream.  Countercurrent regeneration is more effective than cocurrent



regeneration because  the maximum pollutant sorption occurs  where the waste stream



enters the  ion-exchange unit.   Sorption sites become progressively less occupied by



pollutant ions along  the  path of the waste  stream through  the unit.   Therefore, the



countercurrent method is better because it brings fresh regenerant into contact  with the



part of the resin bearing the fewest pollutant ions and as the regenerant proceeds through



the unit and  becomes less  concentrated,  the  resin along the path  of  the regenerant



becomes more heavily occupied with contaminant ions—therefore a mass ratio regenerant



iontsorbed  metal ion  favorable to regeneration  is  maintained all along the regenerant



path.
                                       E-106

-------
                             FIGURE E-6

                ION EXCHANGE BED CONFIGURATIONS
Co-Current
Fixed Bed Mode
                       Service Za
1*1
                                           Regenerant In
                      Service Out  "III        Regenerant Out|j|


                              Service Step            Regeneration Step
Counter-Current
Fixed Bed Mode
                       Service In
                      Service Out
             Regenerant Out
                                  _          Regenerant Zn


                            Service Step               Regeneration Step
 Counter-Current
 Continuous Mode
                    Service Zn
                    Service  Out
                 Regenerant Out
                                  1
                                       Resin Flow
                         Hash To Remove
                            Fines


                         Pulse Generation
                         Section
                                                   ~ » Regenerant Out
                                E-107

-------
        Continuous  ion-exchange operations are run countercurrentty.  Figure M-6 shows



how ion-exchange resin beads are circulated through a loop.  One segment of the loop is



the seryice segment, through which wastewater to be treated is sent, and another section



is the regeneration segment, through which regenerant is passed in a direction opposite to



the direction the wastewater took.



        Since ion exchange is  basically a method for tranferring pollutant ions from the



waste stream to  the regenerant solution, there arises the problem of  disposing of the



spent regenerant.  In some cases, it is economical to recover the metal pollutant from the



regenerant.  Disposal or  recovery is simplified  when the  volume of regenerant  is



minimized.   Many fixed bed  units minimize  regenerant volume with the "staged" or



"proportional" regeneration technique.  The first part of the regenerant leaving the ion



bed is the most enriched in the pollutant  species being removed. This portion is sent to



treatment or disposal. The second portion of regenerant to leave the ion-exchange bed



leaves with a significantly  lower pollutant concentration.  It is stored and used as the first



portion of regenerant in the next service regeneration cycle.



        Ion exchange removes metal priority pollutants  with outstanding efficiency.



Table E-26 summarizes  the results of treatability studies  on ion exchange  removal of



priority pollutants.    Most removal efficiency  percentages are  in the high nineties.



Table E-24 summarizes  ion exchange removal efficiencies  for  each  metal  priority



pollutant  obtained in treatability  studies with  industrial  wastewaters and  synthetic



solutions.



        One chemical company has prepared a summary of  treatment and cost data for



an industrial ion-exchange  system, treating a chromium-bearing waste, which it considers



to represent BAT for chromium removal.  The waste stream is a cooling tower blowdown,



containing chromium added to inhibit growth of fungi and algae.
                                       E-108

-------
                                TABLE E-26

               TREAT ABILITY STUDIES SUMMARY FOR PRIORITY
                 POLLUTANT REMOVAL WITH ION EXCHANGE
METAL
As
Cd
Cr
Cu
Pb
Hg
Ag
Zn
DATA
POINTS
19
17
12
3
2
5
5
7
EFFLUENT CONC., mg/1
MEAN MED MIN
1.65
0.019
0.36
1.8
0.03
0. 0005
3.5
2.2
0.60
0. 0003
0.05
2.0
-
0.0001
0.14
0.4
0.0
0.0001
0.01
0.5
-
0
0.01
0
8.
0.
1.
3.

0.
6.
10
MAX
0
1
8 (11)
0 (4)
-
002
5 (7)
(9)
MEAN
87.1
96.8
96.7
96.5
99.85
99. 9*
93.7
97.7
REMOVAL %
MED MIN
96.5
99.9*
99.5
97
-
99.9*
95
99
21
75
88
93
-
99.9*
90
90
MAX
100
99. 9H
99.9
99*

100
100
100

*


*

*
*
*
*Data  set includes results from synthetic solutions.

()  s Data points used for that computation.
                                  E-109

-------
         This application  for  ion  exchange is  relatively  new technology.  Slowdown is



filtered and pH adjusted  before passing through weak base anion exchange vessels for



chromium removal and  then weak acid cation  exchangers for zinc and trivalent chrome



removal. Upon regeneration of the resins, chrome and zinc can be recovered and recycled



back to the cooling towers eliminating a large percentage of the make-up chrome and zinc



solutions. Another advantage of ion exchange is  the elimination of voluminuous metal



sludges formed in the precipitation technique  commonly employed  for chrome-and-zinc



removal in cooling tower blowdown.



         Figure E-7  is the flow diagram of the system. TableE-27 summarizes operating



parameters and removal data.  Tables E-28 and  E-29 present daily and rolling  average



chromium effluent concentrations.



         The ion exchange units were installed  in January 1978 and have consistently met



the NPDES permit.  Installed costs were $4.7 million.  The operating costs for the  first



quarter of 1981 were  approximately $80,000/month. This figure includes utilities services,



wages,  salary and  payroll overhead,  maintenance,  chemical  requirements,  laboratory



analyses,  technical  engineering  services,  catalyst  (resin),  fixed  indirects,  and  unit



depreciation.  Assuming an average flow of 650 gpm, at 8 ppm Cr °  removal across the



unit, this comes to roughly $W/pounds of Crtot or $2.85/1,000 gallons.



         A survey of published ion exchange treatability data is presented in Tables M-3Q



These data were compiled by Calmon, Casana, and Gold of Water Purification Associates



(1980); many of these represent results obtained  with synthetic solutions.



         Minor drawbacks  to  the  application of  ion  exchange  to  industrial waste



treatment exist. They include the problems of spent regenerant disposal,  susceptibility to



damage by high temperatures and strong oxidants, and the tendency to contamination by



organic matter present  in the waste stream. Furthermore, suspended organic solids will



foul the resin and aromatic molecules will be irreversibly adsorbed onto the resin.
                                       E-110

-------
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-------
                                TABLE E-27

                   CHROMIUM AND ZINC REMOVAL SUMMARY


Treatment Technology:  Ion Exchange

Data Source:  Cooling Tower Slowdown       Data Source Status:
Point Source Category:  Organic Chemicals   Engineering estimate
Subcategory:                                Bench scale
Plant:                                      Pilot scale
References:                                 Pull scale

Use in System:  Cr Removal and Reuse
Pretreatment of Influent:  Dual Media Filtration (Anthracite/Sand,
                           pH adjustment

Design or Operating Parameters*

Wastewater Flow:  400 gpm Avg? 1000 gpra avg design  1500 gpm max design
Solids Loading Rate:  0.50 lb/day/ft* based on 400 gpm 8 40 ppm TSS
Bed Height:  Anion 44"  Cation 36"
Pressure Drop:
Resin Type:  Anion Rohm & Haas IRA-94  Cation Rohm & Haas DP-1
Avg. Run Length:  Anion 1 regeneration/day  Cation 1 regeneration/3
                  days  (based on 400 gpm)
Regenerant Used:  5X HC1  5X NaOH
Cycle Time:  8 hrs/regeneration time
Backwash Rate:
Resin Pulse Volume:
Unit Configuration:  Dual Media Filtration, pH adjustments, Anion
                     Exchange  (.Chrome Removal), Cation Exchange
                      (Zinc Removal)


                        REMOVAL DATA

              Sampling period:  7/1/79 - 7/31/30

                               Concentration, mg/1    Percent
         Pollutant/Parameter  Influent    Effluent   Removal

         Toxic pollutants:
          Chromium

             Mean Concentration 10.94         .48        94

             9_ath percentile   36.00       2.58        99

             9.5th percentile   21.78       1.20        99

             9.0th. percentlle   17.31       0.80        98
                                  E-112

-------
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-------
          TABLE E-30

POLLUTANT REMOVAL SUMMARIES
  ARSENIC REMOVAL SUMMARY
Source

Potable Well
Potable Well
Potable Well
Synthetic
As cone
Influent
1.06
0.84
0.09

Drinking Water 0.06
H
M
M
H
"
"
"
«
II
M
n
"
"
Geo thermal

1.06
24.7 *
60.1 •
104 *
12.8 •
25.4 *
34.7 •
6.54*«
13.4 ••
26.7 *•
6.75"
13.4 ••
26.7 ••
100 •
100 **
(ag/1)
Effluent
0.01
0
0

0.003
0.17
0
0.6
3.0
0.5
1.9
5.7
1.33
2.3
8.0
0.7
2.3
5.5
0
0
Removal (%)

91
100
100

99.5
21
100
99
97
96.5
92.4
83.5
79.6
73.0
70.0
88.8
83.0
79.3
100
100
Coriined Data
Source
Potable Well
Synthetic
TOTAL
Data
Points

3
16
19
As effluent cone, (aw/1)
mean aed
0.003 0
1.96 1.01
1.65 0.60
min max
0 0.01
0 8.0
0 8.0
As Removal (%)
mean aed min max
97 100 91 100
85.2 90.6 21 100
87.1 96.5 21 100
           E-115

-------
                  TABLE E-30  (Continued)

               CADMIUM REMOVAL SUMMARY

(an Cd/l)
Data
Pts. Mean Med Min Max
14 0.0018 0.0002 0.0001 <0.01
3 0.1 0.1 0.1 0.1

17 0.019 0.0003 0.0001 0.1
Jieisoval ( ^ )
HA
no.
Data.






?ts. Mean Med. Min. Max.
1« 96.2 99.9* 75* 99
3 99.7 99.8 99.5* 99
+ ^
17 96.8 99.9 75 99
.9*
.9*
4f
.9




Sours* Initial Other
woncv^AA W^OH
(ae/1 Cd) Ps
CdSO. Synthetic
solution 5




Gas Hashing
Hastevater 0.039
•esent ment Volsse (ac/1 Cd) (»)

pa adj. 8.6 500 0.
1000 0.
1600 0.
3000 0.
4800 0.

Hg;Cu pH adj. S.S. 1000 <0.

0001*
9002*
0003*
008*
0018*

01*«
Reacvel 200Q <0.01..
w.w. rrea
Phsto Plant 1.7 Organic

:> pH adj. 100 <0.

001
^••••••••^B
99.9*
99.9*
99.9*
99.9*
99.9*

75*
75*

99.9*
C Inorganic S.S. res.
Sales
WW *rea Cd
Placing 4.6 CS «


pR adj. S.S. 100 <0.


001


99.9*
Inorganics res. NaCIO

ww 5-ss Cd
Battery Plant 0.02


Flue gas
Trtatsent
rea. CK

pH adj. 9.0 100 0.
S3 rtsoved 100 0.
300 0.


Solution 0.8 Hg pH adj. 9.0 1000 0.
Cr 3000 0.


0002
0002
OOC2


0002-
0003*


99
99
99


99.9*
99.9*
?b
Inorg. Salts
          in s«ri*s.
Cth«r haavy sctals r»duc«d
ta vtry low levels.
                              E-116

-------

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                                 E-117

-------
                        TABLE E-30 (Continued)

                   CHROMIUM REMOVAL SUMMARY
               Concentration(rag/l  as Cr)              _    ._
               	•	             Capacity-
 Source           Influent    Effluent   Seaoval(%)   (*CrO /ft )

 Plating Waste       44.8        0.025       99.9      1.7 - 2.0
 (rinse water)

 Cooling Tower        9.8        0.02        99.8         3.0
 Slowdown
(Electroplating)
 Electroplating     41.6        0.01        99.8      5.2 - 6.3
 Waste (Rinse
 Water)

 Cooling Tower
 Slowdown           17.9        1.8         90          5-6

 Cooling Tower
 Slowdown             -         0.1

 Cooling Tower
 Slowdown           10          1           90       2.5 - 4.5

 Cooling Tower      7.4-10.3     1          86-90
 Slowdown

 Coolifio Tower       20        < 0.05        99.4
 Slowdown
 Cooling Tower       10          0.05        99.5      0.6 - 5.2
 Slowdown

 Wool Dyeing
 Wastewater       10-20         0.05     99.5-99.75  0.6 - 5.2

 Cooling Tower
 Slowdown          8.96         0.2      97.7          2.51
 (Chesicai
 Complex}

 Pigaent          1210         <0.5      99.9+
 Manufacture
 Wastewater
                                E-118

-------
   TABLE  E-30 (Continued)
COPPER REMOVAL SUMMARY
Source
Synthetic
Synthetic
Synthetic
Synthetic
£ff (ma /I Cu) Removal
-
-
93
0.5 99
Rayon Wastewater 3.0 99+
Pickle Rinse


No data ?ts
3

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4

No data r>ts
4
Soln. 2.0 95
Combined Data
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Mean Med
1.8 2.0
Removal %
Mean Hed
96.5 97
Capacity (mec/1)
Mean Med
1303 =1290
(\) Capacity (aes/1)
-
1220 (pH 4)
-
1250 (H* forr
1412
1330


Min Kax
0.5 3.0

Min Max
93 99+

Min Max
1220 1412
         E-119

-------
                       TABLE E-30 (Continued)

                     LEAD REMOVAL SUMMARY
  Source     InfCag/1 Pb)  Eff (n»c/l Pb)  Removal (%) Capacity

Azssunition

  Plant         6.5            0.01        99.8

Wastevaters


Synthetic      50              0.05        99.9        4.4 lb/ft3
Solution

               28.5            0.03        99.85       4.4 lb/ft3
                               E-120

-------














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                                           E-122

-------
                       TABLE  E-30  (Continued)

                     SILVER REMOVAL SUMMARY
Influent
Synthetic So In.
Synthetic So In.
Sand/Carbon Treated
Effluent Cone.
(mq/1 Aq)
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Not reported
0.01
Removal
%
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91.7
Not reported
Photographic wastes 10
Photographic wastes <1
Photographic wastes 6.5
95
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90
278
75
900-1300
                               E-123

-------
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-------
Conclusion



         The vast majority of waste  treatment systems in the organic chemicals  and



plastics industry use coagulation-flocculation-precipitation,  or  ion exchange, or both, to



remove metal  priority pollutants  from wastewater.   However,  other metal-removing



systems  exist and are  used  to some  extent  as in  the inorganic  chemicals processing



industry.   These are  reduction and oxidation  processes, membrane processes (reverse



osmosis), and carbon adsorption.
                                       E-127

-------
                                 REFERENCES *


AMORE, F..  1979.  Anal. Chem. 51:1105A

BEAUDET, B.A., BILELLO, L.J., KELLAR, E.M., and ALLAN, J.M.  (ESE), and TURNER,
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CATALYTIC, INC.  1978. Letter of 20 September 1978  to CMA Committee for review of
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CATALYTIC, INC.  I979b. Laboratory Study of Biological System Kinetics. Biological
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                                    E-128

-------
FE1LER,  H.   1980.  Fate of Priority Pollutants  in Publically Owned Treatment Works-
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                                      E-129

-------
HYDROSCIENCE,  INC.    1981.   Survey  of Industrial  Applications  of Aqueous-Phase
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                                     E-130

-------
LIPTAK, B.G. 1974. Environmental Engineers'Handbook. ChiIton, Radnor, Pa.

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                                     E-131

-------
    U.S.  ENVIRONMENTAL PROTECTION  AGENCY  (EPA).   I979b.   Treatability of the
         Priority Pollutants by Activated Carbon.  Hwang, S.T., Organic Chemicals Branch,
         Washington, D.C. June 1979

    U.S.  ENVIRONMENTAL PROTECTION  AGENCY (USEPA).   I979c.  Coagulation and
         Precipitation of  Selected Metal  Ions from  Aqueous Solutions.   Research  and
         Development, Washington, D. C. EPA 600/2-79-204

    U.S. ENVIRONMENTAL PROTECTION AGENCY (EPA).  I979d. Self-Monitoring Program
         Analytical Methods Package.  EPA 440/1-79/102, Washington, D.C. July 1979

    U.S.  ENVIRONMENTAL PROTECTION  AGENCY. (EPA). I979e.  Review of Existing
         Conventional Pollutant BAT Effluent Guidelines (Section 73 of Clean Water Act of
         1977).  Action Memorandum from Assistant Administrator for Water and Hazardous
         Materials to the Administrator, June 22, 1979

    U.S. ENVIRONMENTAL PROTECTION AGENCY (EPA).   I980a.  Treatability of Priority
         Pollutants in Wastewater by Activated Carbon.  Hwang, S.T., Organic  Chemicals
         Branch, Washington, D.C. To be presented at the AlChE Philadelphia meeting.  June
         I960

    U.S.  ENVIRONMENTAL PROTECTION AGENCY (EPA).  I980b.  Computerized Waste-
         water Treatment Model.  Technical Documentation.  September 1980

    U.S.  ENVIRONMENTAL PROTECTION  AGENCY  (EPA).   1981 a.   EPA files, Organic
         Chemicals Branch

    U.S.  ENVIRONMENTAL PROTECTION  AGENCY (EPA).  I98lb.   Bench-Scale Stean,
         Stripping  Treatment of Organic  Priority Pollutants.   Office of Research  and
         Development,  Robert  S.  Kerr Environmental Research  Laboratory,   Industrial
         Sources Section, Ada, Okla.

    U.S. ENVIRONMENTAL PROTECTION AGENCY (EPA). No date.  Treatability of Priority
         Pollutants by Coagulation/Flocculation. Research Triangle Park

    WAITE, W.H.  No date.  Pollution Control  Through  Selective Ion Exchange.  Rohm and
         Haas Co., Philadelphia, Pa.

    WALK,  HAYDEL  AND ASSOCIATES,  INC.   I980a.   Laboratory  Studies of Priority
         Pollutant Treatcbility.  Prepared for the U.S.   Environmental Protection Agency,
         Office of Research and Development, Industrial Environmental Research Labora-
         tory, Cincinnati.  Contract No.  68-03-2579, Directive 2579 WD-6

    WALK,  HAYDEL AND ASSOCIATES, INC.  I980b.   Industry  Survey to Determine the
         Performance of Activated Carbon Adsorption. Prepared for the U.S. Environmental
         Protection Agency

    WISE,  H., and FARENTHOLD, P.   1981.   Occurrence and Predictability  of Priority
         Pollutants in Wastewaters of the Organic Chemicals and Plastics/Synthetic Fibers
         Industrial Categories. Effluent Guidelines Division, U.S. Environmental Protection
         Agency
* References from other sections of the  1981 Contractor's Engineering Report also
in this reference list.

                                         E-132

-------
            APPENDIX F

STATISTICAL DETAILS AND DEVELOPMENT OF
        VARIABILITY FACTORS

-------
                                APPENDIX  F

                  STATISTICAL DETAILS AND DEVELOPMENT OF
                            VARIABILITY FACTORS
    This Appendix presents the major  statistical methodologies and data

processing procedures used in the development of the proposed effluent

limitations from the OCPSF effluent data.  As explained in Section IX,

variability factors were determined using organic priority pollutant data from

the CMA study and heavy metals data from five BPT Daily Data File plants.

Organic priority pollutant data from  the Verification study were used in

conjunction with the CMA data to determine median long term values for

calculating the effluent limitations.  The Screening data were used to

investigate BAT subcategorizaton.  Some elementary formulas and definitions

are presented first; subsequent sections discuss the rationale for using daily

sample averages to model effluent variability, goodness-of-fit tests,

derivation of variability factors, example variability factor calculations,

and the statistical methodology used  to investigate BAT subcategorization.




A.  FORMULAS AND DEFINITIONS

    Important formulas and definitions of statistical terms used in this

appendix include the following:




    1.   N - number of valid  observations used in a particular analysis (e.g.,

         the total number of  valid effluent values at a particular plant for a

         particular pollutant)
                                  F-l

-------
                                          N

    2.    Mean - arithmetic average:   X =  I  X./N
                                                        N

                                                                  _ 9
    3.    Variance (unbiased estimate):     02  _   1       I   (X.  -  X)
                                          o   —                i

                                               N -  1    i=l






         (The standard deviation is  S = Vs  .)




    4.    Minimum - the smallest value in a set of N observations.







    5.    Maximum - the largest value in a set of N  observations.







    6.    Range - the minimum subtracted from  the maximum







    7.    Median - the middle value in a set of N observations.   If N is odd (N



         = 2k - 1 for some integer k),  the median is  the kth order statistic,



         C(k).  If N is even (N = 2k),  the median is







                            l/2[C(k) + C(k +  1)].





B.  RATIONALE FOR USING DAILY SAMPLE AVERAGES IN MODELING EFFLUENT VARIABILITY



    In the CMA Five-Plant Study, multiple measurements of organic  pollutant



concentrations in daily samples were made by  one or more laboratories.   Thus,



several reported values of a specific pollutant concentration were available



for a particular daily sample.  Because NPDES permits require a single



reported value, the Agency considered several alternate approaches for



characterizing the variability of the pollutant concentration of individual



daily samples.  The following approaches were considered.
                                   F-2

-------
         •    Arbitrarily selecting one measurement per day and




              calculating a variance from the selected measurements









         •    Calculating daily sample averages of multiple




              measurements and computing a variance of the results









         •    Performing a variance component analysis using




              replicate measurements and adding estimates of




              relevant components to estimate the variance of a




              single measurement.









The first alternative was rejected because it does not use all the data and




gives different answers depending on which measurements are selected.  The




second method is a way duplicate measurements can be handled in NPDES




reporting; it is more straightforward than the last alternative, which




eventually also was rejected.  The variance component method is described




briefly below.









    A variance component analysis of data for a given plant and pollutant




characterizes variation in effluent monitoring results at the plant by




estimating a variance component for each relevant source of variation.




Because of the way the CMA study was conducted, it was possible to estimate




variance components for the following sources:
                                   F-3

-------
         •    Within-day variation attributable to short-term


              replication errors within a laboratory





         •    Between-day variation attributable to process,


              treatment, sampling, and longer-term


              within-laboratory variation





         •    Between-laboratory variation.





The between-day and between-lab variance components generally are larger than


the within-day variance component because many more factors affect between-day


and between-laboratory variability.





    Although it was possible to estimate a between-laboratory variance


component from the CMA data, it was not necessary to do so to characterize


effluent variability.  In practice, a single laboratory generally performs all


monitoring analyses of a given pollutant at a given plant, so


between-laboratory differences do not affect observed effluent variation at a


plant.  (Between-lab differences do contribute to between-plant differences,


which are reflected in the observed long-term performance of the industry.)
                                                                        2
    Given estimates of the within- and between-day variance components a


     o
and of" for a specific plant and pollutant, the variance of a single
measurement is estimated from
                                   o2 = o2 + o?.
                                         w    b
                                   F-4

-------
              9      2
Estimates of a  and or" can be obtained from data for a given plant,
              w      b



lab and pollutant using formulas in Linear Models (Searle, 1971).
    A comparison of the daily sample average and variance component approaches



resulted in selection of the daily sample average because of its relative



simplicity, its confortnance to general monitoring practice, and its tendency



to give conservative variance estimates.  The conservativeness of the daily



sample average approach results from including measurements from different



laboratories in the daily average.  This tends to make the variances of daily



average data larger than corresponding variance component estimates.







    TABLE F-l shows a comparison of standard deviations estimated from the CMA



data by the two approaches.  The variance component estimates in the table



were based on log  (C-10) for individual concentrations (C) above 10 Vg/1;
                 6



the daily sample average estimates were based on log  (C-10) for daily
                                                    G



sample averages (C) above 10.  Note that in 8 out of 13 plant-pollutant



comparisons, the daily sample average result was larger.  The median standard



deviation for the daily sample average method was 1.54 compared to 1.37 for



the variance component method.







    Daily sample averages were computed by averaging replicate measurements



within laboratories and then averaging the results across laboratories.



Before computing daily sample averages for organic pollutants, it was



necessary to decide how to handle results below the detection limit (<10



yg/1).  Alternatives considered were to exclude such values or to replace



them with some number between zero and the limit.  In order to use all the



data and to be conservative from the standpoint of effluent levels plants can
                                   F-5

-------
                                     TABLE  F-l

                         COMPARISON OF STANDARD  DEVIATIONS
                              ESTIMATED BY  TWO METHODS
METHOD
ORGANIC POLLUTANT
(8)
(10)

(21)

(23)

(25)
(31)
(44)
(59)
(64)
(65)

1 , 2 ,4-tr ichlorobenzene
1 , 2-dichloroethane

2 , 4 , 6 -t r ichlorophenol

Chloroform

1 , 2-dichlorobenzene
2,4-dichlorophenol
Methylene Chloride
2 , 4-dinitrophenol
Pentachlorophenol
Phenol

PLANT
P4
PI
P3
P3

PI

P4
P4
PI
P3
P3
P3
P5
LAB
8
9
1
4
3
3
6
8
1
4
8
9
9
1
6
-
-
-
Variance
Component
.95
.73
.84
2.20
2.32
2.26
1.31
1.50
.84
1.35
1.23
1.19
1.25
1.02
1.15
1.37
2.69
1.13
1.77
-
-
-
Daily
Average
.88
2.54
1.39

1.55

.92
1.54
2.12
1.07
1.80
1.48
1.25
.24
NOTE: The average standard deviation is given for the variance component
      method where there are estimates for more than one laboratory.
                                   F-6

-------
                                  TABLE F-l
                                 (concluded)
                                                                 METHOD
ORGANIC POLLUTANT
PLANT
LAB
Variance     Daily
Component   Average
(66)



(68)
(70)
(86)
Bis(2-ethylhexyl) Phthalate



Di-n-butyl Phthalate
Diethyl Phthalate
Toluene
P3



P3
P3
P3
3
6
8

3
3
3
1
2
1
1
1
1
1
.54
.34
.00
.63
.29
.52
.71



1
1
1
1



.50
.20
.65
.99
                                   F-7

-------
achieve, a replacement value equal to the detection limit was chosen.   For



example, suppose duplicate measurements on a sample resulted in Cl = 20 pg/1



and C2 = ND (not detected).   Setting C2 = 0 gives an average concentration of



C = 10 yg/1; setting C2 = 10 gives C^ = 15 yg/1.   Note that the use of 10



not only yields a higher average,  but results in counting the pollutant as



detected in the sample (with detected defined as C > 10).







C.  GOODNESS-OF-FIT TESTS



    The statistical distribution used to model the effluent data assumes that



X = log (C-D)  is NORMAL for C > D, where C is the daily effluent
             6



concentration and D is the analytical detection limit.  To assess the validity



of that assumption, goodness-of-fit tests were performed using the studentized



range test based on the statistic







                                   U = R/S,







with the range (R) and standard deviation (S) defined in A.  Critical values



of the U-test are given in Biometrika Tables (Pearson and Hartley, 1969).



An upper tail test was used to guard against alternative distributions with



heavier tails than the lognormal distribution:  if such alternatives were



appropriate, the lognormal distribution would tend to underestimate the 99th



percentile.







    A test was run using daily sample averages above the detection limit  for



each plant-pollutant data set.  The criterion for distribution rejection  was a



statistical significance level of  a = 0.01  for each test.  As the results
                                   F-8

-------
 in TABLE F-2 show, the model was rejected for only one of the 27 data sets


 tested  (lead at Plant 113).  The Agency concluded that the lognormal


 distribution is appropriate for modeling the data above the analytical


 detection  limit.






    For organic pollutants, a detection limit of D = 10 yg/1 was used; no


 metals readings were reported as being at or below a detection limit,


 therefore D = 0 was used.






 D.  DERIVATION OF VARIABILITY FACTORS


    To develop variability factors for each pollutant at each plant, the


 Agency assumed that the concentration C has a delta distribution modified to


 have its origin at D, the analytical detection limit (Aitchison and Brown,


 1957).  This assumption implies that a result under the detection limit has


 probability 6 of occurring, and x = log(C - D) for C > D is normally


                                      2
 distributed with mean y and variance o .   The 99th percentile value of


 the concentration is then
                             C0.99
with
                           = i"1 [(.99 - 6)/(l - 6)J ,
where f  (•) is the inverse of the standard normal cumulative


distribution function.  The mean and variance of C for C > D are
                                   F-9

-------
                                  TABLE F-2

                  GOODNESS-OF-FIT TESTS FOR VARIABILITY DATA
             LOG  (C - D)  FOR DAILY AVERAGES C OVER D yg/fc

(8)
(10)

(21)
(23)
(25)
(31)
(44)
(59)
(64)
(65)

(66)
(68)
(70)
(86)
(119)



(120)

(122)
(128)


(121)
POLLUTANT
1 , 2 ,4-trichlorobenzene
1,2-dichloroethane

2,4,6-trichlorophenol
Chloroform
1 , 2 -dichlorobenzene
2 ,4-dichlorophenol
Methylene chloride
2,4-dinitrophenol
Pentachlorophenol
Phenol

Bis(2-ethylhexyl) phthalate
Di-n-butyl phthalate
Diethyl phthalate
Toluene
Chromium



Copper

Lead
Zinc


Cyanide
*Critical values for the studentized









n U.99
3 2.00
4 2.44
5 2.80
6 3.10
7 3.34
8 3.54
10 3.88
11 4.01
PLANT
P4
PI
P3
P3
PI
P4
P4
PI
P3
P3
P3
P5
P3
P3
P3
P3
3
110
113
126
113
118
113
27
110
113
P5
range test
n
13
14
18
20
25
30
45
90
NDAY
11
7
7
18
14
6
5
13
7
4
3
4
26
10
24
10
46
8
90
26
145
27
13
158
8
140
27
(a =
U
4
4
4
4
5
5
5
6
U



























0.01
.99
.24
.34
.67
.80
.06
.26
.67
.27
3
2
2
3
3
2
2
4
3
2
1
2
3
3
3
3
3
3
3
5
5
5
4
6
2
6
4










.00
.73
.65
.18
.05
.48
.53
.23
.02
.44
.73
.00
.64
.79
.94
.41
.14
.25
.18
.01
.42
.18
.53
.01
.63
.07
.14
upper









TEST RESULT*
N.
N.
N.
N.
N.
N.
N.
N.
N.
N.
N.
N.
N.
N.
N.
N.
N.
N.
N.
N.
N.
N.
P <
N.
N.
N.
N.
tail)









S.
S.
S.
S.
S.
S.
S.
S.
S.
S.
S.
S.
S.
S.
S.
S.
S.
S.
S.
S.
S.
S.
0.01
S.
S.
S.
S.
are:









N.S. = not significant (U value below critical level).
Pearson and Hartley, 1969
                                   F-10

-------
and


                            o2 - e2v + °  (e°  - 1).              (3)

The Agency defined the daily variability -factor as
                                C            y + zo
                        VF(1) =  0.99 = D + e	             (4)

                                yc           y + 1/2 a2
                                        D + e
Estimates of the above quantities are calculated by replacing 6 by the

                                                        2
proportion of observations below D and replacing y and o  with the mean

and variance of log (C-D) for observations above D.
    To obtain the variability factor for a monthly mean C of 4 samples per

month, only results above the detection limit (i.e., C > D) were averaged.

The following assumptions were made:  C has a modified delta-lognormal

                                                                        2
distribution with the same mean as C and with variance proportional to ac

(Barakat, 1976), and measurements are uncorrelated.  The last assumption

implies that the probability of obtaining no results above D in the four

monthly samples for a month is
                                    64 = 6-                    (5)
The other assumptions give
                                   F-ll

-------
and
                                     W4 + Z4 °4
                        C0.95=D+e
with
                               -1 [(.95 - 5 )/(! - 6 )].
                                 L        4        4 J
z  = $   |(.95 - 5 )/(! - 6 )
The Agency defined the 4-day monthly variability factor as
                            F           V4 + Z4 °4
                    VF(4) =  0.95 = D + e	                (9)
                             ^        y^ + 1/2 02-

                                    D + e
                                                          Q
    To estimate VF(4), it is necessary to express y,  and aj- in terms


of 6, y, and o.  Since y— = y , it can be shown using (2) and
(6) that
                                        2    2
                              V4 = V +    "  4 .               (10)
           2                                              2
To relate o, to parameters of the original distribtuion, c— must be

                            2
expressed as a function of a .  When k out of 4 tests in a month are above
                            C

D (k > 0), the variance of C for that month is o^/k.  In addition, k
                                                O

varies randomly from month to month with probability distribution
             • (0-
                           PrlK = kl = (71(1 - 6)k 64"k
                                   F-12

-------
for k = 0, 1, 2, 3, 4 (K has a binomial distribution with parameter 1-6).


      2                                  2
Thus o_ is a weighted average of values a /k for different k:
      c                                  c
                           4


                        =  E  Pr(K=k)


                          k=l 1 - 64
                                     2    2
                          cfK~ 2u + a  , a    ...
                        = f(6)e p      (e   - 1)
with






                    f(6) = (1 - 64)     I   Pr(K = k)/k.

                                       k=l




Equating the expressions in (7) and (12) and simplifying with the aid of (10)



gives
                           = log
1 + f(6)(e°  - 1)  .
Equations (5), (10), and (13) now express the parameters 6,, u , and




 2                                                2
a,  in terms of the original parameters 6, y, and o .   Substituting




the values calculated earlier for these three parameters into the three



equations and substituting the results into equation (9) gives an estimate of



VF(4).
    For organic priority pollutants a detection limit of D = 10 ug/1 was



used in the model.  For metals and cyanide, no readings had been reported as



being at or below a detection limit.
                                   F-13

-------
E.  EXAMPLE OF VARIABILITY FACTOR CALCULATIONS


    Use of the above formulas to estimate variability factors is illustrated


below with data for 1,2-dichloroethane (10) from CMA plant 3.  To avoid


rounding errors and reproduce computer results, intermediate calculations were


carried out to several decimal places.  Measurements of 1,2-dichloroethane


were made on samples from 33 days, but the pollutant was detected on only 7


days.  The daily sample average values (C) and their corresponding values of


log  (C - D) are listed in TABLE F-3.






The  estimated mean and variance of x are then
                              A   _
                              u = x = 1.40442
and
                            a2 = s2 = 1.93184
                 _      2
(Definitions for x and s  are given under Formulas and Definitions).
The estimated probability of obtaining a daily sample average at or below the


detection limit is
                            6 =  26/33 =  0.787879,
so
                       z =  §"1(0.952857) =  1.67321.
                                    F-14

-------
                   TABLE F-3



VALUES OF C AND X FOR 1,2-DICHLOROETHANE RESULTS
Daily
Sample Average _
Concentration (C)
13
25.5
50
11
12
11
15
x = loge(C - 10)
1.09861
2.74084
3.68888
0
0.69315
0
1.60944
                    F-15

-------
Therefore, by formulas (1), (2), and (4), the estimated 99th percentile, mean,



and daily variability factor are
                          S0.99 ' 10 * °* + "
                               = 10
and
                        VF(1) = c/y  = 2.498
These results were rounded to 52, 21, and 2.50 and then entered into the



variability factor table.







     For the four day average variability factor, formula (5) gives
thus
                            6  = (26/33)4 = 0.385334;
                         z. = $"1(0.918655) = 1.39608.
                          4
                                   F-16

-------
Next, f(6) in (12) is estimated.  By  (11),
                                      Pr(K = k)
Thus
                        I                              I

                        | 1    463(1  - £)  = 0.414975  |
                        I                              I

                        | 2    662(1  - 6)2 = 0.167586  |
                        I                              I

                        | 3    4$  (1  - 6)3 = 0.030080  |
                        I                              I

                        | 4        (1  - £)4 = 0.002025  |
                       J	I
                      A         A  -1 4
                    f(6) =  (1  - 6  )  Z  Pr(K = k)/k =  0.828582.

                                    k=l
By formulas (10) and  (13) then,
 r     -
;[l + f(6)(«
                                          a
                          = logl + f(6)(e
                          = 1.77333
and
                      A    A
                         = 1.48368.



Using equations (8), (6), and  (9), respectively, the estimated  95th


percentile, mean, and variability factor for 4-day averages  are
                                  A      A
                    A             V4 + V4
                    CQ 95 = 10 + e*    ** = 38.3,


                                   F-17

-------
                               *4
                    y_ = 10 + e            =20.7,
and
                       VF(4) = c"rt OC/V_ = 1.850.
The variability factor was rounded to 1.85 and then entered into the summary



table.
F.  SUBCATEGORIZATION



    The data selection and reduction and statistical test, procedures employed



in the subcategorization analyses are described in this section.  The



wastewater characteristics examined were untreated influent concentrations of



all priority pollutants except pesticides and asbestos.







    Data from the Screening study were used for subcategorization because that



study provided the most comprehensive assessment on the presence of priority



pollutants at OCPSF plants (in terms of plant coverage and number of



pollutants per plant).  Untreated influent data were summarized as follows to



create one observation for each plant:
                                   F-18

-------
         •    Not detected, trace, and values under 10 yg/fc
              were replaced by 10.

         •    Since the Screening data was used, pollutant
              concentration levels at a plant were usually based on
              a single analysis measurement.  For plants where
              multiple analysis determinations were made, a sample
              average was generated for that pollutant.

         •    The value 10 yg/fc was inserted for any compound
              for which there was no measurement at a plant (i.e.,
              if a value was not reported for a pollutant, it was
              considered not detected).

         •    Natural logarithms of the resulting concentrations
              were computed.

The initial data base produced by the above process continued observations for

143 plants.
    Many priority pollutants were considered in the subcategorization

analysis--88 organic compounds and 14 metals plus cyanide.  Furthermore, the

correlations among measurements of different pollutants caused by common

analytical, sampling, and matrix effects made one-pollutant-at-a-time analyses

inappropriate.  Therefore, alternate multivariate analysis procedures were

considered.



    The classical multivariate technique for comparing the means of two

populations (e.g., two possible subcategories of plants) involves comparing an

F-statistic to tabled critical values of the F distribution with p and N1 +


N_ - p - 1 degrees of freedom, where p is the number of pollutants and N-


and ti  are the numbers of plants with data in the two groups (Morrison,


1967, p. 125-126).  It can be seen, therefore, that the number of plants with
                                   F-19

-------
measurements must exceed the number of pollutants measured in order to use




this technique; that is,
(since N- + N_ - p - 1 must be greater than zero).   There are pollutant





measurements on 143 plants in the Screening file, but it was necessary to use




the BPT Summary file to obtain other plant characteristics such as




product/processes employed.  Many of the plants in the Screening file could




not be identified or had incomplete information in the Summary file.  Thus




less than 143 plants could be used in statistical comparisons based on the




classical test.  For example, there are 14 Plastics-Only and 78 Not




Plastics-Only plants identifiable in the Screening file; there are 13




Organics-Only and 31 Mixed Organics/Plastics plants identifiable.  It can be




seen from these examples that it was not possible to include all 102 priority




pollutants of interest (88 organics and 14 metals/cyanide) in a single




multivariate comparison of groups of plants--splitting the pollutants into




groups would have been necessary.









    Another difficulty with using the classical multivariate test was the




analytical limitations of the Screening data.  These we11-documented




limitations made the use of a nonparametric procedure preferable, since such




procedures are based on less restrictive assumptions than the classical




multivariate procedure.  Unfortunately, the well-known nonparametric




procedures are univariate  (statistical analyses of only one variable at a




time).  To address these problems, another multivariate technique called
                                   F-20

-------
principal components was used to define a few new uncorrelated variables based


on the original pollutant variables, and the nonparametric test was applied to


the new variables.  The principal component analysis defined new variables as


weighted averages of the original pollutant-specific variables; weights were


selected to retain as much information as possible in the original data


(Morrison, 1967, p. 222-230).  Principal components were derived separately


for organics and metals/cyanide because their measurements are based on


different analytical methods; the derivation for organics is described below


(the derivation for metals was similar).
    For each plant, let X ,...., X   represent the original 88 organics
                         1        oo


variables (logs of mean concentrations of organic priority pollutants in the

                                                  _       2
acid, base/neutral, and volatile fractions).  Let X.  and s. represent the



mean and variance of the ith variable, and R = (r..)  the matrix of pairwise


                                    —    2
correlations among the 88 variables X., s., and r.. were computed from



the 143 plant-specific observations described above).  The first principal


component, Y , was defined as the weighted average
                            88          _                            (14)
                      Yl =
whose coefficients a., were chosen to make the sample variance
                      2     88  88

                     s.., =  Z   Z  a. na.,r . .
                      Yl   .=1 j=1  il jl ij
                                   F-21

-------
as large as possible given that
                               88
                               I   a.  = 1.
                              1=1   U
The second principal component was defined as the weighted average


                           88          _                                   (15)

                     Y2 = .^ *i2(Xi - V/Si

whose coefficients a   were chosen to make the sample variance
                      2     88  88
                     s   =  Z   I  a  a.0r..
                      Y2   1=1  =l  l2 j2 ^
as large as possible given that
                                88
and
                             88
                             I  a.,a.. = 0.
(The last condition makes Y- and Y_ uncorrelated.)  Additional principal


components were defined in similar fashion.  The weights for each component

were computed by the PRINCOMP procedure in SAS (SAS Institute, 1982, p.

347-361).  The value of the first principal component at a given plant was

obtained by substituting the log-mean concentrations for the 88 pollutants at

that plant for the X. in formula (14).  Plant-specific values of other
                                   F-22

-------
principal components were obtained from corresponding formulas for those

components.



    When a principal component analysis is based on the correlation matrix R
                                                                     2
as above, the total variation for all 88 components (the sum of the s *s)

                                                              2
equals the number of original variables, 88.  Thus the ratio s  /88


indicates the proportion of the total variation accounted for by the ith

component.  Because of the way principal components are defined, the

proportion of variation accounted for by successive components generally

decreases (and never increases).



    Principal components analysis has the following advantages as a

variable-reduction procedure:

                                    2
         •    It indicates through sy./88 how many components

              are needed to describe the data.

         •    The first few components summarize most of the
              information in the data when the original variables
              are highly correlated.

         •    The principal components themselves are
              uncorrelated so interpretation of statistical
              analyses based on them is straightforward.

         •    Principal components often have a physical meaning
              that can be identified from the magnitudes of the
              weights (a..).



For the organics Screening data, the first 5 components accounted for 74

percent of the total variation; for metals and cyanide the first five

components accounted for 78 percent of the total variation.  Morri-son suggests
                                   F-23

-------
that up to five principal components be retained for subsequent analysis if




those components account for at least 75 percent of the total variation.









    The weights defining the first five principal components for organics and




for metals/cyanide are shown in TABLES F-4 AND F-5, respectively.









    In the final stage of the statistical subcategorization analysis,  the




first five principal components were evaluated for each plant, and plants




belonging to groups of interest (e.g., Plastics-Only or Not Plastics-Only




producers) were identified using information from the BPT Summary file.




Plants not classifiable were excluded from the remainder of the analysis,




which consisted of using a normal-scores test (Bradley, 1968) to compare group




medians of principal component scores.









    Results of the comparison of Plastics-Only and Not Plastics-Only plants




are given in TABLE F-6.  Differences between the two groups were found for the




first and fifth organics components.  Based on an examination of the relative




magnitudes of the weights for individual components in Table F-4,  these two




components can be roughly interpreted as the average for all 88 compounds and




the average for benzene, chlorobenzene, ethylbenzene and toluene,




respectively.  The statistical test indicates that Not Plastics-Only plants




had higher median levels of these two weighted averages than the Plastics-Only




plants.









    A further analysis based on subdividing Not Plastics-Only plants into




Organics-Only and Mixed Organics/Plastics producers showed no significant
                                   F-24

-------
                  TABLE F-4



PRINCIPAL COMPONENT WEIGHTS FOR ORGAN ICS DATA
NAME
(001)
(002)
(003)
(004)
(005)
(006)
(007)
(008)
(009)
(010)
(011)
(012)
(013)
(014)
(015)
(016)
(017)
(018)
(019)
(020)
(021)
(022)
(023)
(024)
(025)
(026)
(027)
(028)
(029)
(030)
(031)
(032)
(033)
(034)
(035)
(036)
(037)
(038)
(039)
(040)
(041)
PRIN1
ACENAPHTHENE
ACROLEIN
ACRYLONITRILE
BENZENE
BENZIDINE
CARBON TETRACHLORIDE
CHLOROBENZENE
1 , 2, 4-TR I CHLOROBENZENE
HEXACHLOROBENZENE
1 2-DICHLOROETHANE
1 1, 1-TRICHLOROETHANE
HEXACHLOROETHANE
1 1-DICHLOROETHANE
1 1,2-TRICHLOROETHANE
1 1,2,2-TETRACHLOROETHANE
CHLOROETHANE
BIS (CHLOROMETHYL) ETHER
BIS (2-CHLOROETHYL) ETHER
2-CHLOROETHYLVINYL ETHER
2-CHLORONAPHTHALENE
2,4, 6-TR I CHLOROPHENOL
4-CHLORO-M-CRESOL
CHLOROFORM
2-CHLOROPHENOL
1 , 2-D I CHLOROBENZENE
1,3-DICHLOROBENZENE
1,4-DICHLOROBENZENE
3, 3-D I CHLOROBENZ I D I NE
1,1-DICHLOROETHYLENE
1 , 2-TRANSD I CHLOROETHYLENE
2,4-DICHLOROPHENOL
1 , 2-D I CHLOROPROPANE
1,3-DICHLOROPROPYLENE
2,4-DIMETHYLPHENOL
2,4-DINITROTOLUENE
2,6-DINITROTOLUENE
1 , 2-D I PHENYLHYDRAZ I NE
ETHYLBENZENE
FLUORANTHENE
4-CHLOROPHENYLPHENYL ETHER
4-BROMOPHENYLPHENYL ETHER
0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
11832
10254
09594
03579
11649
04990
02269
12806
12283
06166
07084
13167
10759
11434
09515
08960
10805
13682
10458
13611
08193
09946
02229
07882
11444
12127
10948
13667
08101
11179
07089
11051
09710
07025
13105
11739
12806
06442
12304
13420
13231
PR1N2
-0.
0.
0.
0.
-0.
0.
0.
-0.
-0.
0.
0.
-0.
0.
0.
0.
0.
0.
-0.
0.
-0.
0.
0.
0.
0.
-0.
-0.
-0.
-0.
0.
0.
0.
0.
0.
0.
-0.
-0.
-0.
0.
-0.
-0.
-0.
09204
03237
02801
02401
06185
14408
08494
07363
06556
14630
12300
07959
17180
19300
19678
17613
14920
07077
16754
06862
02875
04933
09740
05713
04583
02829
04410
07195
13390
20678
04118
19151
19114
05421
05846
05911
05186
03413
10152
07890
07321
0.
-0.
-0.
0.
-0.
0.
0.
-0.
-0.
0.
0.
0.
-0.
-0.
-0.
-0.
-0.
-0.
0.
-0.
-0.
-0.
0.
-0.
-0.
-0.
0.
-0.
0.
0.
-0.
-0.
0.
0.
-0.
-0.
-0.
0.
0.
-0.
-0.
PRIN3
12450
13206
14006
24430
00499
09154
01713
04961
00722
03189
06478
01439
05333
01635
00526
03963
04864
03315
04113
04357
14453
11297
18054
14389
02831
01400
00434
05525
14023
02071
07943
00915
07285
05740
06753
07384
05715
13828
14610
03595
06447

0.
-0.
-0.
-0.
-0.
-0.
-0.
-0.
0.
-0.
-0.
0.
-0.
-0.
-0.
-0.
-0.
-0.
-0.
-0.
0.
0.
0.
0.
-0.
-0.
0.
-0.
0.
-0.
0.
-0.
-0.
0.
-0.
-0.
-0.
0.
0.
-0.
-0.
PRIN4
02471
07823
07650
00345
02740
04663
00106
06440
03107
05613
01088
00687
06053
05458
04839
03809
08669
05069
02569
04806
29237
30597
06215
28065
07489
06128
03403
06190
04340
05852
34257
05173
04893
28435
06536
05341
02549
05917
03246
09384
07584
PRIN5
-0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
-0.
-0.
0.
-0.
-0.
-0.
0.
-0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
-0.
0.
-0.
-0.
-0.
0.
0.
-0.
0.
-0.
0.
0.
07431
15138
15403
39891
03294
11093
39068
07410
03824
02358
08441
01359
06081
12345
15969
08165
06753
00900
05771
00417
06094
02545
05912
06125
11233
04829
03100
02805
17501
08186
05122
06060
14428
06726
03616
04886
00964
26989
08005
02231
04262
                   F-25

-------
TABLE F-4 (concluded)
NAME
(042)
(043)
(044)
(045)
(046)
(047)
(048)
(049)
(050)
(051)
(052)
(053)
(054)
(055)
(056)
(057)
(058)
(059)
(060)
(061)
(062)
(063)
(064)
(065)
(066)
(067)
(068)
(069)
(070)
(071)
(072)
(073)
(074)
(075)
(076)
(077)
(078)
(079)
(080)
(081)
(082)
(083)
(084)
(085)
(086)
(087)
(088)
PRIN1
BIS-(2-CHLOROISOPROPYL) ETHER
BIS-(2-CHLOROETHOXY) METHANE
METHYLENE CHLORIDE
METHYL CHLORIDE
METHYL BROMIDE
BROMOFORM
D I CHLOROBROMOMETHANE
TR I CHLOROFLUOROMETHANE
D I CHLOROD I FLUOROMETHANE
CHLOROD I BROMOMETHANE
HEXACHLOROBUTAD I ENE
HEXACHLOROCYCLOPENTADI ENE
ISOPHORONE
NAPHTHALENE
NITROBENZENE
2-NITROPHENOL
4-NITROPHENOL
2,4-DINITROPHENOL
4, 6-D I N I TRO-0-CRESOL
N-N 1 TROSOD 1 METHYLAM 1 NE
N-N 1 TROSOD 1 PHENYLAM 1 NE
N-N 1 TROSOD I-N-PROPYLAMINE
PENTACHLOROPHENOL
PHENOL
BIS-(2-ETHYLHEXYL) PHTHALATE
BUTYLBENZYL PHTHALATE
DI-N-BUTYL PHTHALATE
DI-N-OCTYL PHTHALATE
Dl ETHYL PHTHALATE
DIMETHYL PHTHALATE
BENZO( A (ANTHRACENE
BENZO(A)PYRENE
3,4-BENZOFLUORANTHENE
BENZO(K)FLUORANTHENE
CHRYSENE
ACENAPHTHYLENE
ANTHRACENE
BENZO(GHI )PERYLENE
FLUORENE
PHENANTHRENE
D IBENZO( A, H) ANTHRACENE
INDENO(1,2,3-C,D)PYRENE
PYRENE
TETRACHLOROETHYLENE
TOLUENE
TRICHLOROETHYLENE
VINYL CHLORIDE
0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
12328
12994
01847
06459
11343
09996
10759
03985
10350
10936
13577
13372
12654
08261
10075
09850
09867
09247
11066
12811
13042
13280
10152
03146
07348
10984
09483
12487
11862
11160
12087
13441
13487
12990
11579
10319
09696
13456
11169
11080
13666
13549
11794
07083
03813
07514
10825
PRIN2
-0.
-0.
0.
0.
0.
0.
0.
0.
0.
0.
-0.
-0.
-0.
-0.
-0.
0.
0.
-0.
0.
-0.
-0.
-0.
0.
0.
-0.
-0.
-0.
-0.
-0.
-0.
-0.
-0.
-0.
-0.
-0.
-0.
-0.
-0.
-0.
-0.
-0.
-0.
-0.
0.
-0.
0.
0.
08636
05707
14937
14575
16426
16523
18494
18125
14501
19881
07686
07690
07552
08181
03826
04016
02423
03557
01715
10043
05853
08230
11060
04506
01975
08687
03585
05723
10368
08238
12152
05759
05981
08323
10256
10236
11007
07662
10541
06292
07228
05998
09883
12133
00456
18593
17387
-0
-0
0
-0
-0
-0
0
0
-0
-0
-0
-0
0
0
-0
-0
-0
-0
-0
-0
-0
-0
-0
0
0
0
0
0
0
0
0
0
-0
-0
0
0
0
0
0
0
-0
-0
0
0
0
0
-0
PR INS
.04923
.04904
.29997
.03850
.06482
.03763
.02639
.16554
.07459
.01253
.06010
.04000
.00808
.24327
.00322
.16553
.15526
.16634
.15425
.07234
.05274
.05791
.08187
.09045
.22260
.03570
.14928
.05483
.01156
.02932
.00108
.00831
.02084
.05720
.06777
.21682
.21446
.00658
.20816
.15200
.02773
.01665
.17964
.07433
.22582
.09676
.02209

-0.
-0.
0.
-0.
-0.
-0.
-0.
0.
-0.
-0.
-0.
-0.
0.
0.
-0.
0.
0.
0.
0.
-0.
-0.
-0.
0.
0.
0.
-0.
0.
0.
-0.
0.
-0.
-0.
-0.
-0.
0.
0.
0.
-0.
0.
0.
-0.
-0.
0.
0.
-0.
-0.
-0.
PRIN4
08711
07580
03189
08328
05632
03338
08996
00962
05124
05321
06901
09478
05459
11219
01309
26254
21177
21247
20787
08064
04155
08475
16777
18532
11881
06840
11303
00643
05015
02961
01091
08044
04020
03931
03394
10626
07784
07446
06221
02978
05851
05135
06655
03379
04796
02850
06305
PRIN5
0.
0.
0.
0.
0.
-0.
-0.
0.
0.
-0.
0.
0.
-0.
••0.
0.
0.
-0.
0.
-0.
0.
0.
0.
-0.
0.
0.
-0.
-0.
-0.
-0.
-0.
0.
-0.
-0.
0.
-0.
-0.
0.
-0.
-0.
-0.
-0.
-0.
-0.
0.
0.
-0.
-0.
02223
02963
07741
02434
06992
08045
13525
05837
06669
12406
04334
02735
04904
07097
07289
03919
01496
08969
03203
11704
05756
05837
06747
07148
04058
06570
12809
08868
09015
09997
07808
01869
02449
06108
10366
12002
01894
05279
08166
12882
03735
06193
11559
10503
28578
11590
11654
        F-26

-------
                     TABLE F-5
PRINCIPAL COMPONENT WEIGHTS FOR METALS/CYANIDE DATA

(lit)
(115)
(117)
(118)
(119)
(120)
(121)
(122)
(123)
(124)
(125)
(126)
(127)
(128)
NAME
ANTIMONY
ARSENIC
BERYLLIUM
CADMIUM
CHROMIUM
COPPER
CYAN I DE
LEAD
MERCURY
NICKEL
SELENIUM
S I LVER
THALLIUM
ZINC
PRINT
0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
30083
19453
27386
32574
23323
28649
04380
28694
24750
28106
28805
31248
31597
22166
0
0
0
0
-0
-0
0
-0
-0
-0
0
0
0
-0
PRIN2
.14570
.32669
.13534
.03418
.40820
.09643
.48968
.17496
.11203
.07280
.19861
.11945
.21691
.53631
PRIN3
-0.
0.
-0.
0.
0.
0.
0.
0.
-0.
0.
-0.
-0.
-0.
0.
06916
11624
18238
02977
31476
17821
67704
14908
42100
18551
18106
09996
20932
19460
0.
0.
-0.
-0.
0.
-0.
-0.
0.
-0.
-0.
0.
-0.
0.
0.
PRIN4
10133
61894
52114
21213
07162
04895
23871
07995
07369
05328
35473
25184
09984
10805

0.
-0.
-0.
-0.
0.
0.
0.
0.
0.
-0.
0.
-0.
0.
0.
PRIN5
23727
26333
06186
19271
03567
07541
38796
23695
51283
43498
15347
37689
01308
04248
                   F-27

-------
                            TABLE F-6

       COMPARISON OF PLASTICS-ONLY PLANTS WITH OTHER PLANTS
PRINCIPAL
COMPONENT
1
2
3
4
5
ORGANICS
Cumulative
% Variation
56
63
68
72
74
Significance
Level"
<.001
.520
.125
.445
<.001
METALS/CYANIDE
Cumulative
% Variation
49
58
66
73
78
Significance
Level*
.473
.338
.130
.757
.498
Based on the Terry-Hoeffding (normal scores) test comparing medians
for principal component score for Plastics-Only and Not Plastics-Only
plants.  There were 92 plants involved in the comparisons, 14
Plastics-Only and 78 Not Plastics-Only.
                             F-28

-------
differences (see TABLE F-7).  Likewise, no significant differences were found




among the three BPT subcategories for Not Plastics-Only (TABLE F-8).   These




analyses employed the same principal components as the Plastics-Only/Not




Plastics-Only comparison; they included all Screening plants that could be




identified as belonging to the groups of interest.
                                 F-29

-------
                            TABLE F-7

             COMPARISON OF ORGANICS-ONLY PLANTS WITH
                  MIXED ORGANICS/PLASTICS PLANTS
PRINCIPAL
COMPONENT
1
2
3
4
5
ORGANICS
Cumulative
% Variation
56
63
68
72
74
Significance
Level*
.717
.871
.502
.837
.738
METALS/CYANIDE
Cumulative
% Variation
49
58
66
73
78
Significance
Level*
.694
.550
.258
.948
.410
Based on the Terry-Hoeffding (normal scores) test comparing median of
principal component scores for Organics-Only and Mixed
Organics/Plastics plants.  There were 44 plants involved in the
comparisons, 13 Organics-Only and 31 Mixed Organics/Plastics.
                             F-30

-------
                                TABLE F-8

                  COMPARISON OF THREE BPT SUBCATEGORIES
                      FOR NOT PLASTICS-ONLY PLANTS*
PRINCIPAL
COMPONENT
1
2
3
4
5
ORGANICS
Cumulative
% Variation
56
63
68
72
74
Significance
Level**
.575
.705
.370
.122
.342
METALS/CYANIDE
Cumulative
% Variation
49
58
66
73
78
Significance
Level**
.710
.166
.822
.978
.270
 *  The 3 subcategories are Type I with Oxidation (27 plants), Type I
    without oxidation (8 plants), and Not Type I (9 plants).

**  Based on the normal scores test comparing medians of principal
    component scores for plants in the 3 subcategories (with 44 plants
    involved in the comparisons).  The test was run using PROC NPAR/WAY
    in SAS Institute (1982), pages 205-211, with the van der Waerden
    option.
                                 F-31

-------
                                 REFERENCES

AITCHISON, J., and J.A.C. BROWN.  1957.  The Lognormal Distribution, Cambridge
University Press, London, pp.  14-15, 95-96.

BARAKAT, R.  1976.  Sums of indepenent lognormally distributed random
variables.  Journal Optical Society of America 66: 211-216.

Biometrika Tables for Statisticians, Vol. 1, page 200.

BRADLEY, J.V.  1968.  Distribution-free Statistical Tests, Prentice-Hall,
Englewood Cliffs, NJ, 149-154, 326-330.

MORRISON, D.F.  1967. Multivariate Statistical Methods, McGraw-Hill, New York,
125-126, 222-230.

SAS INSTITUTE, INC.  1982.  SAS User's Guide:  Statistics, Gary, NC, 205-211,
347-361.

SEARLE, S.R.  1971.  Linear Models,  Wiley, New York, 473-474.
                                   F-32

-------
           APPENDIX G
CHEMICAL TREES OF THE GENERALIZED PLANT



       CONFIGURATIONS (GPCs)

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         APPENDIX H
HEALTH AND ENVIRONMENTAL EFFECTS




    OF PRIORITY POLLUTANTS

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                                APPENDIX H

                    HEALTH AND ENVIRONMENTAL EFFECTS OF
                            PRIORITY POLLUTANTS
A.  GENERAL

    This appendix presents a description of the toxic human health and
environmental effects associated with each of the 108 priority pollutants (see
Table VI-1) that the Agency is considering regulating with BAT, NSPS or
pretreatment standards.  The priority pollutants are listed in alphabetical
order by the fraction in which they appear -- volatile organic compounds, acid
extractable organic compounds, base/neutral extractable organic compounds,
metals and cyanide, and polychlorinated biphenyls.
B.  PRIORITY POLLUTANTS

    1.   Volatile Organic Compounds

    Acrolein

    Acrolein is a potent irritant of the eyes and nose in humans.  Effects
were observed within 5 minutes at levels of 0.58 mg/cu m (Albin 1962, as
reported in USEPA 1980).  Vapor concentrations of 23 mg/cu m were reported to
be lethal within a short time (Henderson and Haggard 1943, as reported in
USEPA 1980).  Strong skin irritation was reported to result from dermal
exposure to 10% acrolein in ethanol (Lacroix et al.  1976, as reported in
USEPA 1980).  In vitro studies have shown that acrolein is a potent
inhibitor of the synthesis of human polymorphonuclear leukocytes chemotaxis
(Bridges et al. 1977, as reported in USEPA 1980).  The odor threshold for
humans was reported to be 0.48 mg/cu m (Reist and Rex 1977, as reported in
USEPA 1980).

    Acute inhalation studies in rats, mice, rabbits, and guinea pigs have
shown pathological changes in the lungs including edema, hyperemia,
hemorrhages, and possible degenerative changes in the bronchial epithelium
(Skog 1980, Pattle and Cullumbin 1956, Salem and Cullumbin 1960, as reported
in USEPA 1980).  Hyperemia and fatty degeneration of the liver and focal
inflammatory changes in kidneys have been reported in rats administered lethal
subcutaneous doses of acrolein (Skog 1950, as reported in USEPA 1980).
Acrolein was reported to cause significant cardiovascular effects, including
tachycardia (Basu et al. 1972, as reported in USEPA 1980), and bradycardia,
and decreased blood pressure (Egle and Hudgins 1974, as reported in USEPA
1980).  In acute inhalation studies, acrolein was also found to increase
respiratory resistance in guinea pigs exposed to 0.92-2.3 mg/cu m for up to 12
hours (Murphy et al. 1963, as reported in USEPA 1980); to be cytotoxic to
the airway cells of hamsters exposed to 13.8 mg/cu m for 4 hours (Kilburn and
McKenzie 1978, as reported in USEPA 1980); to reduce mucus flow rates in cats
                                   H-l

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(dosage unspecified; Carson et al.  1966, as reported in USEPA 1980); and to
inhibit rabbit phagocytosis, adhesiveness, and calcium dependent ATPase
activity in in vitro tests (Low et al. 1977, as reported in USEPA 1980).

    In subacute inhalation tests, dogs and monkeys continuously exposed to
2.3-4.1 mg/cu m for 90 days subsequently developed eye and respiratory tract
irritation.  In the same study, dogs and monkeys exposed repeatedly to 8.5
mg/cu m for eight hours per day, five days per week, for six weeks developed
pathological changes in the lungs (squamous metaplasia and basal cell
hyperplasia of the trachea) (Lyon et al. 1970, as reported in USEPA 1980).
Hamsters, rats, and rabbits exposed by inhalation to 11.3 mg/cu m for 6
hours/day for 13 weeks showed signs of eye irritations, decreased food
consumption and decreased weight gain (Feron et al. 1978, as reported in
USEPA 1980).  Epithelial metaplasia and inflammation of the nasal cavity were
observed in a chronic toxicity study in hamsters exposed to 9.2 mg/cu m for 7
hours/day for 52 weeks (Feron and Kruysse 1977, as reported in USEPA 1980).
In a subacute oral toxicity study,  rats exposed to acrolein in drinking water
at concentrations up to 200 rug/liter for 90 days only showed slight weight
reduction at the highest level tested.  This effect was attributed to
unpalatability of drinking water (Albin 1972, as reported in USEPA 1980).
Acrolein has been shown to be mutagenic in different short-term bacterial
assays (USEPA 1980).  The carcinogenic potential of this compound has not yet
been established (USEPA 1980).

    The acute toxicity of acrolein on freshwater aquatic organisms is
reflected by static 96-hour LC50 values of 0.057-0.080 mg/liter in cladoceran
(mean acute value of 0.068 mg/liter for the species), 0.09-0.10 mg/liter in
the bluegill, and 0.16 mg/liter in the largemouth bass.  Aquatic macrophytes
were destroyed or badly scorched after one week of exposure to 25 mg/liter.
After 24-hour exposure to 10 mg/liter, 98% of adult snails and 100% of snail
embryos died.  In a total of nine short-term exposures with seven fish
species, acute toxicity values ranged from 0.046 to 0.115 mg/liter.  Flavor
impairment of rainbow trout flesh was reported to occur up to 4 days after a
4-hour exposure to 0.090 mg/liter (USEPA 1980).  Toxicity to the saltwater
eastern oyster was manifested by a 50% decrease in shell growth at 0.055
mg/liter using a flow through test.  Chronic toxicity was observed in
cladoceran at 21 yg/liter and the fathead minnow at 21 yg/liter.  The
effects of acrolein on fresh and saltwater plants have not been studied (USEPA
1980).

    EPA has established an ambient water quality criterion of 320 mg/liter for
the protection of human health from the toxic properties of acrolein ingested
through water and contaminated aquatic organisms.

    EPA has not yet established an aquatic life water quality criterion for
acrolein.
    Acrylonitrile

    Acrylonitrile is an acute poison that is a severe skin and eye irritant
 (NAS 1980).  Acute toxicity can cause nasal and respiratory oppressions,
vomiting, nausea, weakness, fatigue, headache, and diarrhea (Patterson et
                                   H-2

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al. 1976, as reported in USEPA 1980).  Occupational studies have associated
acrylonitrile with diseases of the peripheral nervous system, stomach,
duodenum, and skin (Goncharova et al. 1977, Shirshova et al. 1975 and
Stamov et al. 1976, as reported in USEPA 1980).  Other studies have shown
changes in the heart and circulation, blood methemoglobin content, and
clinical blood values; lowered blood cell counts; and mild liver injury
(Sakarai and Kusimto 1972, Ostrovskaya et al. 1976, Zotova 1975, and Shustov
and Mavrina 1975, as reported in USEPA 1980).

    Acrylonitrile has been characterized as a serious hazard in inhalation
studies (Union Carbide Corporation 1970, as reported in NAS 1980).  In one
study, all exposed rats died within 5 minutes while breathing saturated air;
in another study, all exposed rats died in 4 hours breathing 0.33 mg/liter.
Acute oral toxicity values for acrylonitrile range from 27 to 128 mg/kg for
mice (Benes and Cerna 1959, Zeller et al. 1969, as reported in NAS 1980) and
from 78 to 93 mg/kg for rats (Benes and Cerna 1959, Smyth and Carpenter 1948,
as reported in NAS 1980).

    A 90-day oral toxicity study, incorporating 0.66 and 0.99 mg/liter of
acrylonitrile in the drinking water of rats resulted in the animals'  death
before the end of the experiment (NRDC 1976, as reported in USEPA 1980).

    Rabbits and rats breathing 50 mg/cu m for 6 months developed changes in
peripheral blood patterns, functional disorders in the respiratory and
cardiovascular systems, and signs of neuronal lesions in the central nervous
system (Knobloch et al. 1972, as reported in USEPA 1980).

    Chronic inhalation exposures of dogs, cats, rats, guinea pigs, rabbits,
and monkeys to concentrations ranging from 0.12 mg/liter to 0.33 mg/liter
produced irritation of the eyes and nose, loss of appetite, gastrointestinal
disturbances, and incapacitating weakness of the hind legs (Dudley et al.
1942, as reported in NAS 1980).  Central nervous system effects also occurred
in inhalation studies of rats exposed to 80 ppm for one year (USEPA 1980).

    The mutagenicity of acrylonitrile has been demonstrated in the Salmonella
typhimurium test and in Escherichia coli W P2 strains.  Fetal malformations
and maternal toxicity were observed in rats administered 65 mg/kg/day by
gavage on days 6-15 of gestation.  Other embryotoxic effects included reduced
fetal body weight and crown-rump length and increased incidences of minor
skeletal variants.

    Acrylonitrile was carcinogenic in rats administered 100 or 300 mg/liter
for 12 months in the drinking water.   Cancer of the stomach, central nervous
system, and inner ear were reported (USEPA 1980).

    The toxicity of acrylonitrile to freshwater aquatic organisms was
demonstrated in the cladoceran, fathead minnow, guppy, and bluegill,  with
96-hour LC50 values ranging from 7.55 to 33.5 mg/liter.   The only information
on saltwater species is a 24-hour LC50 value of 24.5 mg/liter for the
pinfish.  No other data including the effects of aquatic plant life are
available (USEPA 1980).
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    EPA has established an ambient water quality criterion of zero for the
maximum protection of human health from the potential carcinogenic effects due
to exposure to acrylonitrile through ingestion of contaminated water and
contaminated aquatic organisms.  However, since the zero level may not be
attainable at the present time, a level of 0.058 yg/liter, corresponding to
an estimated lifetime incremental cancer risk of 0.000001, was recommended.

    EPA has not yet established an aquatic life water quality criterion for
acrylonitrile.
    Benzene

    Single exposure to benzene at 20,000 ppm has caused death within 5-10
minutes in humans and produced acute toxic effects including nausea,
giddiness, headache, unconsciousness, convulsions, and paralysis (Browning
1965 and Eckardt 1973, as reported in NAS 1977).  The chronic occupational
exposure of benzene to humans has been reported to produce thrombocytopenia,
leukopenia, and anemia.  In more severe cases of benzene hematoxicity,
pancytopenia and acute myeloblastic leukemia have been observed (USEPA 1980).
Increased incidence of chromosomal aberrations with aneuploidy and breakage
has been observed in nonsymptomatic workers exposed to benzene (NAS 1980).

    In chronic animal studies, leukopenia has been reported in rats exposed to
88 ppm, 7 hours per day, for up to 269 days.  Below this level, no blood
changes were observed in rats, guinea pigs and rabbits (Wolf et al. 1956, as
reported in USEPA 1980).  Other studies in which leukopenia developed include
a study in which rats were given 132 oral doses of 50 mg/kg over 6 months
(Wolf et al. 1956, as reported in USEPA 1980) and a study of rats exposed to
44 ppm for 5 hours/day, 4 days/week, for 5 to 7 weeks (Deichmann ejb al.
1963, as reported in USEPA 1980).  Abnormalities of the spleen and lungs were
observed in rats exposed to 31-47 ppm, 20 hours per week, for 6-31 weeks
(Deichmann et al. 1963, as reported in USEPA 1980).  Pregnant mice
administered 3 ml/kg gave birth to offspring with malformations and decreased
white cell counts (Watanabe and Yoshida 1970, as reported in USEPA 1980).  In
another study, mice administered 0.3-1.0 ml/kg benzene by gavage during days
6-15 of gestation developed significant maternal lethality and embryonic
resorptions (Nawrot and Staples 1979 as reported in USEPA 1980).  Inhalation
studies in rats conducted at various times before and during pregnancy, at
concentrations ranging from 210 mg/cu m to 1,000 mg/cu m produced no
malformations but did decrease fetal weight gain (USEPA 1980).  Benzene was
not mutagenic in the Salmonella/microsome in vitro assay (Lyon 1975, Shahin
1977, Simon et al. 1977, as reported in USEPA 1980).  However, it has been
reported that chromosomal abnormalities in bone marrow cells have resulted
from benzene exposure in a number of species including rats, rabbits, mice,
and amphibians (USEPA 1980).  Benzene-induced leukemogenesis has not been
demonstrated in laboratory animals  (USEPA 1980).

    A variety of freshwater organisms are sensitive to the affects of
benzene.  Static 96-hour LC50s have been reported in juvenile rainbow trout
(5.3 mg/liter), goldfish (34,42 mg/liter),  fathead minnow (33.47 rag/liter),
guppy  (36.6 mg/liter)> mosquitofish  (386 mg/liter), bluefish (22.5 lag/liter)
and Daphnia magna (203-620 nag/liter) .  A 5'0i reduction in the cell numbers
                                   H-4

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of Chlorella vulgaris was seen after 48 hours of exposure to 530 mg/liter
benzene.  Most saltwater organisms exposed to benzene gave 96-hour LC50 values
between 5 and 100 rag/liter.  Striped bass, anchovy, and pacific herring are
more sensitive species giving values between 5.8 and 25 rug/liter.  Saltwater
invertebrates appear to be less sensitive.  Female pacific herring exposed to
700 mg/liter for 48 hours exhibited reduced survival of embryos at hatching
and reduced survival of larvae through yolk absorption.  The 96-hour LC50
values ranged from 27 mg/liter for the grass shrimp to 450 rag/liter for the
copepod.  Chronic effects for saltwater organisms have not been studied.
Benzene concentrations of 20-100 mg/liter inhibited growth in three species of
algae (USEPA 1980).

    EPA has established an ambient water quality criterion of zero for the
maximum protection of human health from the potential carcinogenic effects due
to exposure to benzene through ingestion of contaminated water and
contaminated aquatic organisms.  However, since the zero level may not be
attainable at the present time, a criterion of 0.66 yg/liter, corresponding
to an incremental lifetime cancer risk of 0.000001, was recommended.

    EPA has not yet established an aquatic life water quality criterion for
benzene.
    Bromoform

    Bromoform is regarded as highly toxic to humans by all major routes of
exposure (lungs, GI tract, skin).  However, information concerning the
compound's toxicity in humans is not extensive.  Acute inhalation exposures
produce irritation of the respiratory tract, pharynx, and larynx, with
lacrimation and salivation.  Mild poisoning cases may be limited to headache,
listlessness, and vertigo.  In more severe cases, symptoms may include
unconsciousness, loss of reflexes, convulsions, and death resulting from
respiratory failure.  Histopathological findings include fatty, degenerative
and necrotic changes in the liver (USEPA 1980).  No information on chronic
toxicity in humans is available.

    In studies with the mouse, LD50s of 1,820 and 1,400 mg/kg were reported
following single subcutaneous and intragastric injections, respectively (USEPA
1980).  Single subcutaneous doses of 278 and 1,112 mg/kg bromoform resulted in
impaired liver function in the mouse (Kutob and Plaa 1962, as reported in
USEPA 1980), and 10 daily injections of 100-200 mg/kg/day produced liver and
kidney pathology in the guinea pig (NAS 1978, as reported in USEPA 1980).
Reticuloendothelial system function (liver and spleen phagocytic activity) was
suppressed in mice given intragastric doses of 0.3 to 125 mg/kg/day bromoform
(Munson et al. 1978, as reported in USEPA 1980).  Bromoform was shown to be
mutagenic in in vitro tests with three strains of Salmonella typhimurium
(Clayton and Clayton 1981).  Inconclusive evidence for potential carcinogenic
activity of bromoform has been reported by Theiss et al.  (1977, as reported
in USEPA 1980) using the strain A mouse lung tumor assay system.  Mice were
injected at doses of 4, 48, and 100 mg/kg 3 times/week for 6 to 8 weeks and
were sacrificed 24 weeks after the first injection.  A significant increase in
lung tumors was observed only at the middle dose, and a dose-response
relationship was not evident.  Epidemiological studies provide some evidence
                                   H-5

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for a positive association between trihalomethane levels in drinking water
supplies and the incidence of cancer.  The results of these studies are
limited, however, by inability to control for all confounding variables and
limited monitoring data (USEPA 1980).

    Acute aquatic toxicity for bromoform has been evaluated in two freshwater
species.  The 96-hour LC50 values reported for Daphnia magna and for the
bluegill were 46,500 and 29,300 yg/liter, respectively.  In studies with the
mysid shrimp and sheepshead minnow, 96-hour LCSOs were 24,400 and 17,900
ug/liter, respectively.  In an embryo-larval study with sheepshead minnow.,
chronic effects were observed at 6,400 yg/liter (USEPA 1980).  In freshwater
and saltwater algae, 96-hour EC50 values of 112,000 and 12,300, respectively,
were reported (based on effects in chlorophyll a) (USEPA 1980).

    EPA has established an ambient water quality criterion of zero for the
maximum protection of human health from the potential carcinogenic effects due
to exposure to bromoform through ingestion of contaminated water and aquatic
organisms.  However, since a zero level may not be obtainable at the present
time, a level of 0.19 yg/liter, corresponding to a lifetime incremental
cancer risk of 0.000001, was recommended.

    EPA has not yet established an aquatic life ambient water quality
criterion for bromoform.
    Carbon Tetrachloride

    Carbon tetrachloride produces acute, subacute, and chronic poisoning with
fatalities by ingestion, inhalation, and dermal routes in both humans and
animals.  In humans, carbon tetrachloride has been shown to cause liver arid
kidney damage (Dume et al. 1969 and Echardt 1965, as reported in NAS 1977).
Signs and symptoms of acute toxicity include dyspnea, cyanosis, proteinuria,
hematuria, jaundice, hepatomegaly, optic neuritis, ventricular fibrillation,
eye, nose, and throat irritation, headache, dizziness, vomiting, abdominal
cramps and diarrhea (NAS 1977).  Chronic exposures generally result in
gastrointestinal upset, such as nausea and vomiting, and nervous system
symptoms, such as headache, drowsiness, and excessive fatigue (Browning 1961,
as reported in NAS 1977).  Hepatic cirrhosis and necrosis, renal damage,
changes in blood enzymes, and increased serum bilirubin also result from
chronic exposure (Busuttil et al. 1972, Litchfield and Garland 1974, as
reported in NAS 1977).

    In a series of studies to evaluate the carcinogenic potential of carbon
tetrachloride, liver tumors were observed during lifetime exposures of mice,
hamsters, and rats using different routes of exposure:  hamsters were orally
administered 6.25-12.5 yl/week for 30 weeks (Della-Porta et al. 1961, as
reported in NAS 1977); mice were orally administered 0.1 ml, twice a week  for
20-26 weeks (Confer and Stenger  1965, as reported in NAS 1977), rats were
injected subcutaneously with 0.2-0.3 ml/100 g every two weeks (Kawasaki 1965,
as reported in NAS 1977) and rats were administered 1.3 ml/kg orally twice a
week for 12 weeks (Ruber and Glover 1967, as reported in NAS 1977).   However,
carbon tetrachloride was not found to be mutagenic or teratogenic (NAS  1977).
                                   H-6

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    Carbon tetrachloride produces acute and chronic toxic effects on
freshwater vertebrates and acute toxic effects on freshwater invertebrates.
The 96-hour LC50 values for bluegill were reported as 27.3 and 125 mg/liter.
A 48-hour LC50 value of 35.2 mg/liter was reported for Daphnia magna.  The
96-hour LC50 values reported for tidewater silversides and Limanda limanda
were 150 mg/liter and 50 mg/liter, respectively (USEPA 1980).

    EPA has established an ambient water quality criterion of zero for the
maximum protection of human health from the potential carcinogenic effects due
to exposure to carbon tetrachloride through the ingestion of contaminated
water and contaminated aquatic organisms.  However, since the zero level may
not be attainable at the present time, a level of 0.40 ug/liter,
corresponding to an estimated lifetime incremental cancer risk of 0.000001,
was recommended.

    EPA has not yet established an aquatic life water quality criterion for
carbon tetrachloride.
    Chlorobenzene

    Chlorobenzene has been identified as a respiratory irritant and a central
nervous system depressant in humans (NAS 1977).

    Chlorobenzene has an acute oral LD50 of approximately 3-3.4 mg/kg in rats
(Vecerek et al. 1976, as reported in USEPA 1980).  The rats died about 7
days after exposure and showed signs of many metabolic disturbances such as
elevated levels of serum glutamic-oxaloacetic transaminase (SCOT), lactase
dehydrogenase, alkaline phosphatase, blood urea nitrogen, and decreased levels
of glycogen phosphorylase and blood sugars.

    Chronic feeding studies administered in dogs and rats produced clinical
and pathological changes (Knapp et al.  1971, as reported in USEPA 1980).
DogS administered 272.5 mg/kg/day, by gavage, 5 days/per week for a period of
90 days, exhibited gross and/or microscopic pathological changes in the liver,
kidneys, gastrointestinal mucosa, and hematopoietic tissues.   Clinical
symptoms included an increase in immature leukocytes, low blood sugar,
elevated serum glutamic-pyruvic transaminase (SGPT) and alkaline phosphatase.
In chronic inhalation studies, rats, rabbits, and guinea pigs were exposed to
200, 475, and 1,000 ppm over 44 days (Irish 1963, as reported in USEPA 1980).
Histopathological changes in the lungs, liver, and kidneys occurred in the
high-dose group.  The middle dose group exhibited an increase in liver weight
and slight liver histopathology.  No effects were reported in the low dose
group.

    Chlorobenzene was administered orally to rats in daily doses of 14.4-228
mg/kg for a total of 137 doses over 192 days.  No blood or bone marrow changes
were observed (Irish 1963, as reported in USEPA 1980).  No studies have
evaluated the carcinogenic potential of Chlorobenzene, although an NCI
bioassay is in progress.

    The acute toxicity of Chlorobenzene to various saltwater and freshwater
species is reflected by LC50 values for cladoceran of 86 mg/liter, the
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goldfish, 51.6 mg/liter, the fathead minnow,  29.1-33.9 mg/liter,  the guppy,
45.3 mg/liter, the bluegill, 15.9-24.0 mg/liter,  and the sheepshead minnow,
10.5 mg/liter.  Chlorobenzene has also demonstrated acute toxic effects to
freshwater and saltwater algae with 96-hour EC50  values ranging from 22.4 to
34.1 mg/liter (USEPA 1980).

    EPA has established an ambient water quality  criterion of 488 yg/liter
for the protection of human health from the toxic properties of chlorobenzene
through ingest ion of water and contaminated aquatic organisms.   Using
available organoleptic data for controlling undesirable taste and odor of
ambient water, the estimated level is 20 yg/liter.

    EPA has not yet established an aquatic life water quality criterion for
chlorobenzene.
    Chlorodibromomethane

    No data are available on the toxicity of Chlorodibromomethane to humans,
animals, or aquatic organisms.

    EPA has not yet established ambient water quality criteria for
Chlorodibromomethane because of the lack of sufficient information.
    Chloroethane

    Of the chlorinated ethanes,  monochloroethane is considered to be one of
the least toxic.  It is known to disturb cardiac rhythm (Goodman and Gilman
1975, as reported in USEPA 1980) and overdoses can lead to severe contractile
failure of the heart (Doering 1975, as reported in USEPA 1980).  Exposure to
acute concentrations in humans has also been reported to cause neurologic
symptoms (including central nervous system depression, headache, dizziness,
incoordination, inebriation, and unconsciousness); abdominal cramps;
respiratory tract irritation and respiratory failure; and skin and eye
irritation.  As a halogen-containing hydrocarbon, chloroethane is potentially
toxic to the liver (USEPA 1980).

    In a series of acute inhalation studies in guinea pigs, exposure to two
percent chloroethane in air for 540 minutes produced histopathological changes
in liver and kidneys; exposure to four percent chloroethane for the same
period resulted in deaths.  When guinea pigs were exposed to 23-24 percent
chloroethane for five to ten minutes, unconsciousness and some deaths weres
reported (Sayers et al. 1929, as reported in Clayton and Clayton 1981).
Repeated two-hour exposures for 60 days to 5,300 ppm chloroethane was reported
to cause a decrease in the phagocytic activity of leukocytes, lowered hippuric
acid formation in the liver, and histopathological changes in the liver,
brain, and lungs (species tested not specified) (Troshina 1964, as reporter! in
Clayton and Clayton 1981).  In a study in which rats and dogs were exposed to
chloroethane at concentrations of 0, 1,600, 4,000, or 10,000 ppm for six
hours/day, five days/week for two weeks, the only observed effects were slight
liver weight increase in the 4,000 and 10,000 ppm male rats and CNS depression
                                   H-8

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in the high dose animals (Dow Chemical Company, unpublished data, as reported
in Clayton and Clayton 1981).

    No data on the toxicity of chloroethane to aquatic organisms are available.

    EPA has not yet established an ambient water quality criteria for
chloroethane because of the lack of sufficient data.
    2-Chloroethyl Vinyl Ether

    No toxicity data for 2-chloroethyl vinyl ether in humans are available,
and only limited acute toxicity information in animals has been published.
The acute oral LD50 in the rat has been given as 250 mg/kg, and the acute
dermal LD50 in the rabbit as 3,200 mg/kg (Smyth ejt al. 1949, as reported in
USEPA 1980) .   Toxic effects were observed in rats exposed to 250 ppm
2-chloroethyl vinyl ether vapor for four hours (Carpenter et al.  1949, as
reported in USEPA 1980).  No chronic studies for this compound have been
conducted.

    In an acute toxicity study with the bluegill, the 96-hour LC50 was
determined to be 354,000 ug/liter (USEPA 1980).  No toxicity data are
available for saltwater species.

    EPA has not yet established ambient water quality criteria for
2-chloroethyl vinyl ether because of the lack of sufficient data.
    Chloroform

    Chloroform has been reported to cause severe adverse effects on the human
body.  Acute effects via skin absorption include local irritation, hyperemia,
erythemia, and moisture loss (Malten et al. 1968, as reported in USEPA
1980); central nervous system depression and gastrointestinal irritation
(Challen et al. 1958, as reported in USEPA 1980) and hepatic and renal
damage (Fuhner 1923 and Althausen and Thoenes 1932, as reported in USEPA
1980).  Oral doses of 44.6 and 148.3 g have produced severe nonfatal
poisonings in humans; a dose of 296.6 g was fatal (Van Oettingen 1964, as
reported in NAS 1980).  Chronic effects in humans include central nervous
system depression, loss of appetite, hallucinations, ataxia, nausea, rheumatic
pain, and delirium (NIOSH 1974, as reported in USEPA 1980).

    Oral LDSOs have been estimated for male rats (0.8 ml/kg), mice (0.33
ml/kg), and dogs (1.0 ml/kg) (Kimura et al. 1971, Hill et al. 1975,
Klassen and Plaa 1966, as reported in NAS 1977).  Chloroform has been shown to
produce liver tumors after oral administration of 138 mg/kg for 78 weeks.  In
this same study, kidney epithelial tumors were observed when an average dose
level of 100 mg/kg was administered to rats by gavage for 78 weeks and
sacrificed at 111 weeks (NCI 1976, as reported in NAS 1977).  The fetuses from
rats exposed to 489 mg/cu m (100 ppm) of chloroform 7 hours/day during the 6th
to 15th day of gestation were reported to have an increased incidence in
several abnormalities which included acaudia, imperforate anus, subcutaneous
edema, missing ribs, and delayed ossification of sternebrae.  At an exposure
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of 147 mg/cu m (30 ppm) there was an increased incidence of delayed
ossification of skull bones and of wavy ribs (Schwetz 1974, as reported in
USEPA 1980).   Maternal toxicity was observed in pregnant rats given oral
chloroform doses of 126 mg/kg/day and greater.   Doses of 316 mg/kg/day and
greater caused acute toxic nephrosis and hepatitis and death of dams, as well
as fetotoxicity.  Oral doses of 100 mg/kg/day or higher were toxic to rabbits,
dams, and fetuses (Thompson et al. 1974, as reported in USEPA 1980).

    Ninety-six hour LC50 values for rainbow trout and bluegill were reported
as 43.8-66.8 mg/liter and 100-115 mg/liter, respectively.  Daphnia magna had
a 48-hour LC50 value of 28.9 mg/liter.  Anesthetization or death occurred at
concentrations between 97 and 207 mg/liter for stickleback, goldfish, and
orangespotted sunfish.  Teratogenesis was produced in 40 percent of the embryo
of rainbow trout exposed to 10.6 mg/liter for 23 days; 1.24 mg/liter produced
50 percent mortality of the embryo larval stage after a 27 day exposure.  A
96-hour LC50 for pink shrimp was reported as 81.5 mg/liter.  No other
information on marine organisms or on aquatic plant life is available (USEPA
1980).

    EPA has established a water quality criterion of zero for maximum
protection of human health from the potential carcinogenic effects due to
exposure to chloroform through ingestion of contaminated water and
contaminated aquatic organisms.  However, since zero may not be attainable at
the present time, a criterion of 0.19 yg/liter, corresponding to a lifetime
incremental cancer risk of 0.000001, has been recommended.

    EPA has not yet established an aquatic life water quality criterion for
chloroform.
    Dichlorobromomethane

    No information is available on human toxicity to dichlorobromomethane.  As
a halomethane, it is reported that the compound is "probably narcotic in high
concentrations" (USEPA 1980).

    In mice, the LDSOs for males and females administered dichlorobromomethane
by gavage is 450 and 900 mg/kg, respectively.  At doses between 500 and 4,000
mg/kg, histopathological examinations revealed fatty infiltration in livers,
pale kidneys, and hemorrhage in kidneys, adrenal glands, lungs, and brain
(Bowman et al. 1978, as reported in USEPA 1980).  Cambell (1978, as reported
in USEPA 1980) reported reduced water consumption and body weight in mice
given 300 mg/liter dichlorobromomethane in drinking water.  Cellular and
humoral immune responses were suppressed in mice exposed by gavage to 125
mg/kg/day of dichlorobromomethane for 90 days.  (Schuller et al. 1978, as
reported in USEPA 1980).  Suppression of hepatic phagocytic activity has also
been reported in mice (USEPA 1980).  Limited evidence for tertogenic
properties of dichlorobromomethane are presented in a study by Schwetz et
al. (1975, as reported in USEPA 1980), in which some fetal anomalies
(unspecified) were observed among mice exposed to vapors at 8,375 mg/cu m for
7 hours/day during gestation days 6 to 15.   Dichlorobromomethane was reported
to be mutagenic in an in vitro test with Salmonella typhimurium (Simmon
et al. 1977, as reported in USEPA 1980).  Inconclusive evidence for
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potential carcinogenic activity of dichlorobromomethane has been reported by
Theiss et al. (1977, as reported in USEPA 1980) using the strain A mouse
lung tumor assay system.  Mice were injected at doses of 20, 40, and 100
rag/kg, three times/week for 6 to 8 weeks and were sacrificed 24 weeks after
the first injection.  A marginally significant incidence of lung tumors was
observed only at the highest dose (p <0.067).

    No aquatic toxicity data are available for dichlorobromomethane.
Available data for halomethanes indicate that acute toxicity to freshwater
aquatic life occurs at concentrations as low as 11,000 yg/liter (USEPA
1980).

    EPA has established ambient water quality criterion of zero for maximum
protection of human health from the potential carcinogenic effects due to
exposure to dichlorobromomethane through the ingestion of contaminated water
and aquatic organisms.  However, since the zero level may not be attainable at
the present time, a level of 0.19 yg/liter, corresponding to a lifetime
incremental cancer risk of 0.000001, was recommended.

    EPA has not yet established an aquatic life water quality criterion for
dichlorobromomethane.
    1,1-Dichloroethane

    1,1-Dichloroethane has been shown to cause marked excitation of the heart,
central nervous system depression, respiratory tract irritation, and burning
skin in humans.  Liver injury was observed in experimental animals exposed to
4,000-17,500 ppm (species, route unspecified) (Sax 1975).  The oral LD50 for
the rat is 14 g/kg (Sax 1975).  Retarded fetal development occurred in rats
exposed to 24,250 mg/cu m (Schwetz et al. 1974,  as reported in USEPA 1980).
No information is available on the toxic effects of 1,1-dichloroethane on
aquatic organisms (USEPA 1980).

    EPA has not yet established ambient water quality criteria for
1,1-dichloroethane because of the lack of sufficient data.
    1,2-Dichloroethane

    In humans, 1,2-dichloroethane has been shown to produce central nervous
system depression, gastrointestinal upset, and systemic injury to the liver,
kidneys, lungs, and adrenals (USEPA 1979, as reported in USEPA 1980).
Accidental oral ingestion of a single dose of 0.5-1.0 g/kg resulted in death;
autopsy revealed liver necrosis and focal adrenal degeneration and necrosis
(Wirtshafter and Schwartz 1939, Yodaiken and Babcock 1973, as reported in
USEPA 1980).  Acute toxic effects include nausea, vomiting, dizziness,
internal bleeding, cyanosis, rapid but weak pulse, and unconsciousness.
Chronic exposure to 1,2-dichloroethane has been shown to cause neurological
changes, loss of appetite and other gastrointestinal problems, anemia,
irritation of the mucous membranes, liver and kidney impairment, and in some
cases death (NIOSH 1978, USEPA 1979, as reported in USEPA 1980).
                                   H-ll

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    Acute and subacute inhalation studies with dogs, rabbits, guinea pigs,
rats, and mice indicate that 1,2-dichloroethane is toxic to the liver, bone
marrow, blood, kidneys, myocardium, and sometimes the adrenals (Heppel et;
al. 1946, Liola et al. 1959, Liola and Fondacaro 1959, as reported in USEPA
1980).  Chronic inhalation exposures to 100-400 ppm 1,2-dichloroethane, for
5-32 weeks in the guinea pig, monkey, rabbit, dog, and cat were reported to be
toxic to the liver at concentration of 200 ppm and greater (Spencer et al.
1951, Hofman et al. 1971, as reported in USEPA 1980).  Increased liver
weights were observed in guinea pigs after a 32-week exposure to 100 ppm of
1,2-dichloroethane (Spencer et aj.. 1951, as reported in USEPA 1980).

    Exposure of female rats to 57 mg/cu m (4 hrs/day, 6 days/week) for 6
months before breeding and throughout gestation resulted in a reduction in
litter size, number of live births, and fetal weights (vozovaya 1974, as
reported in USEPA 1980).  1,2-Dichloroethane was found to be carcinogenic at
several sites to both rats and mice administered 50-300 mg/kg for 78 weeks by
gavage (NCI 1978, as reported in USEPA 1980).

    The acute toxic effects of 1,2-dichloroethane on freshwater organisms is
reflected in 96-hour LC50 values for the fathead minnow (118 mg/liter) and the
bluegill (431-550 mg/liter).  Toxic.ity to saltwater organisms was demonstrated
in the mysid shrimp at 113 mg/liter.  Chronic toxicity was observed in the
fathead minnow in concentrations ranging from 14 to 29 mg/liter.  Toxicity to
aquatic plants was observed in saltwater algae at concentrations ranging from
more than 126 mg/liter to more than 433 mg/liter (USEPA 1980).

    EPA has established an ambient water quality criterion of zero for the
maximum protection of human health from the potential carcinogenic effects
from exposure to 1,2-dichloroethane through ingestion of contaminated water
and contaminated aquatic organisms.  However, since the zero level may not be
attainable at present, a level of 0.94 yg/liter, corresponding to a lifetime
incremental cancer risk of 0.000001, was recommended.

    EPA has not yet established an aquatic life water quality criterion for
1,2-dichloroethane.


    1,1-Dichloroethylene

    The primary acute effect of 1,1-dichloroethylene is depression of the
central nervous system.  Animal studies have shown  1,1-dichloroethylene to
produce liver and kidney damage in the rat exposed to 189 mg/cu m (Prendergast
et al. 1967, as reported in USEPA 1980) and to produce cardiac sensitization
at high concentrations  (102,000 mg/cu m) for 10 minutes (Siletchnik and
Carlson 1974, as reported in USEPA 1980).  Pregnant rats exposed by inhalation
to 80-160 ppm on days 6 to  15 of gestation showed decreased weight gain,
decreased food consumption, and increased water consumption.  Increased liver
weight was observed at  160 ppm only.  In the offspring, there was a
significantly increased incidence of skeletal alterations at 80 and 160 ppm.
In the same study, rabbits exposed to 160 ppm on days 6 to 18 days of
gestation had an increase in resorptions in the dams; in the offspring, a
significant increase  in several minor skeletal variations was observed  (Murray
et al. 1979, as reported in USEPA 1980).  Kidney adenocarcinomas were
                                   H-12

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produced in Swiss mice exposed to 100 mg/cu m, 4 hours per day, 4 to 5 days
per week for 52 weeks (Maltoni et al. 1977, as reported in USEPA 1980).  In
another study, a small increase in hepatic hemangiosarcomas was observed in
mice exposed to 220 mg/cu m by inhalation 6 hours/day 5 days per week for 7-12
months (Lee et al. 1972, as reported in USEPA 1980).  No effect was observed
in rats exposed to 200 mg 1,1-dichloroethylene in drinking water for two years
or to 100 and 300 mg/cu m by inhalation, 6 hours per day, 5 days per week for
18 months (Rampy et al. 1977, as reported in USEPA 1980).  An NCI bioassay
is currently in progress (USEPA 1980).  1,1-Dichlorethylene, which has a
structure similar to vinyl chloride monomer (a known liver carcinogen in
several species including humans), is also suspected of being a human
carcinogen.

    Acute toxicity of 1,1-dichloroethylene on freshwater aquatic fish life is
reflected by 96-hour LC50 values for the fathead minnow of 169 mg/liter and
for the bluegill of 73.9 mg/liter.  Furthermore, the toxicity of this compound
increases with increasing chlorine content.  The 48-hour LC50 value for
Daphnia magna was reported as 11.6 mg/liter.  The 96-hour LC50 values were
reported in the sheepshead minnow to be 249 mg/liter, the tidewater
silversides 250 mg/liter, and the mysid shrimp 224 mg/liter.  No information
is available on the chronic effects of 1,1-dichloroethylene on aquatic
organisms (USEPA 1980).

    EPA has established an ambient water quality criterion of zero for the
maximum protection of human health from the potential carcinogenic effects due
to exposure to 1,1-dichloroethylene through ingestion of contaminated water
and contaminated aquatic organisms.  However, since the zero level may not be
attainable at present, a level of 0.33 yg/liter, corresponding to a lifetime
incremental cancer risk of 0.000001, was recommended.

    EPA has not yet established an aquatic life water quality criterion for
1,1-dichloroethylene.
    1,2-Dichloropropane

    Acute toxic effects reported in humans include vertigo, lacrimation,
irritation of the mucous membrane, and changes in the blood (St. George 1937,
as reported in USEPA 1980).  Death has been reported after ingestion of a
50-ml solution containing 1,2-dichloropropane (Larcan et al. 1977, as
reported in USEPA 1980).

    The oral administration of 5,700 mg/kg of 1,2-dichloropropane in dogs
produced staggering and loss of coordination in 15 minutes, complete lack of
coordination in 90 minutes, and death in 3 hours.  Congestion of the lungs,
kidney, and bladder was reported along with hemorrhage of the stomach and
respiratory tract.  Liver and kidney damage was also produced (Wright and
Schaffer 1932, as reported in USEPA 1980).  Inhalation exposure to 400 ppm for
7 hours/day for 128-140 days was reported to cause slight fatty degeneration
of the liver in mice, but no effects were observed in rats similarly exposed
(Heppel et al. 1948, as reported in USEPA 1980).  1,2-Dichloropropane is
mutagenic in the Salmonella typhimurium assay (DeLorenzo et al. 1977, as
reported in USEPA 1980).  Chromosomal aberrations in rat bone marrow were
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reported (Dragusanu and Goldstein 1975, as reported in USEPA 1980).  No
information is available on the carcinogenicity of 1,2-dichloropropane in
animals (USEPA 1980).

    The acute toxicity of 1,2-dichloropropane in freshwater aquatic organisms
was demonstrated in cladoceran, fathead minnows, and bluegill; 96-hour LD50
values were 52.5, 139.3, and 280-320 mg/liter, respectively.  Tidewater
silverside, a saltwater organism, was affected with an LC50 of 240 mg/liter.
Growth inhibition of sheepshead minnow was observed after exposure to 164
mg/liter for 33 days.  Chronic toxicity was reported in the fathead minnow in
concentrations ranging from 6 to 11 mg/liter.  No information is available on
the toxic effects on aquatic plant life (USEPA 1980).

    EPA has not yet established ambient water quality criteria for
1,2-dichloropropane because of the lack of sufficient data.


    1,3-Dichloropropylene

    No information is available on the toxic effects in humans.   Daily oral
doses of up to 2.5 mg/kg of 1,3-dichloropropylene for six months caused an
increase in trypsin activity, a decrease in trypsin inhibitor, an increase in
blood lipase activity, and a decrease in amylase (Strusevich and Ekshtat 1974,
as reported in USEPA 1980).  Daily oral doses of 2.2 and 55 mg/kg/day for 30
days resulted in changes in the liver function of rats (Kurysheva and Ekshtat
1975, as reported in USEPA 1980).  Oral LD50 values for the rat of 140 mg/kg
and the mouse of 300 mg/kg and an LC50 for the rat and mouse of 4,530 mg/cu m
were reported (Hine et al. 1953, as reported in USEPA 1980).
1,3-Dichloropropylene was mutagenic in the Salmonella typhimurium assay
(DeLorenzo et al. 1977, as reported in USEPA 1980).  The carcinogenic
potential of 1,3-dichloropropylene has not been established, although an NCI
bioassay is in progress.

    Acute toxicity of 1,3-dichloropropylene in freshwater aquatic organisms is
reflected by 96-hour LC50 values in the cladoceran and the bluegill of 6.15
and 6.06 mg/kg, respectively.  Acute toxicity to saltwater organisms occurred
in the mysid shrimp and sheepshead minnow with LC50 values of 0.79 and 1.77
mg/liter, respectively.  Chronic toxicity was observed in the fathead minnow
in concentrations ranging from 180 to 330 yg/liter.  Acute toxic effects on
fresh- and saltwater algae were reported at 4.95 and 1.0 mg/liter,
respectively (USEPA  1980).

    EPA has not yet established water quality criteria for
1,3-dichloropropylene because of the lack of sufficient data.
    Ethylbenzene

    Although ethylbenzene has a wide environmental distribution,  little
information is available on  its biological effects (USEPA  1980).  It has been
shown to persist in man for  days after exposure  (USEPA  1980).  Men exposed to
4.35 mg/liter in the air experienced eye  irritation, which diminished  in
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intensity on continued exposure.  At a concentration of 21.75 mg/liter,
however, the irritation to eye and nasal membranes was intolerable (Patty
1963).

    In a 6-month study on rats, daily single oral doses of ethylbenzene were
found to produce histopathological changes in the kidney and liver (Wolf et
al. 1956, as reported in USEPA 1980).  No data are available on the
teratogenicity, mutagenicity, or carcinogenicity of ethylbenzene (USEPA 1980).

    Among freshwater animal species, the 96-hour LC50 ranged from 32 mg/liter
in the bluegill to 97.1 mg/liter in the guppy.  The 48-hour EC50 value in
Daphnia magna is 75 mg/liter.  The 96-hour LC50s in saltwater invertebrates
are 3.7 mg/liter for the bay shrimp, 87.6 mg/liter for the mysid shrimp and
1,030 mg/liter for the pacific oyster.  In saltwater fish, the 96-hour LC50
for striped bass was 0.43 mg/liter, but it was 275 mg/liter for the sheepshead
minnow.  The variability in fish and invertebrate data may be due to
difficulties in testing ethylbenzene in saltwater.  No adverse effects were
observed in aquatic plants exposed to ethylbenzene (USEPA 1980).

    EPA has established an ambient water quality criterion of 1.4 mg/liter for
the protection of human health from the toxic properties of ethylbenzene
ingested through water and contaminated aquatic organisms.

    EPA has not yet established an aquatic life water quality criterion for
ethylbenzene.
    Methyl Bromide

    Methyl bromide is a central nervous system depressant and is regarded as
highly toxic to humans.  Acute fatal intoxication can result from inhalation
of vapors at concentrations as low as 1,164 to 1,552 mg/cu m, and harmful
effects can occur at 388 mg/cu m (USEPA 1980).  Minor poisoning episodes may
be limited to mild neurological and GI disturbances, with recovery in a few
days.  More severe cases may involve visual and speech disturbances,
incoordination, tremors developing to convulsions, and psychic disturbances.
Neurological disorders may be persistent.  Death may result from pulmonary
edema or circulatory failure, and pathological changes often include
hyperemia, edema, lung and brain inflammation, and degenerative changes in the
kidneys, liver, and stomach (Doull et aj.. 1980, and USEPA 1980).  Skin
contact with methyl bromide may produce prickling, cold sensation, erythema,
vesication, blisters, damage to peripheral nerve tissue, and permanent brain
damage (USEPA 1980).

    Methyl bromide is also neurotoxic to animals.  Exposure to 846 to 997
mg/cu m for 22 to 26 hours was lethal to rats  (Irish et al. 1940, as
reported in USEPA 1980).  A 3-hour exposure to 846 mg/cu m and a 13.5-hour
exposure to 1,164 mg/cu m were lethal to rabbits and guinea pigs, respectively
(von Oettingen 1964, as reported in USEPA 1980).  In rabbits, 128 mg/cu m for
8 hours/day, 5 days/week resulted in lung irritation and paralysis (Irish et
al. 1941, as reported in USEPA 1980).  Dogs receiving methyl bromide by
ingestion (fumigated diet yielding residual bromide at a dose level of 150
mg/kg/day) were adversely affected (Rosenblum et al. 1960, as reported in
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USEPA 1980).  Subcutaneous administration of methyl bromide (in oil) to
rabbits at 20-120 mg/kg caused paralysis, cessation of drinking, and reduced
urine excretion (Kakizaki 1967, as reported in USEPA 1980).  Cattle fed methyl
bromide fumigated hay (resulting in bromide ion concentrations of 6,800 to
8,400 mg/liter) developed signs of CNS toxicity (motor incoordination) at 10
to 12 days of exposure (Knight and Reina-Guerra 1977, as reported in USEPA
1980).   Bromomethane was reported to be mutagenic in an in vitro test with
Salmonella typhimurium (Simmon et al.  1977, as reported in USEPA 1980).
No chronic studies of methyl bromide toxicity are available.

    For methyl bromide,  the 96-hour LC50 value for the bluegill, a freshwater
species, is 11,000 ug/liter and for the tidewater silverside,  a saltwater
species, is 12,000 yg/liter (USEPA 1980).  No chronic toxicity data for
aquatic organisms are available.

    EPA has established ambient water quality criterion of zero for maximum
protection of human health from the potential carcinogenic effects due to
exposure to methyl bromide through the ingestion of contaminated water and
aquatic organisms.  However, since the zero level may not be attainable at the
present time, a level of 0.19 yg/liter, corresponding to a lifetime
incremental cancer risk of 0.000001, was recommended.

    EPA has not yet established an aquatic life water quality criterion for
methyl bromide.
    Methyl Chloride

    Methyl chloride is not generally regarded as highly toxic in humans,
although numerous instances of poisonings have been reported.  Serious or
prolonged exposures may occur because of methyl chloride's odorless and
colorless properties, low irritancy, and characteristic latency of effect
(USEPA 1980).  Methyl chloride acts principally as a central nervous system
depressant.  In persons exposed to levels ranging from 52 to more than 20,000
mg/cu m, the following toxic symptoms have been reported:  blurred vision,
headache, nausea, loss of coordination, and personality changes, lasting from
hours to days (USEPA 1980).  Severe poisonings are characterized by a latent
period followed by serious neurological disorders which may be persistent.
Renal and hepatic injury are common.  Coma and death may result from cerebral
and pulmonary edema and circulatory failure (USEPA 1980).  No other chronic
effects have been reported, although no epidemiological studies of populations
exposed to methyl chloride have been reported.

    In acute inhalation studies in animals, methyl chloride has produced
severe neurological disturbances.  The LC50 value for the mouse was 6,500
mg/cu m following a six-hour inhalation exposure (Davis et al.  1977, as
reported in USEPA 1980).  Permanent muscular dysfunction was reported in mice
surviving several weeks of daily six-hour exposures at 1,032 mg/cu m, and
paralysis followed exposure to 531 mg/cu m for 20 hours (von Oettinger et
al. 1964, as reported in USEPA 1980).  In dogs and monkeys, signs of
poisoning were observed after one six-hour exposure to 1,032 mg/cu m.  Daily
exposure of dogs to this concentration for 2 to 4 weeks led to some deaths and
permanent neuromuscular damage in survivors (von Oettinger 1964, as reported
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in USEPA 1980).  Under prolonged exposures to less severe levels, methyl
chloride increased mucus flow in cats (Weissbecker et. al. 1971, as reported
in USEPA 1980).

    Little aquatic toxicity data are available for methyl chloride.  Dawson
et al. (1977, as reported in USEPA 1980) reported 96-hour LC50 values for
the bluegill (a freshwater species) and the tidewater silverside (a saltwater
species) of 550,000 and 270,000 yg/liter, respectively.  Data on the general
class halomethanes indicate that acute toxicity may occur at levels as low as
11,000 yg/liter (USEPA 1980).  No data on toxic effects to aquatic plants
are available.

    EPA has established an ambient water quality criterion of zero for the
maximum protection of human health from the potential carcinogenic effects due
to exposure to methyl chloride through ingestion of contaminated water and
aquatic organisms.  Since the zero level may not be attainable at the present
time, a level of 0.19 yg/liter, corresponding to a lifetime incremental
cancer risk of 0.000001, was recommended.

    EPA has not yet established an aquatic life water quality criterion for
methyl chloride.


    Methylene Chloride

    The acute toxic effects of methylene chloride on humans include decreased
psychomotor performance (Winneke 1974, as reported in USEPA 1980), central
nervous system dysfunctions and irritation of the mucous membranes (eyes,
respiratory tract, and skin) (NAS 1978, as reported in USEPA 1980).  Mild
poisoning produces somnolence, lassitude, anorexia, and mild lightheadedness.
Fatal poisonings have resulted from cardiac injury and heart failure (NAS
1978, citing Hughes 1954, Stewart and Hake 1976, Collier 1936, Moskowitz and
Shapiro 1952, as reported in USEPA 1980).  Upon metabolism, methylene chloride
will form carbon dioxide, which will increase carboxyhemoglobin levels in the
blood and interfere with oxygen transfer and transport (USEPA 1980).

    Central nervous system functional disturbances were produced in animal
studies in which rats were exposed for 3 hours to 1,740 mg/cu m (Fodor and
Roscovanu 1976, as reported in USEPA 1980).  Liver changes were reported in
mice continuously exposed for up to 2 weeks to 87-347 mg/cu m (NAS 1978 citing
Haun et al. 1972, as reported in USEPA 1980).  Conjunctivitis, blepharitis,
corneal thickening, keratitis, and iritis were observed in rabbits (Ballantyne
et al. 1976, as reported in USEPA 1980).  Fetotoxicity and embryotoxicity
were reported in mice and rats exposed to 4,340 mg/cu m for 7 hours on day 9
of gestation (Schwetz et al. 1975, as reported in USEPA 1980).

    Methylene chloride was reported to be mutagenic in the Salmonella
typhimurium assay.  No information on the carcinogenicity of methylene
chloride in animals or humans is available (USEPA 1980).

    The acute toxic effects of methylene chloride on freshwater aquatic
organisms have been studied.  96-Hour LC50 values were determined for Daphnia
magna (224 mg/liter), fathead minnow (193 mg/liter), and bluegill (224
                                   H-17

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mg/liter).  Among saltwater species, mysid shrimp have reported 96-hour LC50
values of 256 mg/liter; sheepshead minnows, 331 mg/liter; and tidewater
silverside, 270 mg/liter.  No information on the chronic toxicity of methylene
chloride on aquatic organisms is available.  Toxicity to both freshwater and
saltwater algae was reported to occur in concentrations greater than 662
mg/liter (USEPA 1980).

    EPA has established an ambient water quality criterion of zero for the
maximum protection of human health from the potential carcinogenic effects due
to exposure to halomethanes including methylene chloride through the ingestion
of contaminated water and contaminated aquatic organisms.  However, since the
zero level may not be attainable at the present time, a level of 0.19
yg/liter corresponding to a lifetime incremental cancer risk of 0.000001 was
recommended for all the halomethanes including methylene chloride.

    EPA has not yet established an aquatic life water quality criterion for
methylene chloride.


    1,1,2,2-Tetrachloroethane

    A number of cases of human poisonings from occupational exposure to
1,1,2,2-tetrachloroethane have been reported.  Frequently noted symptoms
include vomiting, nausea, gastric pain, headache and dizziness, and in some
cases death resulting from central nervous system (CNS) depression.  Chronic
exposure can result in hepatotoxic and CNS effects (ACGIH 1981, USEPA 1980).
In two occupational studies, hepatic injury and leukopenia were reported in
workers exposed to concentrations of 1,1,2,2-tetrachloroethane between 1.5 and
247 ppm for three years, and nervous complaints and gastric symptoms were
present in workers exposed to concentrations between 9 and 98 ppm (Jeney ejb
al. 1957, Lobo-Mendoca 1963, as reported in ACGIH 1981).  Cases of human
deaths have also resulted from accidental or intentional
1,1,2,2-tetrachloroethane ingestion (USEPA 1980).

    Acute inhalation exposure of rats and mice to 1,1,2,2-tetrachloroethane
produced anesthesia, fatty degeneration of the liver, tissue congestion, and
death; exposures in these studies ranged from 5,900 ppm  (three hours) to
11,400 ppm (six hours for two days).  A three-hour exposure of mice to 600 ppm
resulted in increased hepatic triglycerides and total lipids and decreased
hepatic energy stores (Tomokuni 1969, as reported in USEPA 1980).  Intravenous
or intraperitorieal injection of 0.7 ml (total dose administered in five doses
over 14 days) in guinea pigs caused weight loss, convulsions, death, and fatty
degeneration of the liver and kidney (Muller 1932, as reported in USEPA
1980).  Injection of 200 mg/kg was  lethal to mice in seven days (Natl. Res.
Counc. 1952, as reported in USEPA 1980).

    Chronic inhalation exposure of  rabbits to 1,1,2,2-tetrachloroethane at
14.6 ppm, 4 hours/day for 11 months induced liver and kidney degeneration
(Navrotskiy et al. 1971, as reported in USEPA 1980).  White blood cell
count, pituitary adrenocorticotropic hormone, and fat content of the liver
were affected in rats exposed by inhalation to 1.94 ppm, 4 hours/day for up to
265 days  (Deguchi  1972, as reported in USEPA 1980).  Monkeys exposed to 1,000
or 4,000 ppm, 2 hours/day for 190 days developed marked  vacuolation of the
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liver (Horiguchi et al. 1962, as reported in USEPA 1980).  A National Cancer
Institute bioassay was conducted for 1,1,2,2-tetrachloroethane in which male
and female mice received time-weighted average doses of 142 and 282 mg/kg/day
by stomach tube for 78 weeks (NCI 1978,  as reported in USEPA 1980).  The
incidence of hepatocellular carcinomas in both male and female mice was
positively correlated  (p <0.001) with dosage level.  In male and female rats
given time-weighted average doses of 62 and 108 mg/kg/day (males) and 43 and
76 mg/kg/day (females) for 78 weeks, the incidence of neoplasms was not
statistically significant.  1,1,2,2-Tetrachloroethane was shown to be
moderately mutagenic in in vitro assays with Salmonella typhimurium and
E. coli (USEPA 1980).

    In freshwater species, LD50 values of 9,320-23,900 yg/liter have been
reported for the cladoceran, 20,300 ug/liter for the fathead minnow, and
19,600-21,300 yg/liter for the bluegill.  In an embryo-larval study of
fathead minnow, chronic toxicity was observed at 2,400 yg/liter (USEPA
1980).  Acute toxicity in saltwater species of 1,1,2,2-tetrachloroethane was
reported for mysid shrimp and sheepshead minnow with LD50 values of 9,020 and
12,300 lag/liter, respectively (USEPA 1980).  No chronic studies in saltwater
species were available.  In 96-hour EC50 tests with freshwater and saltwater
algae using chlorophyll a and cell number as measured responses, toxic
effects were observed at concentrations of 136,000-146,000 and 6,230-6,440,
respectively (USEPA 1980).

    EPA has established an ambient water quality criterion of zero for the
maximum protection of human health from the potential carcinogenic effects due
to exposure to 1,1,2,2-tetrachloroethane through ingestion of contaminated
water and aquatic organisms.  However, since the zero level may not be
attainable at the present time, a level of 0.17 ng/liter, corresponding to a
lifetime incremental cancer risk of 0.000001, was recommended.

    EPA has not yet established an aquatic life water quality criterion for
1,1,2,2-tetrachloroethane.


    Tetrachloroethylene

    The acute effects of tetrachloroethylene on humans are dominated by
central nervous system depression.  Lassitude, mental fogginess, and
exhilaration were observed in human volunteers exposed to 6,258 mg/cu m for 95
and 130 minutes (Carpenter 1937, as reported in USEPA 1980).  When-this
concentration was raised to 10,000 mg/cu m signs of inebriation were observed
and, at 13,400 mg/cu m, all volunteers were forced to leave the chamber within
7.5 minutes.  Minimal effects on the central nervous system were observed on
volunteers exposed to 1,300 mg/cu m (Rowe et al. 1952 and Stewart et al.
1961, as reported in USEPA 1980).  Irritation of the mucous membranes have
also been reported (NAS 1980).  Mild to severe hepatotoxicity was observed in
several instances following inhalation of tetrachloroethylene (dose and
duration unspecified; Hake and Steward 1977; Salund 1967; Stewart et al.
1961; Stewart 1969; Meckler and Phelps 1966, as reported in NAS 1980).  No
consistent neurological changes were reported in a study of 12 volunteers
exposed to 168 and 670 mg/cu m tetrachloroethylene for 5.5 hours per day for
up to 53 days (Stewart et al. 1977, as reported in USEPA 1980).
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Occupational exposure to an average concentration of 400 mg/cu m (in one
worker, for up to 15 years) resulted in subjective complaints, such as
headaches, fatigue, somnolence, dizziness, and a sensation of intoxication
(Medek and Kovarik 1977, as reported in USEPA 1980).  No other information on
the subacute of chronic toxicity of tetrachloroethylene on humans is available.

    Few studies have been conducted to evaluate the acute toxic effects of
tetrachloroethylene on animals.  A single 240-minute exposure to 1,340 mg/cu m
(200 ppm) resulted in moderate fatty degeneration of the liver of mice (Kylin
et al. 1963, as reported in NAS 1980).  Levels of serum glutamic oxaloacetic
transaminase were elevated following a single oral dose of 0.75 ml/kg in rats
(Moslen et^ al. 1977, as reported in NAS 1980).  Similarly, intraperitoneal
administration of 0.3 to 0.5 ml/kg tetrachloroethylene in rats resulted in
increased serum enzyme levels (Klassen and Plaa 1967, as reported in NAS
1980).  The oral LD50 value for the dog and cat is 4,000 mg/kg, the rabbit,
5,000 mg/kg, and for the mouse, the values range from 195 to 8,100 mg/kg
(USDHHS 1980).

    Rats, guinea pigs, rabbits, and monkeys exposed repeatedly for 7 hours per
day showed no changes in behavior at concentrations up to 2,720 mg/cu m
(duration unspecified; Rowe et al. 1952, as reported in USEPA 1980).  After
a 2-week exposure to 10,999 mg/cu m for 7 hours per day, rats showed signs of
marked salivation, restlessness, irritability and loss of equilibrium and
coordination (Rowe et al. 1952, as reported in USEPA 1980).  Changes in EEC
patterns were reported in rats exposed to 100 mg/cu m, 4 hours per day, for 15
to 30 days (Dmitrieva 1966; Dmitrieva and Kuleshov 1972, as reported in USEPA
1980) .  Increased liver weight and mild to marked centra] fatty degeneration
of the liver were reported in guinea pigs exposed to 670-16,750 mg/cu m, 7
hours per day for up to 158 repeated exposures (Rowe el; al. 1952, as
reported in USEPA 1980).  Congestion and granular swelling in the kidney was
observed in rats exposed to 1,540 mg/cu m for 8 hours per day, 5 days per week
over a period of 7 months (Carpenter 1937, as reported in USEPA 1980).  A very
high incidence of nephrotoxicity and a little evidence of hepatotoxicity was
observed in a chronic oral study of mice and rats gavaged with doses of
tetrachloroethylene ranging from 386 to 1,072 mg/kg/day for 78 weeks (National
Cancer Institute 1977, as reported in NAS 1980).

    Tetrachloroethylene did not induce mutations in Escherchia coli in the
presence of a microsomal activating system (Greim et al. 1975, as reported
in NAS 1980).  Female rats and mice exposed to 2,000 mg/cu m for 7 hours daily
on days 6 through 15 of gestation did not produce teratogenic effects.
However, there was a decrease in the fetal body weight of mice, a small but
significant increase in fetal resorptions in the rat, subcutaneous edema in
mice pups and delayed ossification of skull bones and sternabrae in the mice
(Schwetz et al. 1975, as reported in USEPA 1980).  Heptocellular carcinomas
were reported in mice, but not rats gavaged with daily oral doses of
tetrachloroethylene ranging from 386 to 1,072 mg/kg for up to 78 weeks
(National Cancer Institute 1977, as reported in NAS 1980).

    The acute toxic effects of tetrachloroethylene on aquatic fish life is
reflected by 96-hour LC50 values for the cladoceran, 17.7 mg/liter; the midge,
30.8 mg/liter; the rainbow trout, 4.8-5.8 mg/liter; the fathead minnow,
13.5-21.4 mg/liter; the bluegill, 12.9 mg/liter; and the mysid shrimp, 10.2
                                   H-20

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mg/liter.  Chronic toxicity was observed in the fathead minnow in
concentrations ranging from 0.5 to 1.4 mg/liter and in the mysid shrimp in
concentrations ranging from 0.3 to 0.67 mg/liter.  No adverse effects were
observed on chlorophyll a or cell number of freshwater algae exposed to
concentrations as high as 816 mg/liter.  Saltwater algae, however, are more
sensitive and have EC50 values ranging from 10.5 to 509 mg/liter (USEPA
1980).

    EPA has established an ambient water quality criterion of zero for the
maximum protection of human health from the potential carcinogenic effects due
to exposure to tetrachloroethylene through ingestion of contaminated water and
contaminated aquatic organisms.  However, since the zero level may not be
attainable at present, a level of 0.80 yg/liter, corresponding to a lifetime
incremental cancer risk of 0.000001, was recommended.

    EPA has not yet established an aquatic life water quality criterion for
tetrachloroethylene.
    Toluene

    Acute toxic effects in humans include adverse mental changes, such as
altered psychomotor performance, irritability, disorientation, and
unconsciousness (NAS 1980).  Additionally, toluene abuse has been associated
with cardiac arrhythmias and with liver and kidney dysfunction (Hayden et
al. 1977, Weisenberger 1977, as reported in NAS 1980).  In occupational
exposures to solvent mixtures, workers have reported myelotoxicity (NAS 1980),
minor blood cell change, and hepatomegaly (Greenburg et al.  1942, as
reported in NAS 1980), and immunoincompetence (Lange et al.  1973, as
reported in NAS 1980).  These affects cannot be attributed to toluene alone.

    The minimal lethal concentration of toluene was reported to be 20 mg/liter
in mice for a single 8-hour inhalation exposure.  The acute oral toxicity of
toluene is greater in young rats than in adult animals (Kimura et al.  1971,
as reported in NAS 1980).  Liver microsomal activity was decreased by acute
oral administration of high doses of toluene to rats (Mungikar and Pawar 1976,
as reported in USEPA 1980).  Rats exposed to 1,000 ppm for 8 hours/day for 1
week had slightly elevated serum glutamic-oxaloacetic transaminase (SCOT) and
serum glutamic-pyruvic transaminase (SGPT) activities.  Chronic studies in two
dogs exposed 8 hours/day for 6 months showed nervous system intoxication,
incoordination, paralysis of the hind legs, and congestive changes in the
lungs, heart, liver, kidney, and spleen (Tahti et al. 1977,  as reported in
NAS 1980).  Chromosome damage of bone marrow cells was reported in rats
injected with 1 g/kg of toluene (Lyapkalo 1973, as reported in NAS 1980).
Embryotoxicity was observed in rats exposed to toluene vapors at 600 mg/cu m
(Hudak et al. 1977, as reported in NAS 1980).  The carcinogenic potential of
toluene has not been established (USEPA 1980).

    The acute toxicity of toluene to freshwater organisms was demonstrated in
four species of fish with 96-hour LC50 values ranging from 17.5 top 59.3
mg/liter.  In saltwater shrimp and oysters, 96-hour LCSOs ranged from 9.5 to
1,050 mg/liter.  Striped bass and coho solmon have LC50 values of 6.3 and
10-50 mg/liter, respectively.  A range of LC50 values between 17.2 and 38.1
                                   H-21

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rag/liter were observed in a number of 24-hour tests on the grass shrimp.  A
chronic toxicity effect was observed on the hatching and survival of
sheepshead larvae and embryos.  Fresh and saltwater algae were adversely
affected at 245 mg/liter and 100 mg/liter, respectively.  Photosynthesis and
respiration were affected in kelp at 10 mg/liter and in algae at 34-85
mg/liter (USEPA 1980).

    EPA has established an ambient water quality criterion of 14.3 mg/liter
for the protection of human health from the toxic properties of toluene
ingested through water and contaminated organisms.

    EPA has not yet established an aquatic life water quality criterion for
toluene.
    Trans -1,2-Dichloroethylene

    Humans have developed nausea, vomiting, weakness, tremor, and cramps
following exposure to high concentrations of trans-1,2-dichloroethylene vapor
(Sax 1975).  The effects are rapidly reversible following removal from
exposure.  No other information is available on the toxic effects of this
compound on humans.

    There is limited information available from experimental studies.
Repeated inhalation exposures of 800 mg/cu m, 8 hours per day, 5 days per week
for 16 weeks of trans-1,2-dichloroethylene produced fatty degeneration of the
liver in rats (Freundt et al. 1977, as reported in USEPA 1980).   In a series
of studies using 1,2-dichloroethylene, no measureable effects on growth,
mortality, organ and body weights, hematology, clinical chemistry and gross
and microscopic pathology were reported in rats, rabbits, guinea pigs, and
dogs exposed to levels as high as 4,000 mg/cu m for six months (ACGIH 1977, as
reported in USEPA 1980).  Trans-1,2-dichloroethylene is not metagenic when
assayed with E_L coli K12 (Greim et al. 1975, as reported in USEPA 1980).
No information is available on the potential teratogenicity or carcinogenicity
of this compound.

    The assessment of the toxicity of trans-l,2-dichloroethylene on aquatic
life is limited to one 96-hour LC50 value of 135 mg/liter for the bluegill.
No other information is available on the toxic effects of this compound on
aquatic life (USEPA 1980).

    EPA has not yet established ambient water quality criteria for
trans-1,2-dichloroethylene because of the lack of sufficient data.
    1,1,1-Trichloroethane

    1,1,1-Trichloroethane primarily causes central nervous system disorders in
humans  (USEPA 1980).  Symptoms include depression; changes in reaction time,
perceptual speed, manual dexterity, and equilibrium; incoordination; and
burning and tingling sensation in the hands and feet.  Other toxic effects
that have been observed in humans include hepatic cellular damage, liver
function abnormalities, nausea, vomiting, diarrhea, hypotension, bradycardia,
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cardiac arrhythmias, eye irritation, fatigue, and death (NIOSH 1978, as
reported in USEPA 1980).

    Experimental studies have shown that 1,1,1-trichloroethane induces toxic
effects in a wide range of animal species.  Cardiac arrhythmia, myocardial
depression, tachycardia, tremors and respiratory failure have been reported in
the monkey.  Cardiac failure, pulmonary congestion, respiratory failure and
damage to the central and peripheral nervous systems have been observed in the
rat.  In the mouse, liver dysfunction, pulmonary congestion, and cardia
arrhythmia have been reported.  In the guinea pig, lung irritation and liver
dysfunction have been observed.  Respiratory failure has been induced in the
dog and damage to the central and peripheral nervous systems has been reported
in the cat (Truhart et al.  1973, Horiguchi and Horiguchi 1971, Tsapko and
Rappoport 1972, Beleg et al. 1974, Herd et al. 1974, Torkelson et al.
1958, MacEwen and Vernot 1974, as reported in USEPA 1980).  In most studies,
high concentrations were used.  The lowest concentration producing toxic
effects was 73 ppm administered four hours per day for 50-120 days (Tsapko and
Rappoport 1972, as reported in USEPA 1980).

    The acute toxic effects of 1,1,1-trichloroethane on freshwater aquatic
organisms is reflected by 96-hour LC50 values of 52-105 mg/liter for the
fathead minnow and 69.7 mg/liter for the bluegill.  Toxicity to saltwater
organisms has been observed in the mysid shrimp, with a reported LC50 value of
31.2 mg/liter, and in the sheepshead minnow, with an LC50 value of 70.9
mg/liter.  Toxicity to plants occurs in freshwater algae at levels greater
than 530 mg/liter and in saltwater algae at levels greater than 669 mg/liter.
No information is available on the chronic toxicity of 1,1,1-trichloroethane
on aquatic organisms (USEPA 1980).

    EPA has established an ambient water quality criterion of 18.4 mg/liter
for the protection of human health from the toxic properties of
1,1,1-trichloroethane ingested through water and contaminated aquatic
organisms.

    EPA has not yet established an aquatic life water quality criterion for
1,1,1-trichloroethane.
    1,1,2-Trichloroethane

    No information is available on the toxic effects of 1,1,2-trichloroethane
in humans.  Kidney necrosis was reported in the mouse and dog administered
single dose intraperitoneal injections of 0.35 ml/kg and 0.45 ml/kg,
respectively (Klassen and Plaa 1967, as reported in USEPA 1980).  The
effective dose that produces kidney necrosis in 50% of the animals is 0.17
ml/kg in mice and 0.4 ml/kg in the dog, both administered by intraperitoneal
injection.  Centrilobular necrosis of the liver was observed in dogs treated
with a single dose of 0.35 ml/kg by intraperitoneal injection (Klassen and
Plaa 1967, as reported in USEPA 1980).  1,1,2-Trichloroethane has been found
to cause liver and adrenal cancer in mice administered 195 and 390 mg/kg/day
by gavage for 78 weeks (NCI 1978, as reported in USEPA 1980).
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    The acute toxic effects of 1,1,2-trichloroethane on freshwater organisms
is reflected by 96-hour LC50 values for Daphnia magna of 18-43 mg/liter, for
the fathead minnow of 81.7 mg/liter, and for the bluegill of 40.2 mg/liter.
Chronic toxicity has been observed in the fathead minnow in concentrations
ranging from 6 to 14.8 mg/liter.   No information is available on the toxicity
to saltwater organisms or the effects of 1,1,2-trichloroethane to aquatic
plants (USEPA 1980).

    EPA has established an ambient water quality criterion of zero for the
maximum protection of human health from the  potential carcinogenic effects due
to exposure to 1,1,2-trichloroethane through ingestion of contaminated water
and contaminated fish.  However,  since the zero level may not be attainable at
present, a level of 0.6 yg/liter, corresponding to a lifetime incremental
cancer risk of 0.000001, was recommended.

    EPA has not yet established an aquatic life water quality criterion for
1,1,2-trichloroethane.
    Trichloroethylene

    The acute toxic effects of trichloroethylene in humans include nervous
system depression, incoordination and unconsciousness (NAS 1977).   Clinical
signs and symptoms are principally those of gastrointestinal upset, narcosis,
and occasional cardiac abnormalities (NAS 1980).  Controlled human clinical
studies have shown that inhalation of 100 to 200 ppm (duration unspecified)
caused complaints of the eye, throat irritation, and fatigue in several
exposed volunteers (Gamberale et al.  1976, Nomiyama and Nomiyama 1977,
Vernon and Ferguson 1969, as reported in NAS 1980).  In a separate study, two
patients who drank 350 and 500 ml trichloroethylene were rendered unconscious
for four and eight days, respectively.   Hypotension and cardiac arrhythmias
were delayed in onset, but were quite serious in nature (Dhuner et al. 1957,
as reported in NAS 1980).

    In an epidemiology study, evidence of increased nervous system disorders
was found in workers exposed for 5 to 15 years to concentrations less than the
threshold limit value (50 ppm).  (Grandjean et al.  1955, as reported  in
USEPA 1980).

    Insomnia, tremors, severe neurasthenic syndromes coupled with anxiety
states and progressive bradycardia have been reported in workers exposed to
concentrations of trichloroethylene ranging from 30 to 632 ppm  (duration
unspecified) with disturbances of the nervous system continuing for up to 1
year following exposure (Bardodej and Vyskoch 1956, as reported in USEPA
1980).  Headaches have been reported in workers exposed to concentrations as
low as 27 ppm (Nomiyama and Nomiyama 1977, as reported in USEPA 1980).  Each
of these accounts of the chronic effects of trichloroethylene suffer  from a
lack of accurate exposure levels and the inability to distinguish
trichloroethylene induced effects from those caused by other factors.

    Behavioral studies have generally confirmed that the CNS depressant
activity of trichloroethylene observed in humans also occurs in rats  following
roughly equivalent exposures (Khorvat and Formanek 1959 arid Goldberg  et al.
                                   H-24

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1964, as reported in USEPA 1980).  The acute oral LD50 of trichloroethylene in
rats if 4,920 mg/kg (NIOSH 1980); and the acute intraperitoneal LD50 for the
mouse isv2.2 ml/kg (Klaasen and Plaa 1967, as reported in NAS 1980).  A single
intraperitoneal injection of 0.6 ml/kg caused a loss of muscle tone,
depression of reflexes, and slowing of heart rate in guinea pigs (Mikiskova
and Mikiska 1966, as reported in NAS 1980).

    In subacute toxicity studies, rabbits injected intramuscularly with 4.38
grams per animal three times a week for four weeks developed a loss of
Purkinje cells with associated basket cells in the cerebellum and other less
specific damage to the telencephalic cortex, basal gaglia and brain stem
nuclei (Bartonicek and Brun 1970, as reported in USEPA 1980).  Similar effects
have been reported in rabbits exposed by inhalation to 1,889 ppm for 20 to 30
days (Bernardi eft al.  1956, as reported in USEPA 1980) and in dogs exposed
to 297-502 ppm (duration unspecified; Baker 1958, as reported in USEPA 1980).

    The chronic toxicity from long term exposure to trichloroethylene is not
considered to differ significantly from the observed acute toxic effects (NAS
1980).  Maximum no-effect levels have been reported in monkeys, 400 ppm,
rabbits and rats, 200 ppm and guinea pigs, 100 ppm, exposed to
trichloroethylene vapor 7 hours per day, 5 days per week for six months (Adams
et al. 1951, as reported in NAS 1980).

    In another study,  rats, guinea pigs, monkeys, rabbits, and dogs exposed by
inhalation to either 730 ppm, 8 hours per day, 5 days per week, for 6 weeks or
35 ppm continuously for 90 days showed no evidence of adverse effects
(Prendergast 1967, as reported in NAS 1980).

    Trichloroethylene has been found to be mutagenic in a number of
microsomally activated in vitro screening systems, including Salmonella
typhimurium (NAS 1980), Excherichia coli (Greim et al. 1975, as reported
in USEPA 1980) and Saccharomyces cerevisiae (Shahin and von Barstel 1977, as
reported in USEPA 1980) .   No evidence of teratogenicity was observed in mice
and rats exposed to 297 ppm on days 6 through 15 of gestation for 7 hours per
day (Schwetz et al. 1975, as reported in NAS 1977).

    Trichloroethylene has been found to be carcinogenic in the liver of mice
orally administered time weighted average doses of 1,169 and 2,339 mg/kg for
males and 869 and 1,739 mg/kg for females five days per week for 78 weeks.
Some evidence of metastasis of hepatocellular carcinoma to the lungs was also
observed in the mice.   No increase in the incidence of tumors was observed in
parallel experiments with rats (NCI 1976, as reported in USEPA 1980).  Two
other long-term bioassays, one in rats and the other using a different strain
of mice, yielded negative results (Maltoni 1979 and Van Duuren et al. 1979,
as reported in USEPA 1980).  This combined with questions about the design of
the NCI study have raised questions about the true carcinogenic potential of
trichloroethylene (NAS 1980).

    The acute toxicity of trichloroethylene on aquatic fishlife is reflected
by 96-hour LC50 values for cladoceran, 39-100 mg/liter, fathead minnow,
40.7-66.8 mg/liter, and the bluegill 44.7 mg/liter.  Intoxication
characterized by erratic swimming, uncontrolled movement and loss of
equilibrium was observed in grass shrimp and sheepshead minnow after several
                                   H-25

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minutes of exposure to 2.0 mg/liter and 20 mg/liter, respectively.  A loss of
equilibrium was reported in the fathead minnow exposed to 21.9 mg/liter for 96
hours.  A 50 percent decrease in 14C uptake during photosynthesis was observed
in saltwater algae exposed to 8 mg/liter trichloroethylene.  No information is
available one the chronic toxicity of trichloroethylene to aquatic fishlife.

    EPA has established an ambient water quality criterion of zero for the
maximum protection of human health from the potential carcinogenic effects due
to exposure to trichloroethylene through the ingestion of contaminated water
and contaminated aquatic organisms.  However, since the zero level may not be
attainable at the present time, a criterion of 2.7 ug/liter at an
incremental lifetime cancer risk of 0.000001, was recommended.

    EPA has not yet established an aquatic life water quality criterion for
trichloroethylene.
    Vinyl Chloride

    This compound in highly flammable and volatile with high explosive
characteristics.  The toxicity of this compound has been clearly described in
animals and in humans (NAS 1977 and USEPA 1980).

    In humans, vinyl chloride has been shown to produce central nervous system
dysfunction, sympathetic-sensory polyneuritic and organic disorders of the
brain (Smirnova and Granik 1970, as reported in NAS 1977)  In occupational
studies, vinyl chloride has been associated with scleroma-like skin
alterations, Raynaud's syndrome, acroosteolysis, thrombocytopenia, portal
fibrosis, and hepatic and pulmonary dysfunction (Juehe and Lange 1972, Juene
et al. 1974, Berk et al. 1975, Martsteller et al.  1975, as reported in
NAS 1977).  In addition, hepatic angiosarcoma, one of the rarest human
malignant neoplasms, has been observed in vinyl chloride workers (Anon 1974,
Makk et al. 1976, as reported in NAS 1977 and Creech and Johnson 1974, as
reported in USEPA 1980).  Lesions of the skin, bone, liver, spleen, and lungs
have also been reported after chronic exposure to this compound (Popper and
Thomas 1975, Gedigk et al. 1975, Thomas and Pepper 1975, as reported in NAS
1977).

    In acute arid subchronic inhalation studies, vinyl chloride has been shown
to produce lung congestion, hemorrhaging, blood-clotting difficulties, and
congestion of liver and kidneys (species unspecified; Mastromatteo et al.
1960, as reported in NAS 1977).  Numerous studies have reported its
carcinogenic effects in rats, mice, hamsters, and rabbits by both inhalation
and oral administration (USEPA 1980).

    No acute or chronic data are available on the effects of vinyl chloride on
freshwater of saltwater organisms (USEPA 1980).

    EPA has established an ambient water quality criterion of zero for the
maximum protection of human health from the potential carcinogenic effects due
to exposure to vinyl chloride through the ingestion of contaminated water and
contaminated aquatic organisms.  However, since the zero level may not be
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attainable at the present time, a level of 2.0 yg/liter, corresponding to a
lifetime incremental increase of cancer risk of 0.000001, was recommended.1

    EPA has not yet established an aquatic life water quality criterion for
vinyl chloride.
lln the Carcinogen Assessment Group's summary and conclusions regarding
carcinogenicity of vinyl chloride (July 14, 1978) an individual lifetime risk
of 0.00001 was associated with an intake of 1.054 mg/kg/day (0.53 mg/liter).
A risk of 0.000001 would be associated with an intake of 0.1054 mg/kg/day
(0.053 mg/liter).
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    2.    Acid Extractable Organic Compounds

    4-Chloro-m-cresol

    The only reported toxic effect of 4-chloro-m-cresol in humans is vesicular
dermatitis.  In sensitive individuals, a 1.5 percent aqueous solution caused a
pruritic vesicular dermatitis within four hours of exposure which regressed
within a week (Guy and Jacobs 1941, as reported in USEPA 1980).

    In animals, acute exposure to 4-chloro-m-cresol produces severe muscle
tremors, damage to renal tubules, and death in a few hours (Wein 1939, as
reported in USEPA 1980).  For the mouse, Wein (1939, as reported in USEPA
1980) reported LDSOs by subcutaneous injection and by intravenous injection of
360 and 70 mg/kg.  For the rat, the subcutaneous LD50 was given as 400 mg/kg.
An oral LD50 of 1,330 mg/kg has also been reported for the mouse (Schrotter
et al.  1977, as reported in USEPA 1980).  In subchronic studies in which
rats were injected subcutaneously with 80 mg/kg/day for 14 days and rabbits
were injected with approximately 6.5 mg/kg/day for four weeks, the only
observed effect was mild inflammation at the site of injection in the rats
(Wein 1939, as reported in USEPA 1980).  No chronic toxicity data for
4-chloro-m-cresol are available.

    Limited aquatic toxicity data is available for 4-chloro-m-cresol.  The
96-hour LD50 for the fathead minnow is 30 yg/liter (USEPA 1980).  No data
are available for saltwater species.

    EPA has not yet established ambient water quality criteria for protection
of human health and aquatic life from exposure to 4-chloro-m-cresol because of
the lack of sufficient information.  However, using available organoleptic
data for control of undesirable taste and odor quality of ambient water, the
recommended criterion is 3,000 yg/liter.
    2-Chlorophenol

    Very little information is available on the toxic effects of
2-chlorophenol on humans.  Acute toxicity has been characterized as being
"likely" to be corrosive and irritating to the eyes and skin (Doedens 1963, as
reported in USEPA 1980).  2-Chlorophenol is considered to be a weak uncoupler
of oxidative phosphorylation (Mitsuda et al.  1963, as reported in USEPA
1980) and a convulsant poison (Farquharson et al. 1958 and Angel and Rogers
1972, as reported in USEPA 1980).

    Relatively few acute toxicological studies are available on laboratory
animals.  Acute LD50 values have been reported as follows:  the rat, 670
mg/kg-oral and 900 mg/kg-subcutaneous (Diechmann 1943, as reported in USEPA
1980); the mouse, 670 mg/kgoral  (Bubnov et al. 1969, as reported in USEPA
1980); and the. blue fox, 440 mg/kg-oral (Bubnov et al. 1969, as reported in
USEPA 1980).  Subcutaneous LD50 values have been reported for the rabbit, 950
mg/kg (Christensen and Luginbyhl 1975, as reported in USEPA 1980).  Minimum
lethal dose values have also been reported for the rabbit, 120 mg/kg,
(intravenous administration; Kuroda 1926, as reported in USEPA 1980); for the
guinea pig 800 mg/kg,  (subcutaneous administration; Christensen and Luginbyhl
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1975, as reported in USEPA);  and for the albino rat, 230 mg/kg
(intraperitoneal administration; Farquharson et al. 1958, as reported in
USEPA 1980).  Symptoms of acute toxicity in rats, regardless of the route of
administration, include restlessness and increased rate of respiration,
followed by the development of motor weakness, tremors and convulsions.
Eventually, dyspnea and the appearance of coma result and continue until death
(Farquharson et al. 1958, as  reported in USEPA 1980).  Marked kidney injury
including red blood cells casts in the tubules, fatty infiltration of the
liver, and hemorrhages in the intestine were observed in rats following fatal
poisoning (dose unspecified;  Patty 1963).  Similar pathological effects were
reported for the blue fox and the mouse (Bubnor et al. 1969 as reported in
USEPA 1980).  A rapid onset of convulsions was observed in mice administered
2-chlorophenol intraperitoneally (dose unspecified; Angel and Rogers 1972, as
reported in USEPA 1980).

    No information is available on the subacute or chronic toxicity, nor on
the mutagenic or teratogenic potential of 2-chlorophenol.  Topical application
of 0.3% dimethylbenzanthracene in benzene as an initiator followed by 20%
2-chlorophenol twice weekly for 20 weeks, promoted papillomas in mice
(Boutwell and Bosch 1959, as  reported in USEPA 1980).

    The acute toxicity of 2-chlorophenol on aquatic fish life is reflected by
96-hour LC50 values for the cladoceran, 2.6-7.4 mg/liter, the goldfish, 12.4
mg/liter, the fathead minnow, 11.6-14.5 mg/liter, the guppy, 20.2 mg/liter,
and the bluegill, 6.6-10 mg/liter.  No effect was observed in fathead minnow
exposed to 3.9 mg/liter in a chronic test using the embryo-larval method.  A
reduction in chlorophyll was  observed in an alga exposed to 500 mg/liter for
72 hours indicating that plants may be less sensitive to 2-chlorophenol than
fish life.  2-Chlorophenol was found to impair the flavor of fish at
concentrations as low as 2 mg/liter (USEPA 1980).

    EPA has not yet established ambient water quality criteria for
2-chlorophenol because of the lack of sufficient data.
    2,4-Dichlorophenol

    No information is available on the toxic effects of 2,4-dichlorophenol on
humans.  In vitro studies, however, indicate that 2,4-dichlorophenol is an
uncoupler of oxidative phosphorylation (Mitsuda et al.  1963, as reported in
USEPA 1980).

    Relatively few studies are available on the acute or subacute toxicity of
2,4-dichlorophenal in animals.  Oral LD50 values have been reported for the
rat, 580 and 4,000 mg/kg (Derchman 1943 and Kobayashi et al. 1972, as
reported in USEPA 1980) and for the mouse, 1,600 mg/kg.  (Kobayashi jit al.
1972, as reported in USEPA 1980).  Acute subcutaneous and intraperitoneal LD50
values for the rat have been reported to be 1,730 mg/kg and 430 mg/kg,
respectively (Deichman 1943 and Farquharson et al.  1958 as reported in
USEPA).

    In a subacute study, all mice survived when 2,4-dichlorophenol was
administered orally for 10 days at a dose of 667 mg/kg body weight (Kobayashi
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e^t al.  1972, as reported in USEPA 1980).   In a six-month feeding study by
the same authors, no observed adverse changes in growth rate, hematology,
serum glutamic oxaloacetic transaminase (SGOT),  serum glutamic pyruvic
transaminase (SGPT), and behavior were reported for male mice fed dietary
levels  as high as 230 mg/kg/day (Kobayashi et al.  1972, as reported in USEPA
1980).   However, at the 230 mg/kg/day dosage levels, slight abnormalities in
liver histopathology were observed.   These authors concluded that 100
mg/kg/day was a maximum no-effect level in mice.

    No  information is available on the chronic toxicity, mutagenicity or
teratogenicity of 2,4-dichlorophenol.  Topical application of 0.3%
dimethylbenzanthracene in benzene as an initiator followed by 20% (312 mg/kg)
2,4-dichlorophenol twice weekly for 39 weeks promoted papillomas and
carcinomas in mice (Boutwell and Bosch 1959, as reported in NAS 1980).

    The acute toxic effects of 2,4-dichlorophenol on aquatic fish life is
reflected by 96-hour LC50 values of 2.6 mg/liter for cladoceran, 2.02 mg/liter
for the bluegill and 8.23 mg/liter for the juvenile fathead minnow.   Chronic
toxicity was observed in the fathead minnow exposed to concentrations ranging
from 290 to 460 yg/liter.  The toxicity of 2,4-dichlorophenol to aquatic
plants  occurs at much higher concentrations, ranging from 50 to 100 mg/liter
depending on the species.  Flavor impairment studies showed that fish flavor
became  tainted in 2,4-dichlorophenol concentrations ranging from 0.4
yg/liter for the largemouth bass to 14 yg/liter for the bluegill (USEPA
1980).

    EPA has established an ambient water quality criterion of 3.09 mg/liter
for the protection of human health from the toxic properties of
2,4-dichlorophenol.

    EPA has not yet established an aquatic life water quality criterion for
2,4-dichlorophenol.


    2,4-Dimethylphenol

    No information on the toxicity of 2,4-dimethylphenol in humans is
available (NAS 1977).  Acute toxicity has been observed in rats, mice, and
rabbits (NAS 1977).  Irritation of mucous membranes, enlargement of blood
vessels of the ears and extremities, and excitability followed by lethargy
were observed in rats and mice exposed by inhalation to 2,4-dimethylphenol.
In the same studies, oral LD50 values for rats and mice were reported as 3,200
mg/kg and 809 mg/kg, respectively; a dermal LD50 of 1,040 mg/kg was reported
for rats (Uzhdovini et al. 1974, as reported in USEPA 1980).  Topical
papillomas have been reported in mice treated with 2,4-dimethylphenol twice
weekly for 28 weeks (Boutwell and Bosch 1959, as reported in NAS 1977).

    The acute toxicity of 2,4-dimethylphenol on aquatic organisms is reflected
in the 96-hour LC50 values of 2.12 mg/liter for cladoceran,  16.75 mg/liter for
the fathead minnow, and 7.75 mg/liter for the bluegill.  Chronic toxicity was
observed in the fathead minnow in concentrations ranging from 1.5 to 3.2
mg/liter.  Chronic tests with invertibrate species, which appear to be most
sensitive to 2,4-dimethylphenol, have not been performed  (USEPA 1980).  Algae
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and duckweed were affected by concentrations of 500 mg/liter and 292.8
mg/liter, respectively.  No information is available on the toxic effects of
2,4-dimethylphenol on saltwater organisms (USEPA 1980).

    EPA has not yet established an ambient water quality criterion for
2,4-dimethylphenol because of the lack of sufficient information.  However,
using available organoleptic data for control of undesirable taste and odor
quality of ambient water, the estimated level is 400 yg/liter.
    4,6-Dinitro-o-cresol

    A number of human poisonings by 4,6-dinitro-o-cresol have been reported.
4,6-Dinitro-o-cresol may be absorbed in acutely toxic amounts through the
respiratory and gastrointestinal tracts and through the skin.  Signs and
symptoms of both acute and chronic poisoning include profuse sweating,
malaise, thirst, lassitude, loss of weight, headache, sensation of heat, and
yellow staining of the skin, hair, sclera, and conjunctiva.  Other effects
occasionally reported include kidney damage, diarrhea, disorders of the
gastrointestinal tract, cardiovascular system, and peripheral vascular and
central nervous systems (Doull et al. 1980, and USEPA 1980).  It has been
estimated that 5 mg/kg may prove fatal to humans (Fairchild 1977, as reported
in USEPA 1980).  A study was conducted in which five male volunteers were
given oral doses of 75 mg/day of 4,6-dinitro-o-cresol for five consecutive
days (Harvey et al. 1951, as reported in USEPA 1980).  At blood levels of 20
mg/kg, an exaggerated sense of well-being was experienced.  At blood levels of
40 to 48 mg/kg, headache, lassitude, and malaise were reported.  In patients
who received 4,6-dinitro-o-cresol for the treatment of obesity during the
1930s, poisonings, deaths, and the development of cataracts were reported.
Signs of poisoning occurred in three people who had taken as little as 0.35 to
1.5 mg/kg/day (NIOSH 1978, as reported in USEPA 1980).  In a Russian study of
agricultural workers, exposure to 0.7 to 0.9 mg/cu m produced unspecified
changes in the blood, cardiovascular, and autonomic and central nervous
systems and in the gastrointestinal tract (Burkatskaya 1965, as reported in
USEPA 1980).

    Acute oral LD50 values have been reported for the rat (30-85 mg/kg), mouse
(16.4-47 mg/kg), and rabbit (24.8 mg/kg) (USEPA 1980).  LD50 values for
subcutaneous administration in the rat, mouse, and goat range from 20-50
rag/kg.  4,6-Dinitro-o-cresol is less toxic by the dermal route, with LD50s for
the mouse and rabbit of 187 and 1000 mg/kg, respectively (USEPA 1980).  In a
feeding study with rats, no adverse effects were observed among rats on diets
containing 100 mg 4,6-dinitro-o-cresol/kg food.  At 1000 mg/kg, observed
effects included weight loss, emaciation, unkempt appearance, and minor
histopathological effects on the liver, kidneys, and spleen (Spencer et al.
1948, as reported in USEPA 1980).  Ambrose (1942, as reported in USEPA 1980)
reported no observable effects in rats fed diets containing 63 mg
4,6-dinitro-o-cresol/kg food for 105 days.  At dietary levels of 125 mg/kg
food, 60 percent of the animals died.  Cats exposed to airborne
4,6-dinitro-o-cresol at 0.2 mg/cu m for 2-3 months had slightly increased body
temperatures and leukocyte counts and decreased hemoglobin concentrations,
erythrocyte counts, and catalase and peroxidase activities (Burkatskaya 1965,
as reported in USEPA 1980).
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    No aquatic, toxicity data are available for 4,6-dinitro-o-cresol.

    EPA has established an ambient water quality criterion of 13.4 yg/liter
for protection of human health from the toxic properties of
4,6-dinitro-o-cresol through ingestion of contaminated water and aquatic
organisms.

    EPA has not yet established an aquatic life water quality criterion for
4,6-dinitro-o-cresol.
    2,4-Dinitrophenol

    2,4-Dinitrophenol is a potent uncoupler of oxidative phosphorylation.
This prevents the utilization of energy provided by cellular respiration and
glycolysis by inhibiting the formation of high energy phosphate bonds.
2,4-Dinitrophenol may also act directly on the cell membrane causing toxic
effects on cells not dependent on oxidative phosphorylation for their energy
requirements (QSEPA 1980).  Acute poisoning in humans from 2,4-dinitrophenol
results in sudden onset of pallor, burning thirst,  agitation, dyspnea,  profuse
sweating, and hyperpyrexia (Horner 1942, as reported in USEPA 1980).
Therapeutic doses of 2,4-dinitrophenol have resulted in skin rashes with
intense itching and considerable swelling (Tainter  et al.  1933, as reported
in USEPA 1980).  A loss of taste for salt and sweets has been reported in some
patients treated therapeutically with 2,4-dinitrophenol (Tainter et al.
1933, as reported in USEPA 1980).  The development  of cataracts in humans has
been clearly demonstrated after use of 2,4-dinitrophenol (USEPA 1980).   Bone
marrow effects (agranulocytosis) and neuritis have  also been reported in
humans (Horner 1942, as reported in USEPA 1980).

    In animals, an increase in the percentage of stillborn young and neonatal
deaths has been reported in a study of rats treated with 20 mg/kg
2,4-dinitrophenol, 8 days prior to mating (Wulff et al. 1935, as reported in
USEPA 1980).

    The acute toxicity of 2,4-dinitrophenol on freshwater aquatic organisms is
reflected in LC50 values of 4.09 mg/liter for Daphnia magna, 16.7 mg/liter
for the juvenile fathead minnow, and 0.62 mg/liter  for the bluegill.
Increased respiration was observed in the tadpoles  of Southern bullfrogs
exposed to 5.52 mg/liter for 7 hours.  A 96-hour lethal threshold value of 0.7
mg/liter has been reported for juvenile Atlantic salmon (USEPA 1980).

    Saltwater organisms are also affected by 2,4-dinitrophenol.  Mysid shrimp
had a 96-hour LC50 of 4.85 mg/liter; the embryo of  herring, a 96-hour LC50 of
5.5 mg/liter; and sheepshead minnow, a 96-hour LC50 of 29.4 mg/liter.
Respiration and motility were reported to be inhibited in the sperm of sea
urchin exposed to 92.0 mg/liter for more than 1 hour.  Abnormal cleavage in
the embryo of the sea urchin was also reported to occur at 46 mg/liter for 2
hours.  At levels of 10 mg/liter, complete mortality of Lymnaeid snails was
reported within 24 hours.  The chronic effects of 2,4-dinitrophenol on
hatching and survival in an early life test with the sheepshead minnow
resulted in limits of 7.9 mg/liter (USEPA 1980).
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    Freshwater plants also exhibited a toxicity to 2,4-dinitrophenol.
Chlorophyll synthesis in algae was inhibited after 3 days exposure to 50
mg/liter.  A 50% reduction in growth was observed in duckweed exposed to 1.47
mg/liter.  Eight-day toxicity thresholds for different species of algae varied
from 16-33 mg/liter (USEPA 1980).

    EPA has established an ambient water quality criterion of 70 yg/liter
for the protection of human health from the toxic properties of total
dinitrophenols through ingested water and contaminated aquatic organisms.

    EPA has not yet established an aquatic life water quality criterion for
2,4-dinitrophenol.


    2-Nitrophenol

    The acute toxic effects of 2-nitrophenol include kidney and liver damage
and methemoglobin formation in experimental animals (Sax 1975).  Experimental
studies have shown 2-nitrophenol to inhibit chloride transport in red blood
cells in rats (Motais et al.  1978, as reported in USEPA 1980) and to
increase the platelet count in rats administered 1 mg/kg by intraperitoneal
injection (Gabor et al. 1960, as reported in USEPA 1980).  Oral LD50 values
are reported for the rat and mouse as 2,830 rag/kg and 1,300 mg/kg,
respectively (Vernot et al. 1977, as reported in USEPA 1980).  No other
information on the toxicity of 2-nitrophenol in human or nonhuman mammals is
available.

    The 24-hour LC50s of 2-nitrophenol in freshwater organisms are 210
mg/liter for Daphnia magna and 66.9 mg/liter for juvenile bluegill.
Eight-hour exposures of gold fish to 33.3 mg/liter resulted in 38% mortality.
Shrimp showed 96-hour lethal threshold values of 32.9 mg/liter.  No chronic
toxicity information is available on any aquatic organisms (USEPA 1980).

    Freshwater plants were reported to be more susceptible to the effects of
2-nitrophenol than aquatic fishlife.  Inhibition of chlorophyll synthesis was
observed in algae treated with 35 mg/liter for 3 days and a 50% reduction in
growth was reported in duckweed exposed to 62.5 mg/liter (USEPA 1980).

    EPA has not yet established ambient water quality criteria for
2-nitrophenol because of the lack of sufficient information.


    4-Nitrophenol

    No information is available on the acute or chronic toxicity of
4-nitrophenol to humans (USEPA 1980).  The known effects of 4-nitrophenol
demonstrated by animal studies include methemoglobinemia and shortness of
breath (Von Oettingen 1949, as reported in USEPA 1980).  4-Nitrophenol
inhibited chloride transport in rat red blood cells (Motais et al. 1978, as
reported in USEPA 1980) and increased respiratory volume in rats administered
7-12 mg by stomach tube (Grant 1959, as reported in USEPA 1980).  Oral LD50s
for the rat and mouse are reported as 350 and 470 mg/kg, respectively
(Fairchild 1977, Vernot et al. 1977, as reported in USEPA 1980).
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    Acute toxicity of 4-nitrophenol has been demonstrated in freshwater
aquatic fishlife.  96-Hour LC50 values reported for 4-nitrophenol for
bluegills and fathead minnows are 8.28 mg/liter and 60.5 mg/liter,
respectively.  The toxicity of this compound to daphnids shows a wide
variation with values ranging from 8.4 to 21.9 mg/liter.  Mortality of 42% in
goldfish was reported after 8 hours exposure to 8.0 mg/liter.  4-Nitrophenol
produced 96-hour LCSOs of 7.17 mg/liter in mysid shrimp and 27.1 mg/liter in
the sheepshead minnow.  96-Hour lethal threshold values for shrimp and
soft-shell clams were reported to be 26.4 and 29.4 mg/liter, respectively
(USEPA 1980).

    Chronic studies on hatching and survival in the early life stage test
showed toxic effects in concentrations ranging from 10 to 16 mg/liter for
sheepshead minnows.  No other information is available on the chronic effects
on aquatic organisms (USEPA 1980).

    Inhibition of chlorophyll synthesis was reported in alga exposed to 25
mg/liter after 3 days.  Growth inhibition of 50% was also reported in alga
exposed to 6.95 mg/liter for 80 hours and in duckweed exposed to 9.45 mg/liter
(USSPA 1980).

    EPA has not yet established ambient water quality water criteria for
4-nitrophenol because of the lack of sufficient information.


    Pentachlorophenol

    Exposure of pentachlorophenol in humans has been reported to cause loss of
appetite, eye irritation, respiratory difficulties, anesthesia, hyperpyrexia,
sweating, dyspnea, skin irritation, and rapidly progressive coma (Menon 1958,
as reported in NAS 1977).  The minimum lethal dose for humans is estimated to
be 29 mg/kg (Toxic Substance List 1974, as reported in NAS 1977).  Chronic
exposure to pentachlorophenol has been associated with the development of
chloracne, a type of acneform dermatitis (Baader and Bauer 1951 and Nomura
1953, as reported in USEPA 1980).  Nonfatal chronic exposures can produce
muscle weakness, headache, anorexia, abdominal pain, and weight loss, in
addition to skin, eye, and respiratory irritation (USEPA 1980).

    Acute symptoms in animals include vomiting, hyperpyrexia, elevated blood
pressure, increased respiration rate, and tachycardia (NAS 1980).  The acute
oral LD50s for pentachlorophenol are reported in the ranges of 120-140 mg/kg
for the mouse, 27-100 mg/kg for the rat, 100 mg/kg for the guinea pig, 100-130
mg/kg for the rabbit, and 150-200 mg/kg for the dog (Christensen et al.
1974, Deichmanri et al. 1942, Knudsen et al. 1974, McGavack et al. 1941,
Stohlman 1951, as reported in NAS 1977).  Teratogenic effects have been
reported in rats orally administered amounts up to 50 mg/kg/day during day
6-15 of gestation  (Schwetz et al. 1974, as reported in NAS 1977).  No
evidence of mutagenicity was found in several short-term bioassays (Anderson
et al. 1972, Fahrig et al. 1978, Vogel and Chandler 1974, Buselmaier et
al. 1973, as reported in USEPA 1980).

    Dermal application of a 20% solution of pentachlorophenol dissolved in
benzene did not increase the rate of papillomas in mice pretreated with
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dimethylbenzanthracene (Boutwell and Bosch 1959, as reported in USEPA 1980).
Mice dosed with commercial pentachlorophenol at 46.4 mg/kg from 7-28 days of
age and then fed 130 ppm in the diet for the remainder of their life did not
have a significant increase in tumors (Innes et al. 1969, as reported in
USEPA, 1980) .   No effect was also observed in rats fed amounts up to 30 mg/kg
for 22-24 months (Schwetz et al. 1978, as reported in USEPA 1980).

    Pentachlorophenol has been shown to be acutely toxic to a wide variety of
freshwater fish.  No chronic test data are available.  For nine fish species
tested, the 96-hour LC50 values ranged from 37 to 340 yg/liter.  Toxicity
tests gave 96-hour LC50 values ranging from 50-130 yg/liter in sockeye
salmon, from 60-77 yg/liter in the bluegill, and 340 yg/liter in fathead
minnows (USEPA 1980).

    Saltwater marine life are also affected by pentachlorophenol.  Adjusted
96-hour LC50 values for sheepshead minnows, pinfish, and striped mullet ranged
from 21 to 442 yg/liter.  Pentachlorophenol appears to be most toxic to
molluscs; shrimp are less sensitive and oysters more sensitive than fish.
Oyster embryos develop abnormally when exposed to 55 yg/liter for 48 hours.
Lugworm feeding activity was significantly inhibited by concentrations of 80
yg/liter pentachlorophenol during a 144-hour exposure.  Chronic studies of
saltwater organisms show that 195 yg/liter significantly reduced hatching of
embryos spawned by exposed parental fish and reduced survival of second
generation sheepshead minnows in a 151-day life cycle exposure (USEPA 1980).

    In plant tests, pentachlorophenol caused complete destruction of
chlorophyll in algae in 72 hours at 7.5 yg/liter, and in kelp in 4 days at
2.66 rag/liter (USEPA 1980).

    EPA has established an ambient water quality criterion of 1.01 mg/liter
for protection of public health from the toxic properties of pentachlorophenol
ingested through water and contaminated fish.

    EPA has not yet established an aquatic life water quality criterion for
pentachlorophenol.
    Phenol

    The predominant effect of phenol on humans is on the central nervous
system leading to sudden collapse and unconsciousness (USEPA 1980).  Numerous
cases of phenol toxicity resulting from occupational exposures have reported
symptoms including shock, collapse, coma, convulsions, cyanosis, and death
(StajduhavCaric 1968, Noury 1940, Johstone and Miller 1960, Cronin and Brauer
1949, Duvernevil and Ravier 1962, Abraham 1972, Light 1931, as reported in
USEPA 1980).

    People who had consumed estimated daily doses of 10-240 mg phenol in well
water for approximately 1 month developed burning of the mouth, mouth sores,
diarrhea, headaches, skin rashes, abdominal pain, dizziness, and dark urine
(Baker et al. 1978, as reported in USEPA 1980).
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    The toxic effects observed in animals are quite similar to those in
humans.  The pathological changes produced by phenol in animals vary with the
route of absorption, vehicle employed,  concentration,  and duration of
exposure.  Local damages to the skin include eczema, inflammation,
discoloration, papillomas, necrosis, sloughing,  and gangrene.   Following oral
ingestion, the mucous membranes of the  throat and esophagus may show swelling,
corrosions, and necroses, with hemorrhage and serious  infiltration of the
surrounding areas.  In a severe intoxication, the lungs may show hyperemia,
infarcts, bronchopneumonia, purulent bronchitis, and hyperplasia of the
peribronchial tissues.  There can be myocardial  degeneration and necrosis.
The hepatic cells may be enlarged, pale, and coarsely granular with swollen,
fragmented, and pyknotic nuclei.  Prolonged administration of phenol may cause
parenchymatous nephritis, hyperemia of  the glomerular and cortical regions,
cloudy swelling, edema of the convoluted tubules, and degenerative changes of
the glomeruli.  Blood cells become hyaline, vacuolated, or filled with
granules.  Muscle fibers show marked striation (Deichman and Keplinger 1963,
as reported in USEPA 1980).

    The acute toxicity of phenols in mammals ranges from an oral LD50 of 100
mg/kg in the cat (Macht 1915, as reported in USEPA 1980) to 620 mg/kg in the
rabbit (Clark and Brown 1906, as reported in USEPA 1980).  Pathological
changes reported in mammals include intense congestion of the peritoneum,
abdominal viscera, kidney and adrenals, and marked degenerative changes in the
kidney.  In rats fed 8,000 mg/liter in  their drinking water over two
generations, there were reduced growth  rates in  the young with many deaths
(Heller and Pursell 1938, as reported in USEPA 1980).   In another study, no
effects were observed in rats fed for 12 months  at concentrations as high as
2,400 mg/liter in the drinking water (Diechmann  and Oesper 1940, as reported
in USEPA 1980).  Slight kidney and liver effects were reported in rats
administered 20 daily doses of 0.1 g/kg by gavage (Unpublished report of Dow
Chemical 1976, as reported in USEPA 1980).  Skin painting studies of mice
exposed to 20% phenol concentrations have produced skin ulcerations, exhibited
strong promoting action on tumor development, and exhibited a weak
carcinogenic response (Salaman and Glendenning 1957, as reported in USEPA
1980).

    The acute toxicity of phenol to freshwater vertebrates ranges from 44.5
mg/liter at 96 hours for the goldfish to 10.2 mg/liter for rainbow trout.
Rainbow trout was the most sensitive species tested with a 24-hour LC50 of 5.0
mg/liter for embryos.  Juvenile rainbow trout were killed at 6.5 mg/liter
phenol in 2 hours.  At these concentrations, there was rapid damage to gills
and severe pathology of other tissues.   Typical  gross pathological changes
have also been reported and include internal hemorrhages, deterioration of
gill membranes, degradation of the liver, and brain damage.  Phenol appears to
act as a nerve poison causing too much blood to  flow to the gills and to the
heart cavity of the fish.  Pathological changes  in the gills and in fish
tissue have been found at concentrations of 20-70 ug/liter.  Phenol is
acutely toxic to freshwater invertebrates, although it appears to be less
toxic to fish  food organisms and lower aquatic life than to fish.  The 48-hour
LC50 for the freshwater flea is 9.6 mg/liter.  A concentration of 2.0 mg/liter
inhibited egg development in oysters and reduced oxygen consumption
approximately 50% in the freshwater snail.  Phenols inhibit chlorophyll
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synthesis, and cause complete destruction of algae at concentrations of 50 and
1,500 mg/liter, respectively (USEPA 1980).

    EPA has established an ambient water quality criterion of 3.5 mg/liter for
the protection of human health from the toxic properties of phenol through
ingestion of contaminated water and contaminated aquatic organisms.

    EPA has not yet established an aquatic life water quality criterion for
phenol.
    2,4,6-Trichlorophenol

    No information is available on the toxic effects of 2,4,6-trichlorophenol
on humans.  In animal studies, a number of different adverse effects have been
observed.  Convulsions were produced in rats injected intraperitoneally with
2,4,6-trichlorophenol during an acute toxicity test.  The LD50 was estimated
at 276 mg/kg in this test (Farquharson et al. 1958, as reported in USEPA
1980).   2,4,6-Trichlorophenol was reported to cause inhibition of lactate
dehydrogenase and hexokinase, in. vitro, in concentrations ranging from
0.0028-0.005 Molar (species unspecified; Stockdale and Selwyn 1971, as
reported in USEPA 1980).  2,4,6-Trichlorophenol was shown to penetrate the
rabbit eye with the highest amounts concentrating in the cornea and
conjunctiva (Ismail et al.  1975, as reported in USEPA 1980).  However, the
significance of this finding has not yet been established.

    No information is available on the subacute or chronic effects of
2,4,6-trichlorophenol.  In a mutagenicity study using a strain of
Saccharomyces cerevisiae, 400 mg of 2,4,6-trichlorophenol increased the
mutation rate (Fahrig et al. 1978, as reported in USEPA 1980).  Evidence of
a genetic change in the offspring of mothers administered 50 or 100 mg/kg of
2,4,6-trichlorophenol on day 10 of gestation was reported in a mouse spot test
(Fahrig et aj.. 1978, as reported in USEPA 1980).  2,4,6-Trichlorophenol was
negative in the Salmonella-mammalian microsome Ames test (Rasanen et al.
1977, as reported in USEPA 1980).  In a lifetime feeding study,
2,4,6-trichlorophenol was shown to be carcinogenic in male rats, including
lymphomas or leukemias, and in both male and female mice, including
hepatocellular carcinomas or adenomas.  Both tests were conducted with dosage
levels of approximately 5,000 ppm in the diet (NCI 1979, as reported in USEPA
1980).   The topical application of a 20% solution of 2,4,6-trichlorophenol in
benzene did not increase the incidence of papillomas in mice pretreated with
dimethylbenzanthracene (Boutwell and Bosch 1958, as reported in USEPA 1980).

    The acute toxicity of 2,4,6-trichlorophenol on aquatic life is reflected
by the following 96-hour LC50 values for the cladoceran, 6 mg/liter, the
fathead minnow, 0.6 mg/liter, the juvenile fathead minnow, 9 mg/liter, and the
bluegill, 0.3 mg/liter.  Chronic toxicity was observed in an early life stage
test using fathead minnow exposed to concentrations ranging from 0.53-0.97
mg/liter.  One hundred percent mortality was observed in lymnaeid snails
exposed to 5 mg/liter for 24 hours.  The highest estimated concentration (ETC)
of 2,4,6-trichlorophenol that will not impair the flavor of fish is 52
ug/liter for a 48-hour exposure of rainbow trout.  Complete destruction of
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chlorophyll was observed in an alga exposed to 10 mg/liter and chlorosis was
reported in duckweed exposed to 5.9 mg/liter (USEPA 1980).

    EPA has established an ambient  water quality criterion of zero for the
maximum protection of human health  from the potential carcinogenic effects due
to exposure to 2,4,6-trichlorophenol through ingestion of contaminated water
and contaminated aquatic organisms.  However, since a zero level may not be
attainable at present, a level of 1.2 yg/liter, corresponding to a lifetime
incremental cancer risk of 10-6, was recommended.

    EPA has not yet established an  aquatic life water quality criterion for
2,4,6-trichlorophenol.
    3.    Base/Neutral Extractable Organic Compounds

    Acenaphthene

    Very little information on the toxic effects of acenaphthene in humans is
available.   It is irritating to skin and mucous membranes, and may cause
vomiting if swallowed in large quantities (Sax 1975).   In animals, oral
administration of 2 g/kg daily for 32 days was reported to cause loss of body
weight, changes in peripheral blood, heightened amino transferase levels in
blood serum, and mild morphological damage to both liver and kidneys in rats.
In the same studies, oral LDSOs for rats and mice were 10 g/kg and 2.7 g/kg,
respectively (Knoblock et al.  1969, as reported in USEPA 1980).  Chronic
inhalation studies showed toxic effects to the blood,  lungs, and glandular
constituents in rats exposed to 12 mg/cu m, 4 hours per day, six days per week
for 5 months (Reshetyuk et al. 1970, as reported in USEPA 1980).

    No information is available on the teratogenicity of acenaphthene and the
only data on mutagenicity, using microoganisms as the indicator system, were
negative (USEPA 1980).  Very little work has been done to determine whether
acenaphthene may have carcinogenic potential.  Negative results were obtained
in the newt with acenaphthene injected subcutaneously (dosage not reported,
USEPA 1980).  The only other carcinogenicity studies available involve
acenaphthene as a component of a complex mixture of polycyclic aromatic
hydrocarbons (USEPA 1980).

    In one study, isolated polycyclic hydrocarbon-rich fractions from the
neutral portion of cigarette smoke condensate were applied (dose unspecified)
to the dorsal skin of female mice, five times a week for 13 months.  The
acenaphthene containing extracts were applied five weeks after the animals
were painted once with 125 ug of 7,12-dimethylbenz(a)anthracene.  No
significant tumor-promoting activity over controls were observed (Akin et
al., 1976 as reported in USEPA 1980).  In a second study benzene extracts, of
gasoline exhaust condensates containing an unspecified concentration of
acenapthene, were reported to be carcinogenic in mouse skin painting studies
(details unspecified; Hoffman and Wynder, 1962 as reported in USEPA 1980).

    The most thoroughly investigated effect of acenaphthene is its ability to
produce nuclear and cytological changes in microbial and plant species.  Most
of these changes, such as an increase in cell size and DNA content, are
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associated with disruption of the spindle mechanisms during mitosis and the
resulting induction of polyploidy (USEPA 1980).

    The acute toxicity of acenaphthene to aquatic organisms is reflected in a
static 48-hour LC50 of 41.2 mg/liter for Daphnia magna; and static 96-hour
LC50 values of 1.7 mg/liter in the bluegill, 0.97 mg/liter in the mysid shrimp
and 2.23 mg/liter in the sheepshead minnow.  Chronic toxicity by the
embryo-larval test was observed in the sheepshead minnow.   Algae were affected
at 500-530 yg/liter.  Bluegill were reported to accumulate acenaphthalene
during a 28-day exposure and a bioconcentration factor of 387 was reported for
this same species (USEPA 1980).

    Sufficient data were not available for EPA to establish ambient water
quality criteria that would protect human health against the potential
toxicity of acenaphthene.  However, a level of 0.02 mg/liter was recommended
based on available organoleptic data, for controlling undesirable taste and
odor quality of ambient water.

    EPA has not yet established an aquatic life water quality criterion for
acenaphthene.
    Acenaphthylene

    No information is available on the toxic effect of acenaphthylene on
humans, animals, or aquatic life.  EPA has not yet established ambient water
quality criteria for acenaphthylene because of the lack of sufficient data.
However, the agency has established an ambient water quality criterion of zero
for the maximum protection of human health from the potential carcinogenic
effects due to exposure to polynuclear aromatic hydrocarbons, which include
acenaphthylene, through ingestion of contaminated water and contaminated
aquatic organisms.  However, since a zero level may not be attainable at
present, a level of 2.8 ng/liter, corresponding to a lifetime incremental
cancer risk of 10-6, was recommended.
    Anthracene

    No information is available on the toxicity of pure anthracene to humans.
However, anthracene oils can cause headaches, nausea, loss of appetite, skin
rashes, and irritation of the mucous membranes (Encyclopedia of Occupational
Health and Safety 1971).  Various oils of anthracene and substances containing
anthracene have also been associated with carcinogenesis in animals (Searle
1976).  Anthracene exhibits relatively low toxicity to animals.  The acute
oral toxicity in rats is greater than 3,200 mg/kg.  Large oral doses in rats
caused reaction of the abdominal wall, rough coat, and diarrhea (Patty 1963).
Anthracene applied to the backs of guinea pigs caused a slight skin irritation
on the pig skin (Patty 1963).   No information is available on the carcinogenic
effects of pure anthracene.

    There is limited information on the toxicity of anthracene to aquatic
organisms.  A 90% lethal photodynamic response was observed in protozon
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exposed to 0.1 yg/liter for 60 minutes.   Bioconcentration factors ranged
from 200 in the Daphnia magna to 3,500 in the may fly (USEPA 1980).

    EPA has not yet established ambient  water quality criteria for anthracene
because of the lack of sufficient data.   However, the agency has established
an ambient water quality criterion of zero for the maximum protection of human
health from the potential carcinogenic effects due to exposure to polynuclear
aromatic hydrocarbons, which include anthracene,  through ingestion of
contaminated water and contaminated aquatic organisms.   However, since a zero
level may not be attainable at present,  a level of 2.8 ng/liter, corresponding
to a lifetime incremental cancer risk of 10-6, was recommended.


    Benz(a)anthracene

    No information is available on the toxic effects of benz(a)- anthracene on
humans.  Most of the studies in animals  have been conducted to evaluate the
carcinogenic potential of benz(a)anthracene.  This is especially true of the
derivatives of benz(a)anthracene.  Benz(a)anthracene has been shown to be
carcinogenic Ln the mouse by several routes of administration (IARC 1973).
Oral administration of 1.5 mg as a 3% solution in "methocelaerosol OF" by
stomach tube, for 15 treatments over a 5-week period, resulted in the
development of hepatomas and lung adenomas (Klein 1963, as reported in IARC
1973).  Skin tumors developed when benz(a)anthracene was applied topically 3
times a week, to mice, in a 1% concentration in toluene and a 0.002%
concentration in n-dodecane (Bingham and Falk 1969, as reported in IARC
1973).  Sarcomas were also produced in mice following subcutaneous injections
with as low as 50 yg administered as a single dose (Steiner and Edgecomb
1952, as repotted in IARC 1973).  No information is available on the
mutagenicity or teratogenicity of benz(a)anthracene (USEPA 1980).

    The only information available on the toxic effects of benz(a)anthracene
on aquatic life is a 6-month study of bluegill exposed to 1.0 mg/liter.  In
this study, 87% mortality was observed (USEPA 1980).

    EPA has not yet established ambient  water quality criteria for
benz(a)anthracene because of the lack of sufficient data.  However, the agency
has established an ambient water quality criterion of zero for the maximum
protection of human health from the potential carcinogenic effects due to
exposure to polynuclear aromatic hydrocarbons, which include
benz(a)anthracene, through ingestion of contaminated water and contaminated
aquatic organisms.  However, since the zero level may not be attainable at
present, a level of 2.8 ng/liter, corresponding to a lifetime incremental
cancer risk of 10-6, was recommended.
    Benzidine

    Epidemiological studies show that occupational exposure to benzidine is
strongly associated with bladder cancer.  A high incidence of bladder tumors
was reported in workmen exposed to benzidine or benzidine and aniline in
British chemical factories.  Thirty cases of bladder tumors were reported,
with a mean latent period of ten years  (Case et al.  1954, as reported in
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USEPA 1980).  In a retrospective study of a single factory, 17 of 76 workmen
exposed to benzidine alone developed bladder tumors (Goldwater et al. 1965,
as reported in IARC 1972).  Bladder cancer has been reported in several
studies of Italian dyestuff workers.  In a study by Barsotti and Vigliani
(1952, as reported in USEPA 1980), 13 of 83 workers developed bladder
carcinomas from exposure to benzidine during the period 1931 to 1948.
Dermatitis and increased urinary fJ-glucuronidase activity have also been
reported in workers exposed to benzidine (USEPA 1980).

    Benzidine is also carcinogenic to experimental animals.  Cholangiomas and
liver-cell tumors were reported in lifetime feeding studies with rats fed
0.017% benzidine in the diet and hamsters fed 0.1% in the diet (Boyland et
al. 1954, Saffiotti et al. 1967, as reported in IARC 1972).  Three of seven
dogs given 200-300 mg/day, 6 days/week, for 5 years developed bladder
carcinomas seven to nine years after the start of treatment (Spitz et al.
1950, as reported in IARC 1972).  Benzidine administered subcutaneously to
rats at a dose of 15 rag/week for their lifespan produced liver injury,
cirrhosis, hepatomas, sebaceous gland carcinomas, and adenocarcinomas of the
rectum (Spritz et al. 1950, as reported in USEPA 1980).  A cumulative dose
of 0.75 mg/kg of benzidine given subcutaneously for 15 days produced tumors in
20 of 22 rats, including hepatomas, cholangiomas, intestinal tumors, and
sebaceous gland carcinomas (Holland et al. 1974, as reported in USEPA
1980).  Hepatomas have been reported in mice given subcutaneous injections of
benzidine (USEPA 1980).

    In addition to its carcinogenic activity, benzidine also causes a
reduction in catalase and peroxidase activity, a reduction in erythrocytes and
thrombocytes, and an increase in leukocytes when injected in rats (Soloimskaya
1968, as reported in USEPA 1980).  Neish (1967, as reported in USEPA 1980)
reported that an intraperitoneal dose of 12.7 mg/kg in rats increased liver
glutathione levels.  Benzidine is mutagenic in the Ames assay with Salmonella
typhimurium and gave positive results in a DNA synthesis inhibition test with
HeLa cells (USEPA 1980).

    Limited toxicity data are available for aquatic organisms.  The 96-hour
LC50 for rainbow trout and lake trout, red shiner, and the flagfish range from
2,500 to 16,200 yg/liter.  Chronic toxicity data for freshwater organisms
are not available.  No saltwater organisms have been tested with benzidine
(USEPA 1980).

    EPA has established an ambient water quality criterion of zero for maximum
protection of human health from the potential carcinogenic effects due to
exposure to benzidine through the ingestion of contaminated water and aquatic
organisms.  However, since the zero level may not be attainable at the present
time, a level of 0.00012 yg/liter corresponding to a lifetime incremental
cancer risk of 0.000001 was recommended.

    EPA has not yet established an aquatic life water quality criterion for
benzidine.
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    3,4-Benzofluoranthene

    3,4-Benzofluoranthene is a member of the class of polynuclear aromatic
hydrocarbons (PAHs).  Many members of this class of chemicals are
carcinogenic.  3,4-Benzofluoranthene has produced skin tumors in mice
following repeated skin painting.  Three groups of mice were painted with
0.01, 0.1, or 0.5% solutions of 3,4-benzofluoranthene in acetone three times
per week.  After 8-12 months, the incidence of carcinomas in the survivors was
0%, 85%, and 90% (Wynder and Hoffman 1958, as reported in IARC 1973).  In a
later study, a single dermal application of 1 mg in acetone produced no tumors
in mice after 63 weeks; the same procedure followed by repeated paintings with
croton resin produced carcinomas in 5 of 20 mice (Van Duuren et al.  1966, as
reported by IARC 1973).  3,4-Benzofluoranthene also produced sarcomas in mice
at the site of injection after 3 subcutaneous injections of 0.6 mg of the
compound over a two month period (Lacassagne et al. 1963, as reported in
IARC 1973).

    No human case studies or epidemiological studies have been conducted which
establish 3,4-benzofluoranthene as a human carcinogen.  Indirect evidence for
the compound's carcinogenicity comes from air pollution studies which indicate
an excess of lung cancer mortality among workers exposed to high
concentrations of PAH-containing material such as coal gas, tars, soot, and
coke oven emissions (IARC 1973, USEPA 1980).

    No data are available on the aquatic toxicity of 3,4-benzofluoran- thene.

    EPA has not yet established ambient water quality criteria for
3,4-benzofluoranthene itself because of the lack of sufficient data.  However,
the agency has established an ambient water quality criterion of zero for the
maximum protection of human health from the potential carcinogenic effects due
to exposure to polynuclear aromatic hydrocarbons, which include
3,4-benzofluoranthene, through ingestion of contaminated water and aquatic
organisms.  Since the zero level may not be attainable at present, a level of
2.8 ng/liter corresponding to a lifetime incremental cancer risk of 0.000001
was recommended.
    Benzo(k)fluoranthene

    No information is available on the toxic effects of benzo(k)fluoranthene
in humans, animals, or aquatic organisms.

    EPA has not yet established ambient water quality criteria for
benzo(k)fluoranthene because of the lack of sufficient data.   However, the
agency has established an ambient water quality criterion of zero for the
maximum protection of human health from the potential carcinogenic effects due
to exposure to polynuclear aromatic hydrocarbons, which include
benzo(k)fluoranthene, through ingestion of contaminated water and aquatic
organisms.  Since a zero level may not be obtainable at present, a level of
2.8 ng/liter, corresponding to a lifetime incremental cancer risk of 0.000001,
was recommended.
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    Benzo(g,h,i)perylene

    Benzo(g,h,i)perylene is a member of the class of polynuclear aromatic
hydrocarbons (PAHs), many of which are known for their ability to induce
cancer.

    No data are available on the aquatic or mammalian toxicity of
benzo(g,h,i)perylene.  This compound has not been identified as a carcinogen;
however, benzo(g,h,i)perylene acted as a cocarcinogen when applied with
benzo(a)pyrene, a known carcinogen, to the skin of mice at a dose of 2 mg, 3
times per week, for 52 weeks (Van Duuren et al. 1973 and 1976, as reported
in USEPA 1980).

    EPA has not yet established ambient water quality criteria for
benzo(g,h,i)perylene because of the lack of sufficient data.  However, the
agency has established an ambient water quality criterion of zero for the
maximum protection of human health from the potential carcinogenic effects due
to exposure to polynuclear aromatic hydrocarbons through ingestion of
contaminated water and contaminated aquatic organisms.   Since a zero level may
not be attainable at present, a level of 2.8 ng/liter corresponding to a
lifetime incremental cancer risk of 0.000001 was recommended.
    Benzo(a)pyrene

    Benzo(a)pyrene is a member of the class of polynuclear aromatic
hydrocarbons (PAHs) and is a well-known animal carcinogen.  Administration of
50-250 ppm in the diet to mice for 122 to 197 days resulted in a greater than
70 percent incidence of stomach tumors (Neal and Ridgon 1976, as reported in
IARC 1973).  Leukemias, lung adenomas, and stomach tumors were produced in
mice by dietary administration of 250 ppm benzo(a)pyrene for 140 days (Rigdon
and Neal, 1969, as reported in IARC 1973).  In hamsters and rats, oral
administration of benzo(a)pyrene produced tumors of the esophagus,
forestomach, and intestine (IARC 1973).

    Benzo(a)pyrene is also carcinogenic when administered by intratracheal
instillation.  Instillation of 3.25 to 52 mg once weekly for 52 weeks in
Syrian golden hamsters produced a respiratory tract tumor incidence of 10 to
93 percent (Feron et al. 1973, as reported in USEPA 1980).

    Many experiments have been conducted involving repeated application to the
skin or subcutaneous and intramuscular injection.  In skin painting studies,
the threshold dose to induce tumors is dependent on the species and strain of
animal tested and the vehicle used.  Thrice weekly applications of
benzo(a)pyrene in acetone to CAF1 mice produced papillomas and carcinomas at a
concentration as low as 0.001% benzo(a)pyrene (Wynder et al. 1957, as
reported in IARC 1973).  In a subcutaneous carcinogenicity study using C57
mice, injection of benzo(a)pyrene in oil at doses of 0.00004, 0.0004, 0.004,
and 0.04 mg produced sarcomas in, respectively, 0, 1, 5, and 23 mice of groups
of 50 (Hieger 1959, as reported in IARC 1973).

    Little information on other potential toxic effects of benzo(a)pyrene is
available.  Benzo(a)pyrene has been shown to have little effect on fertility
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or on the developing embryo in several mammalian and nonmammalian studies
(USEPA 1980).  Benzo(a)pyrene induced damage to the bronchial epithelium of
Syrian golden hamsters in animals treated intratracheally with 0.63 mg
benzo(a)pyrene (total dose) dispersed in various vehicles once weekly for life
(Reznik-Schuller and Mohr 1974,  as reported in USEPA 1980).

    No human case studies or epidemiologic studies have been conducted which
establish benzo(a)pyrene as a human carcinogen.  Indirect evidence for the
compound's carcinogenicity comes from air pollution studies  which indicate an
excess of lung cancer mortality among workers exposed to high concentrations
of PAH-containing material such as coal gas, tars, soot, and coke-oven
emissions (IARC 1973, USEPA 1980).

    No data are available on the aquatic toxicity of benzo(a)pyrene.

    EPA has not yet established ambient water quality criteria for
benzo(a)pyrene because of the lack of sufficient data.   However, the agency
has established an ambient water quality criterion of zero for the maximum
protection of human health from the potential carcinogenic effects due to
exposure to polynuclear aromatic hydrocarbons through ingestion of
contaminated water and aquatic organisms.  Since the zero level may not be
attainable at present, a level of 2.8 ng/liter corresponding to a lifetime
incremental cancer risk of 0.000001 was recommended.
    Bis(2-chloroethoxy) methane

    No toxicity data for bis(2-chloroethoxy) methane in humans are available,
and only limited acute toxicity information in animals has been published.
Acute LD50 values for the rat by oral administration and for the guinea pig by
dermal administration have been given as 65 mg/kg and 170 mg/kg, respectively
(NIOSH 1980).  Unspecified toxic effects were observed in rats exposed to 62
ppm bis(2-chloroethoxy) methane vapors for four hours (NIOSH 1980).  No
chronic studies for this compound have been conducted.

    No aquatic toxicity data are available for bis(2-chloroethoxy) methane.
Available data for the class of chloroalkyl ethers indicate that acute
toxicity to freshwater aquatic life occurs at concentrations as low as 238
mg/liter (USEPA 1980).

    EPA has not yet established ambient water quality criteria for
bis(2-chloroethoxy) methane because of the lack of sufficient data.


    Bis(2-chloroethyl) Ether

    Bis(2-chloroethyl) ether is moderately persistent and insoluble in water.
Toxic effects of exposure to bis(2-chloroethyl) ether have been observed  in
humans.  Exposure to 550 ppm was intolerable and caused irritation of the eyes
and nasal passages.  Bis(2-chloroethyl) ether can also affect the kidney  and
liver (Sax 1975).
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    A wide variety of acute effects has been observed in animals.  Guinea pigs
exposed to 500-1,000 ppm by inhalation immediately developed severe eye and
nasal irritation and in 3 hours developed respiratory disturbances and death
with pulmonary lesions.  Autopsy revealed congestion of the lungs and upper
respiratory tract, pulmonary edema, and congestion of the liver, brain, and
kidney (Schrenk et al.  1933, as reported in USEPA 1980).  Oral LDSOs have
been reported as 75-150 mg/kg for rats, 136 mg/kg for mice, and 126 mg/kg for
rabbits.   Only mild physiological stress has been observed in animals exposed
chronically to bis(2-chloroethyl) ether.  Bis(2-chloroethyl) ether at 300
mg/kg administered orally or by intraperitoneal injection for 80 weeks
produced an increased incidence of liver tumors in mice (Innes et al. 1969,
as reported in USEPA 1980).

    No information is available on the toxic effects of bis(2- chloroethyl)
ether on aquatic fish or plant life (USEPA 1980).

    EPA has established an ambient water quality criterion of zero for the
maximum protection of human health from the potential carcinogenic effects due
to exposure to bis(2-chloroethyl) ether through ingestion of contaminated
water and contaminated aquatic organisms.  Since the zero level may not be
attainable at the present time, a level of 0.030 yg/liter, corresponding to
a lifetime incremental risk of 0.000001, was recommended.

    EPA has not yet established an aquatic life water quality criterion for
bis(2-chloroethyl) ether.


     Bis(2-chloroisopropyl) Ether

    No evidence of human toxicity from exposure to bis(2-chloro- isopropyl)
ether is available.  Acute toxicity of bis(2-chloroisopropyl) ether has been
reported in rats exposed by inhalation to 350 ppm for eight, 5-hour
exposures.  Toxic effects included respiratory difficulty, lethargy, retarded
weight gain, and congestion of the liver and kidneys.  Lethargy and retarded
weight gain were also observed in rats exposed to 70 ppm for 20, 6-hour
exposures (Gage 1979, as reported in USEPA 1980).  An oral LD50 for the rat
was established as 240 mg/kg and a dermal LD50 for the rabbit is reported as
3,000 mg/kg (Smyth et al. 1951, as reported in USEPA 1980).

    In a chronic oral toxicity study, the major toxic effects observed in the
rat exposed to 200 mg/kg/day for a total of 728 days were on the lungs, where
congestion, pneumonia,  and aspiration were noted.  Centrilobular necrosis of
the liver, hyperkeratosis of the esophagus, and agiectasis of the adrenal
cortex were also reported.  In this same experiment, mice exposed to 10
mg/kg/day also developed centrilobular necrosis of the liver (NCI, unpublished
as reported in USEPA 1980).  Bis(2-chloroisopropyl) ether is mutagenic in in
vitro assays (USEPA 1980).  Tumors were induced by bis(2-chloroisopropyl)
ether in rats and mice fed 200 and 25 mg/kg/day respectively for 5 days per
week for two years.  However, the significance of this result has not been
fully determined because of high tumor incidence in controls (NCI, unpublished
as reported in USEPA 1980).
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    No information is available on the toxicity of bis(2-chloroisopropyl)
ether on aquatic organisms (USEPA 1980).

    EPA has established a limit of 3.47 yg/liter for the protection of human
health against the toxic properties of bis(2-chloroisopropyl) ether through
ingestion of water and contaminated aquatic organisms.

    EPA has not yet established an aquatic life water quality criterion for
bis(2-chloroisopropyl) ether.
    Bis-2-ethylhexyl Phthalate

    Toxic effects of bis-2-ethylhexyl phthalate in humans have not been
reported.  In chronic animal studies, liver and kidney weights increased in
both the parental (PI) generation of rats fed 0.4% bis-2-ethylhexyl phthalate
for a maximum of 2 years and in their offspring also fed 0.4% bis-2-ethylhexyl
phthalate for 1 year; and in a second study, at 0.5% for up to 2 years
(Carpenter 1953 and Harris et al. 1956, as reported in USEPA 1980).  Liver
damage was reported in monkeys exposed to bis-2-ethylhexyl phthalate
solubilized in blood (administered as transfusions) in concentrations ranging
from 6.6 to 33 mg/kg for periods ranging from 6 months to 1 year (Kevy et
al. 1978, as reported in USEPA 1980).  Tubular atrophy and degeneration in
the testes were observed in rats administered bis-2-ethylhexyl phthalate in
the diet at 1.5 and 3.0% for 90 days (Shaffer et al. 1945, as reported in
USEPA 1980).  Oral LD50 values have been reported in the rat as 26.0 mg/kg,
and in the rabbit as 34.0 mg/kg.  A dermal LD50 has been reported in the
guinea pig as 10.0 mg/kg (Autian 1973, as reported in USEPA 1980).
Dose-related skeletal abnormalities and reduced fetal weight were reported in
rats administered 5 ml/kg bis-2-ethylhexyl phthalate by intraperitoneal
injection during days 5, 10, and 15 of gestation (Singh et al. 1972, as
reported in USEPA 1980).

    In a recent National Cancer Institute/National Toxicology Program bioassay
(NTP 1982), bis-2-ethylhexyl phthalate was carcinogenic to both rats and mice
fed diets containing the test chemical at concentrations of 6,000 or 12,000
ppm (rats) and 3,000 or 6,000 ppm (mice) for 103 weeks.  An increased
incidence of hepatocellular carcinomas was observed in high dose female rats
and male mice and in both groups of female mice.  In addition, degeneration of
the seminiferous tubules was observed in the high-dose male rats and mice, and
hypertrophy of the cells in the anterior pituitary was found in the high-dose
male rats.

    In freshwater aquatic life 48-hour LC50 values ranging from 1 to 5
mg/liter, for Daphnia magna and greater than 18 mg/liter for the midge have
been reported.  The 96-hour LC50 values were reported as greater than 32
mg/liter for the scud and greater than 770 mg/liter for the bluegill.
Significant increase in total body protein catabolism was reported in rainbow
trout exposed to 14-54 yg/liter for 24 days.  Bis-2-ethylhexyl phthalate at
100 yg/g in the diet of the guppy caused an increase in abortions.
Significant reproductive impairment in Daphnia magna was reported after
chronic exposure to bis-2-ethylhexyl phthalate at 3 yg/liter.  No other
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information was available on the chronic toxic effects of bis-2-ethylhexyl
phthalate or on its toxic effects in aquatic plantlife (USEPA 1980).

    EPA has established an ambient water quality criterion of 15 mg/liter for
the protection of human health from the toxic properties of bis-2-ethylhexyl
phthalate ingested through water and contaminated aquatic organisms.

    EPA has not yet established an aquatic life water quality criterion for
bis-2-ethylhexyl phthalate.


    4-Bromophenyl Phenyl Ether

    No human or mammalian toxicity data are available for 4-bromophenyl phenyl
ether.

    Limited aquatic toxicity data are available for 4-bromophenyl phenyl
ether.  For Daphnia magna, the 48-hour EC50 is 360 ug/liter, and the
96-hour LC50 for the bluegill is 4,940 yg/liter.  In an embryo-larval test
with the fathead minnow, adverse effects on survival and growth were observed
at 122 ug/liter (USEPA 1980).

    EPA has not yet established ambient water quality criteria for
4-bromophenyl phenyl ether because of the lack of sufficient data.


    Butyl Benzyl Phthalate

    Butyl benzyl phthalate is not known to be toxic to humans.  A Russian
report suggests that certain phthalate esters such as dibutyl phthalate and
butyl benzyl phthalate have caused polyneuritis in industrial workers (Milkov
et al. 1973, as reported in Doull et al. 1980); however, similar
observations have not been reported in this country (Doull et al. 1980).

    Phthalate esters are considered as having a low order of acute toxicity in
animal studies.  The only reported LD50 value for butyl benzyl phthalate is
that reported for the mouse by intraperitoneal injection of 3.16 g/kg (Autian
1973, as reported in USEPA 1980).  When single doses of butyl benzyl phthalate
were administered to groups of rats either orally (1.8 g/kg) and
intraperitoneally (4 g/kg), the animals died after four to eight days
(Mallette and Von Hamm 1952, as reported in USEPA 1980).  Histopathological
studies demonstrated toxic splenitis and degeneration of central nervous
system tissue with congestive encephalopathy.  Myelin and glial proliferation
were also reported.  Most phthalate esters are precluded from presenting an
acute toxic response by inhalation because of their low volatility (USEPA
1980).  No chronic or subchronic toxicity data are available for butyl benzyl
phthalate.

    The LC50 values for butyl benzyl phthalate have been reported for three
fish and one invertebrate species ranging from 1,700 ug/liter for the
bluegill to 92,300 ug/liter for Daphnia magna (USEPA 1980).  For two
saltwater species, acute toxic values were reported for the raysid shrimp of
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900 and 9,630 yg/liter and for the sheepshead minnow of 3,000 and 445,000
ug/liter.  The lower values were obtained using a solvent in which the
chemical is more soluble and thus presumably more available (USEPA 1980).
Chronic studies have been conducted with two freshwater species.  In a
life-cycle study of Daphnia magna, effects were observed at 440 yg/liter,
and in an early life stage test with the fathead minnow, an acute value of 220
was reported (USEPA 1980).  EC50 values for freshwater algae showed wide
variation in toxicity, with a range of 110 to 1,000,000 yg/liter (USEPA
1980).

    EPA has not yet established ambient water quality criteria for butyl
benzyl phthalate because of the lack of sufficient data.


    2-Chloronaphthalene

    Little toxicity information is available on 2-chloronaphthalene.   As a
class, chlorinated naphthalenes have been associated with the development of
chloracne in humans, and, in some cases, fatal liver disease.   It has been
demonstrated, however, that monochloronaphthalenes did not produce chloracne
in a test with dermal application to the inner side of the rabbit ear (Adams
et al. 1941, as reported in Clayton and Clayton 1981).

    EPA has not yet established ambient water quality criteria for
2-chloronaphthalene because of the lack of sufficient information.
    4-Chlorophenyl Phenyl Ether

    The only available toxicity data on 4-chlorophenyl phenyl ether is that
reported for experimental animals by Hake and Rowe (1963, as reported in USEPA
1980) for various chlorinated phenyl ethers.  For an unspecified monochloro
phenyl ether, the lethal oral dose within four days of dosing in guinea pigs
was given as 700 mg/kg.  The "survival dose" was reported as 200 mg/kg.
Within 30 days of the single oral dosing, the "lethal" and "survival" doses
were reported to be 600 and 100 mg/kg, respectively.   Hake and Rowe also
reported that 19 daily oral doses of 100 mg/kg/day of a monochloro phenyl
ether over a 29-day period produced no effects in rabbits.  Because of
inadequate experimental detail, these results are difficult to interpret
(USEPA 1980).

    No aquatic toxicity information is available for 4-chlorophenyl phenyl
ether.  Available data for haloethers indicate that acute and chronic toxicity
to freshwater aquatic life occur at concentrations as low as 360 and 122
yg/liter , respectively (USEPA 1980).

    EPA has not yet established ambient water quality criteria for
4-chlorophenyl phenyl ether because of the lack of sufficient data.
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    Chrysene

    No information is available on the toxicity of chrysene in humans.  In one
experimental study, Swiss mice painted three times weekly with a 1% solution
of chrysene in acetone developed skin cancer.  This effect was not repeatable
in other studies however, and the carcinogenicity of chrysene has not been
clearly determined (IARC 1973).

    No information is available on the toxic effects of chrysene on aquatic
organisms.  However, chrysene was reported to bioconcentrate 8.2 times in
clams over 24 hours (USEPA 1980).

    EPA has not yet established ambient water quality criteria for chrysene
because of the lack of sufficient data.  However, the agency has established
an ambient water quality criterion of zero for the maximum protection of human
health from the potential carcinogenic effects due to exposure to polynuclear
aromatic hydrocarbons, which include chrysene, through ingestion of
contaminated water and contaminated aquatic organisms.  However, since a zero
level may not be attainable at present, a level of 2.8 ng/liter, corresponding
to a lifetime incremental cancer risk of 10-6, was recommended.
    Dibenzo(a,h)anthracene

    Dibenzo(a,h)anthracene (DB(a,h)A) is a member of the class of polynuclear
aromatic hydrocarbons (PAHs) and was the first pure chemical compound shown to
be carcinogenic (IARC 1973).  When DB(a,h)A was administered to mice as an
aqueous-oil emulsion in the place of drinking water at an average dose of
0.76-0.85 mg/day, all surviving mice at 200 days had respiratory tract tumors
and 12 of 13 females had mammary carcinomas (Snell and Stewart 1962, as
reported in IARC 1973).   A single dose of 1.5 mg DB(a,h)A in polyethylene
glycol produced forestomach papillomas in 2 of 42 male mice within 30 weeks
(Berenblum and Haran 1955, as reported in IARC 1973).

    Many studies have reported the induction of skin tumors from application
of DB(a,h)A.  Thrice weekly paintings with solutions containing 0.001, 0.01,
and 0.1% DB(a,h)A produced skin carcinomas in one of 30 mice, 43 of 50 mice,
and 39 of 40 mice, respectively (Van Duuren et al. 1967, as reported in IARC
1973).  In a subcutaneous injection study, single injections of DB(a,h)A at
doses ranging from 0.00019 to 8 mg produced incidences of local sarcomas of
2.5% to 100% (IARC 1973).  In in vitro hamster embryo cell transformation
studies, DB(a,h)A at concentrations of 2.5 to 10 yg/ml did not produce any
compound-related increase in cell transformations; however, the 5,6-epoxide of
DB(a,h)A did produce a dose-related increase in cell transformations (Grover
et al. 1971, Huberman et al. 1972, as reported in USEPA 1980).  High doses
of DB(a,h)A have been reported to produce an immunosuppressive effect in mice
(Malmgren et al. 1952, as reported in USEPA 1980).

    No human case studies or epidemiological studies have been conducted which
establish DB(a,h)A as a human carcinogen.  Indirect evidence for the
compound's carcinogenicity comes from air pollution studies which indicate an
excess of lung cancer mortality among workers exposed to high concentrations
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of PAH-containing material such as coal gas, tars, soot, and coke-oven
emiss-ions (IARC 1973, USEPA 1980).

    No data are available on the aquatic toxicity of DB(a,h)A.

    EPA has not yet established ambient water quality criteria for DB(a,h)A
because of the lack of sufficient data.  However, the agency has established
an ambient water quality criterion of zero for the maximum protection of human
health from the potential carcinogenic effects due to exposure to polynuclear
aromatic hydrocarbons, which include DB(a,h)A, through ingestion of
contaminated water and aquatic organisms.  Since the zero level may not be
attainable at present, a level of 2.8 ng/liter corresponding to a lifetime
incremental cancer risk of 0.000001 was recommended.
    Di-n-butyl Phthalate

    Occupational exposure to di-n-butyl phthalate has been associated with
toxic polyneuritis (Milkov et al. 1973, as reported in USEPA 1980).
Abnormal encephalographic responses were observed in three workers exposed to
0.12-0.15 mg/cu m (Men'shikova 1971, as reported in USEPA 1980).

    In animal studies, testicular atrophy has been reported in rats
administered 2,000 mg/kg orally "for a period of time."  Significant weight
loss of the testes was observed after 14 days.  Zinc metabolism was also
affected as evidenced by increased zinc levels in the urine (Carter et al.
1977, as reported in USEPA 1980).  In an inhalation experiment, a dose-related
increase in gamma globulin was observed in rats exposed to concentrations
ranging from 0.098-0.98 mg/cu m, continuously for 93 days (Men'shikova 1971,
as reported in USEPA 1980).  In a feeding study, 50% of rats fed 1.25%
di-n-butyl phthalate in the diet died in the first week of administration
following one year exposure to levels up to 0.25% (Smith 1953, as reported in
USEPA 1980).   A dermal LD50 for rabbits has been reported as 20 ml/kg (Autian
1973, as reported in USEPA 1980).  Dose-related skeletal abnormalities and
reduced fetal weight were reported in the offspring of rats administered 1/10,
1/5, and 1/3 the LD50 value of 3.05 ml/kg di-n-butyl phthalate, by
intraperitoneal injection during days 5, 10, and 15 of gestation (Singh e_t
al. 1972, as reported in USEPA 1980).

    The acute toxicity of di-n-butyl phthalate on fresh water aquatic
organisms is reflected by 96-hour LC50 values for scud (2.1 mg/liter), midge
(4.0 mg/liter), rainbow trout (6.47 mg/liter), fathead minnow (1.3 mg/liter),
and bluegill (0.73-1.2 mg/liter).  Crayfish were less sensitive, having an
LC50 greater than 10 mg/liter.  No information is available on the toxic
effects in saltwater organisms or the chronic effects in any aquatic
organisms.  Di-n-butyl phthalate was reported to be extremely toxic to plant
life, causing toxic effects in algae in concentrations as low as 3.4
ug/liter (USEPA 1980).

    EPA has established an ambient water quality criterion of 34 mg/liter for
the protection of human health from the toxic properties of di-n-butyl
phthalate ingested through contaminated water and contaminated aquatic
organisms.
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    EPA has not yet established an aquatic life water quality criterion for
di-n-butyl phthalate.
    1,2-Dichlorobenzene

    The acute toxic effects on humans following exposure to
1,2-dichlorobenzene include eye and upper respiratory tract irritation when
inhaled (Dupont 1938, as reported in USEPA 1980), and skin irritation and
burning when absorbed through the skin (Reidel 1941, as reported in USEPA
1980).  Chronic exposure to 1,2-dichlorobenzene produced weakness, fatigue,
nausea, headaches, peripheral lymphadenopathy, chronic lymphoid leukemia,
acute myeloblastic leukemia, acute hemolytic anemia, leukocytosis, and bone
marrow hyperplasia under different conditions of exposure (Girard et al.
1969 and Gadrat et al. 1962, as reported in USEPA 1980).  Chronic skin
contact resulted in contact eczematoid dermatitis, erythema, and edema  (Dowing
1939, as reported in U.S. EPA 1980).

    Acute toxic effects were observed in rats exposed to a 4,800 mg/cu m
concentration of 1,2-dichlorobenzene (Cameron et al.  1937 in USEPA 1980).
In this study, nasal and ocular irritation, drowsiness, massive liver
necrosis, coma, and death occurred after exposure by inhalation for 11-50
hours.  Rats (2,138 mg/kg), mice (2,000 mg/kg), rabbits (1,875 mg/kg), and
guinea pigs (3,375  mg/kg) exposed to different levels of 1,2-dichlorobenzene
in single doses by stomach tube developed acute poisoning manifestations
including hyperemia of the mucous membranes, adynamia, ataxia, paraparesis,
paraplegia, dyspnea, and death due to central respiratory paralysis
(Varshavskaya 1967, as reported in USEPA 1980).  On necropsy, enlarged
necrotic livers, and brain, stomach, and kidney edema were observed in these
animals.  Chronic exposure to 1,2-dichlorobenzene at levels of 0.0010.1
mg/kg/day predominantly affected the hematopoietic system after 5 months
(preliminary report, Varshavskaya 1967, as reported in USEPA 1980).  In this
report, rats fed 0.1 mg/kg developed disturbances of higher cortical function
in the central nervous system, inhibition of erythropoiesis, thrombocytosis,
neutropenia, and inhibition of bone marrow mitotic activity.  Hepatic
prophyria was induced in rats fed 455 mg/kg 1,2-dichlorobenzene by stomach
tube daily for 15 days.  Severe liver damage with intense necrosis and fatty
changes were observed (Rimington and Ziegler 1963, as reported in USEPA
1980).  1,2-Dichlorobenzene was not mutagenic in the Salmonella typhimurium
assay (Anderson e_t al. 1972, as reported in USEPA 1980).  No information is
available on the teratogenicity of 1,2-dichlorobenzene, and the carcinogenic
potential of 1,2-dichlorobenzene has not been established (USEPA 1980).

    The acute toxicity of 1,2-dichlorobenzene to freshwater aquatic organisms
has been demonstrated in the bluegill and cladoceran with 96-hour LC50 values
of 5.59-27 and 2.44 mg/liter, respectively.  Chronic toxicity was observed in
fathead minnows in concentrations ranging from 1.6 to 2.5 mg/liter.  Plant
toxicity was demonstrated in freshwater algae at 91.6-98 mg/liter.  Saltwater
organisms affected by 1,2-dichlorobenzene include tidewater silverside,
sheepshead minnows, and rays id shrimp.  LD50 values are 7.3, 9.66, and 1.97
mg/liter, respectively.  Emergence from parasitized oysters was observed in
the polychaete worm at concentrations of 100 mg/liter.  Saltwater algae were
affected at 44.1 mg/liter (USEPA 1980).
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    EPA has established an ambient water quality criterion of 400 yg/liter
for the protection of human health from the toxic properties of total
dichlorobenzenes including 1,2-dichlorobenzene ingested through water and
contaminated aquatic organisms.

    EPA has not yet established an aquatic life water quality criterion for
1,2-dichlorobenzene.
    1,3-Dichlorobenzene

    No information is available on the human or animal effects which result
from exposure to 1,3-dichlorobenzene.

    The acute toxicity of 1,3-dichlorobenzene to aquatic organisms is
reflected in the 96-hour LC50 values of 5.02 mg/liter for the bluegill, 7.79
mg/liter for the fathead minnow, 28.1 mg/liter for the cladoceran, 2.85
mg/liter for the mysid shrimp, and 7.77 mg/liter for the sheepshead minnow.
Chronic toxicity has been observed in the fathead minnow in concentrations
ranging from 1 to 2.27 mg/liter.  Algae are affected by concentrations ranging
from 46.9 to 179 mg/liter, depending on the species (USEPA 1980).

    EPA has established an ambient water quality criterion of 400 yg/liter
for the protection of human health from the toxic properties of total
dichlorobenzenes, including 1,3-dichlorobenzene, through ingestion of
contaminated water and aquatic organisms.

    EPA has not yet established an aquatic life water quality criterion for
1,3-dichlorobenzene.
    1,4-Dichlorobenzene

    1,4-Dichlorobenzene is toxic to mammals, birds, and aquatic organisms and
imparts an offensive taste and odor to water.  Human exposure to
1,4-dichlorobenzene is associated with leukemia and other blood dyscrasias,
liver necrosis, and eye irritation.  Symptoms of exposure include headaches,
weakness, nausea, jaundice, and anemia (Sumers et al. 1952, Cotter 1953,
Perrin 1941, Hallowell 1959, Campbell and Davidson 1970, Nalbandian and Pierce
1965, as reported in USEPA 1980).

    Acute inhalation studies in rabbits exposed to 100 gm/cu m for 30 minutes
daily caused central nervous system depression, and occular and nasal
irritation; rats similarly exposed developed irritation and narcosis while
guinea pigs exposed under the same conditions developed irritation, central
nervous system depression and deaths (Domenjoz 1946, as reported in USEPA
1980).  Rats and guinea pigs administered 500 mg/kg by stomach tube developed
centrilobular hepatic necrosis and marked cloudy swelling of renal tubular
epithelium; no effects were observed at 10 and 100 mg/kg (Hollingsworth et
al. 1956, as reported in USEPA 1980).

    In subchronic studies, rabbits subjected by inhalation to
1,4-dichlorobenzene at approximately 800 ppm for 8-hour periods, 5 days per
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week for as long as 12 weeks, developed tremors, weakness, nystagmus, and
reversible nonspecific eye changes (Pike 1944, as reported in NAS 1977).
Rabbits fed 1,000 mg/kg for 5 days per week developed similar toxicity
symptoms after several months (Pike 1944, as reported in NAS 1977).

    Rats and guinea pigs exposed at 2,050 mg/cu m, 5 hours per day, 5 days per
week for 6 months displayed growth depression (guinea pigs); liver pathology
including cloudy swelling, fatty degeneration, focal necrosis, and cirrhosis;
and increased liver and kidney weights (rats only) (Ho11ingsworth et a1.
1956, as reported in USEPA 1980).

    The acute toxicity of 1,4-dichlorobenzene on aquatic organisms is
reflected in 96-hour LC50 values of 11 mg/liter for the cladoceran, 13
mg/liter for the midge, 1.12 mg/liter for the rainbow trout, 4 mg/liter for
the fathead minnow, 4.28 mg/liter for the bluegill, 1.99 mg/liter for the
mysid shrimp, and 7.4 mg/liter for the sheepshead minnow.  Chronic toxicity
was observed in the fathead minnow exposed to concentrations ranging from 5.6
to 1.04 mg/liter in the embryo-larval test.  Algae were affected by
concentrations ranging from 54.8-98.1 mg/liter, depending on the species
(USEPA 1980).

    EPA has established an ambient water quality criterion of 400 yg/liter
for the protection of human health from the toxic properties of total
dichlorobenzenes including 1,4-dichlorobenzene through ingestion of
contaminated water and contaminated aquatic organisms.

    EPA has not yet established an aquatic life water quality criterion for
1,4-dichlorobenzene.


    3,3*-Dichlorobenzidine

    3,3'-Dichlorobenzidine has not been shown to be toxic in humans.  Three
epidemiological studies of industrial exposure to 3,3*-dichlorobenzidine have
been conducted by Gerarde and Gerarde (1974) in the United States, by
Maclntyre (1975) and Gadian (1975) in Great Britain, and by Akiyama (1970) in
Japan (all as reported in USEPA 1980).  The studies do not provide any
evidence that 3,3*-dichlorobenzidine induces bladder cancer, the
characteristic lesion induced by carcinogenic aromatic amines such as
benzidine used in the dye and pigment industry.  The evidence is not, however,
conclusive since the populations studied have been small, tumors may not have
appeared at the time of the study because of a long latent period, and the
focus of the studies has been solely on bladder cancer as the lesion of
interest (USEPA 1980).

    In rats, the oral LD50 for 3,3'-dichlorobenzidine is 488 for females and
676 for males (Gaines and Nelson 1977, as reported in USEPA 1980).  Pliss
(1959, as reported in USEPA 1980) injected rats subcutaneously with 120 mg of
3,3*-dichlorobenzidine and observed a state of excitation and short-lived
convulsions.  Exposure of rats to a concentrated atmospheric dust of
3,3*-dichlorobenzidine dihydrochloride for 14 days results in slight to
moderate pulmonary congestion; the actual concentration of the compound was
not measured (Gerarde and Gerarde 1974, as reported in USEPA 1980).  However
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HC1 may have caused or contributed to the observed pulmonary effects.  Freeman
et al. (1973, as reported in USEPA 1980) reported that 3,3*-dichlorobenzi-
dine at concentrations of 5 ppm or greater was cytotoxic to embryonic rat
cells in culture.

    3,3'-Dichlorobenzidine has not been shown to be teratogenic.  However, the
compound has been demonstrated to increase significantly the incidence of
leukemia in the offspring of pregnant female mice given doses of 8 to 10 mg by
subcutaneous injection during the last week of gestation (Golub et al. 1974,
as reported in USEPA 1980).   When tested for mutagenicity in the Ames assay
using several strains of bacteria, 3,3'-dichlorobenzidine caused frameshift
and base-pair substitution mutations (USEPA 1980).  3,3*-Dichlorobenzidine. is
carcinogenic in experimental animals.  Male and female rats fed the chemical
at 1,000 mg/kg diet for up to 488 days developed significantly increased
incidences (p <0.05) of mammary adenocarcinomas, granulocytic leukemia
(males only), and Zymbal's gland carcinomas (males only) (Stula et al. 1975,
as reported in USEPA 1980).   3,3'-Dichlorobenzidine added to the feed of rats
for 12 months (total dose of 4.63 g/rat) resulted in a wide variety of tumors
in 22 of 29 surviving animals (Pliss 1959, as reported in USEPA 1980).
Papillary transitional cell carcinomas of the urinary bladder and hepatic
carcinomas were induced in female beagle dogs given oral doses of 100 mg of
3,3*-dichlorobenzidine, three times per week for six weeks, then five times
per week for up to 7.1 years.  Tumors of these types were not found in
controls (Stula et al. 1978, as reported in USEPA 1980).

    No aquatic toxicity data are available for 3,3*-dichlorobenzidine.

    EPA has established an ambient water quality criterion of zero for the.
maximum protection of human health from the potential carcinogenic effects due
to exposure to 3,3*-dichlorobenzidine through ingestion of contaminated water
and aquatic organisms.  Since the zero level may not be attainable at the
present time, a level of 0.010 yg/liter, corresponding to a lifetime
incremental cancer risk of 0.000001, was recommended.

    EPA has not yet established an aquatic life water quality criterion for
3,3'-dichlorobenzidine.
    Diethyl Phthalate

    Diethyl phthalate produces irritation of the mucous membranes of the nasal
passages and the upper respiratory tract in humans when vaporized by heat
(USEPA 1980).

    In animals, diethyl phthalate produced small but significant decreases in
the growth rate of rats exposed for 2 years to 5% diethyl phthalate in the
diet, but no other effects were reported at dosages of 0.5 and 2.5%.  No
adverse effects were reported in dogs fed levels up to 2.5% for 1 year (Food
Research Laboratories, Inc. 1955, as reported in USEPA 1980).  An oral LD50
for rabbits has been reported as 1.0 g/kg (Autian 1973, as reported in USEPA
1980).  Dose-related skeletal abnormalities and reduced fetal weight were
reported in rats administered 1/10, 1/5, and 1/3 of the LD50 value of 5.06
ml/kg diethyl phthalate, by intraperitoneal injection on days 5, 10, and 15 of
gestation (Singh et al. 1972, as reported in USEPA 1980).


                                   H-54

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    The acute toxicity of diethyl phthalate on freshwater aquatic organisms is
reflected by 96-hour LC50 values of 52.1 mg/liter for Daphnia magna and 98.2
mg/liter for bluegill.  The saltwater species, mysid shrimp, gave a 96-hour
LC50 value of 7.59 mg/liter.  Sheepshead minnows were also affected at an LC50
of 29.6 mg/liter (USEPA 1980).

    No information is available on the chronic effects of diethyl phthalate on
aquatic organisms.  Diethyl phthalate is toxic to algae in concentrations
ranging from 3.0 to 90.3 mg/liter (USEPA 1980).

    EPA has established an ambient water quality criterion of 350 mg/liter for
the protection of human health from the toxic properties of diethyl phthalate
ingested through water and contaminated aquatic organisms.

    EPA has not yet established an aquatic life water quality criterion for
diethyl phthalate.
    Dimethyl Phthalate

    Few toxic effects have been observed in humans exposed to dimethyl
phthalate (USEPA 1980).  In animal studies, rats fed for 2 years at levels of
2% and 8% in the diet developed minor growth retardation.  At 8%, some
indication of nephritic damage was observed.  A 90-day LD50 value of 4 ml/kg
was obtained when dimethyl phthalate was applied to the skin of rabbits
(Draize et al. 1948, as reported in USEPA 1980).  Oral LDSOs have been
reported for the mouse (7.2 g/kg), rat (2.4 g/kg), and guinea pig (2-4 g/kg)
(Autian 1973, as reported in USEPA 1980).  Dose-related skeletal abnormalities
and reduced fetal weight were reported in the offspring of rats administered
1/10, 1/5, and 1/3 the LD50 value of 3.38 ml/kg by intraperitoneal injection
during days 5, 10, and 15 of gestation (Singh et al. 1972, as reported in
USEPA 1980).

    The acute toxicity of dimethyl phthalate on freshwater aquatic organisms
is reflected by 96-hour LC50 values for Daphnia magna (33 mg/liter) and
bluegill (49.5 mg/liter).  The saltwater species, mysid shrimp, gave a 96-hour
LC50 value of 73.7 mg/liter, and sheepshead minnow showed an LC50 of 58
mg/liter.  Significant decreases in survival were reported in the larvae of
grass shrimp exposed to 100 mg/liter during active larvae development.  No
information on the chronic effects of dimethyl phthalate on aquatic organisms
is available.  The toxic effect of dimethyl phthalate on plant life occurs at
levels similar to those causing toxic effects on fishlife.  Toxicity occurred
in a wide variety of algae in concentrations ranging from 26.1 to 185 mg/liter
(USEPA 1980).

    EPA has established a water quality criterion of 313 mg/liter for the
protection of human health from the toxic properties of dimethyl phthalate
ingested through contaminated water and contaminated aquatic organisms.

    EPA has not yet established an aquatic life water quality criterion for
dimethyl phthalate.
                                   H-55

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    2,4-Dinitrotoluene

    The acute toxic effects of 2,4-dinitrotoluene in humans include
methemoglobinemia followed by cyanosis (USEPA 1980).  The symptoms of
methemoglobinemia following absorption by inhalation, ingestion, or dermal
absorption of 2,4-dinitrotoluene include headache, vertigo, fatigue, nausea,
dyspnea, tremor, dizziness, loss of weight and appetite, paralysis, chest
pain, shortness of breath, and palpitations.   Many of these symptoms were
observed in workers exposed to 2,4-dinitrotoluene (USEPA 1980).   Acute oral
LD50s for 2,4-dinitrotoluene are 268 and 1,625 mg/kg for rats and mice,
respectively (USEPA 1980).

    The 13 week subacute toxicity of 2,4-dinitrotoluene by oral administration
was studied in dogs, rats, and mice (Ellis et al. 1976 in USEPA 1980).  The
dogs were fed daily doses of 1, 5, and 25 mg/kg, and the rats and mice were
fed dietary concentrations of 0.07, 0.2, and 0.7%.  Toxic effects in dogs and
rats included inhibited muscle coordination in the hind legs, decreased
appetite, and weight loss.  The latter two symptoms were also observed in
mice.  Other symptoms observed in the test species were methemoglobinemia,
anemia with reticulocytosis, lesions in the spleen and liver, demyelination in
the brain, and aspermatogenesis.  The highest dose was lethal to some animals
in all three species, and the lowest dose produced no toxic effect.

    Chronic exposure to 2,4-dinitrotoluene produced benign tumors in rats
(National Cancer Institute 1978, as reported in USEPA 1980).  Rats were fed
average doses of 17.6 and 440 mg/kg/day, and mice were fed doses of 16.3 and
81.5 mg/kg/day for 78 weeks.  Treated male rats at both dose levels.developed
a significantly higher incidence of fibroma of the skin and subcutaneous
tissue (a benign tumor) than their controls.   An increased incidence of
mammary gland fibroadenoma was observed in the high dose female rats.  Certain
rare neoplasms occurred at low incidence in high dose rats, but the study
concluded that these tumors were not compound related.  No tumors were
observed at a statistically significant incidence in mice.   Data available in
the literature on the mutagenicity of 2,4-dinitrotoluene are "limited and
rather confusing" (USEPA 1980).

    The 48-hour EC50 value for 2,4-dinitrotoluene to Daphnia magna  is 35
mg/liter and is 31 mg/liter for the fathead minnow.  No data are available
that describe the toxic effect of 2,4-dinitrotoluene to aquatic plants (USEPA
1980).

    EPA has established an ambient water quality criterion of zero  for the
maximum protection of human health from the potential carcinogenic  effects due
to exposure to 2,4-dinitrotoluene.  Since the zero level may not be attainable
at the present time, a level of 0.11 yg/liter, corresponding to an  estimated
lifetime incremental cancer risk of 10-6, was recommended.

    EPA has not yet established an aquatic life water quality criterion for
2,4-dinitrotoluene.
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    2,6-Dinitrotoluene

    The only toxicity information available on 2,6-dinitrotoluene are oral
LD50 values for the rat of 177 mg/kg and for the mouse of 1,000 mg/kg (USEPA
1980).

    EPA has not yet established ambient water quality criteria for
2,6-dinitrotoluene because of lack of sufficient data.


    Di-n-octyl Phthalate

    Di-n-octyl phthalate is not known to be toxic to humans.  A Russian report
suggests that certain phthalate esters such as dibutyl phthalate and butyl
benzyl phthalate have caused polyneuritis in industrial workers (Milkov et
al.  1973, as reported in Doull et al. 1980); however, similar observations
have not been reported in this country (Doull et al. 1980).

    Phthalate esters are considered as having a relatively low order of acute
toxicity.  A reported oral LD50 for di-n-octyl phthalate in the mouse is 13
g/kg.  LD50 values for the rat by intraperitoneal administration and the
guinea pig by dermal exposure are reported to be 50 ml/kg and 5 ml/kg,
respectively (Autian 1973, as reported in USEPA 1980).  Most phthalate esters
are precluded from presenting an acute toxic response by inhalation because of
their low volatility (USEPA 1980).  In a teratogenicity study, Singh et al.
(1975,  as reported in USEPA 1980) administered eight phthalic acid esters,
including dioctyl phthalate, to rats by intraperitoneal injection on days 5,
10,  and 15 of gestation.  Dioctyl phthalate was administered at doses of 5 and
10 ml/kg.  All of the esters were reported to produce dose-related gross or
skeletal abnormalities and reduced fetal weight, although dioctyl phthalate
had the least adverse effects on embryo-fetal development.  No other chronic
or subchronic data are available for di-n-octyl phthalate.

    Little aquatic toxicity data are available for di-n-octyl phthalate.  In a
26-day early life stage study with rainbow trout, the LC50 was reported to be
139,500 ug/liter.  In 7 to 8-day early life stage studies with redear
sunfish, channel catfish, and the largemouth bass, LC50 values of 6,180, 690,
and 32,900 yg/liter were reported (USEPA 1980).  Available data for the
general class of phthalate esters indicate that acute and chronic toxicity to
freshwater aquatic life can occur at concentrations as low as 940 and 3
yg/liter, respectively.

    EPA has not yet established ambient water quality criteria for di-n-octyl
phthalate because of the lack of sufficient data.


    1,2-Diphenylhydrazine

    No information on the toxicity of 1,2-diphenylhydrazine to humans is
available.

    The oral LD50 of 1,2-diphenylhydrazine in rats is 301 mg/kg (Mason
Research Institute Report 1971, as reported in NAS 1977).  Studies in rats and
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mice have shown that 1,2-diphenylhydrazine produces both benign and malignant
tumors when administered subcutaneously or orally.   Pliss (1974, as reported
in NAS 1977 and USEPA) administered 1,2-diphenylhydrazine by subcutaneous
injection (40 mg/week/rat and 5 mg/week/mouse) and in the diet (30 mg/mouse,
five times per week) for 588 days, and observed an increased incidence of
rhabdomyosarcomas, pulmonary adenomas, leukemia,  and liver tumors in the
mouse, and tumors of the uterus, mammary glands,  Zymbal's gland, liver, and
spleen, and lymphoid leukemias in rats.  In a study by the National Cancel-
Institute (NCI 1978, as reported in USEPA 1980),  mice were fed diets
containing 1,2-diphenylhydrazine at concentrations of 0.008 and 0.04 percent
for males and 0.004 and 0.04 percent for females  for 78 weeks.  Male rats were
fed diets containing 0.008 and 0.03 percent 1,2-diphenylhydrazine and females
0.004 and 0.01 percent.  In rats, 1,2-diphenylhydrazine produced a
significantly increased incidence of hepatocellular carcinomas or neoplastic
nodules in males at both dose levels and females  at the high dose; Zymbal's
gland squamous cell carcinomas in high dose males;  adrenal tumors in high dose
males; and mammary carcinomas in high dose females.  1,2-Diphenylhydrazine
produced hepatocellular carcinomas in high dose female mice, but not in male
mice.

    In a 48-hour EC50 test with Daphnia magna and a 96-hour LC50 test with
the bluegill, toxic values of 4,100 yg/liter and  270 yg/liter,
respectively, were reported (USEPA 1980).  No data are available for any
saltwater species.

    EPA has established an ambient water quality  criterion of zero for the
maximum protection of human health from the potential carcinogenic effects due
to exposure to 1,2-diphenylhydrazine through ingestion of contaminated water
and aquatic organisms.  Since the zero level may  not be attainable at the
present time, a level of 42 ng/liter, corresponding to a lifetime incremental
cancer risk of 0.000001, was recommended.

    EPA has not yet established an aquatic life water quality criterion for
1,2-diphenylhydrazine.


    Fluoranthene

    No information is available on the toxicity of fluoranthene in humans.  In
acute toxicity studies in animals, this compound was found to present a
relatively low degree of toxicity (USEPA  1980).   Fluoranthene does not appear
to be a direct acting carcinogen or mutagen, but  it is a potent cocarcinogen
in animal studies (USEPA 1980).  In skin painting studies, fluoranthene
increased the tumor incidence and reduced the time-to-tumor of mice treated
with benzo(a)pyrene (Van Duuren and Goldschmidt 1976, as reported in USEPA
1980).

    Fluoranthene is acutely toxic to various freshwater and marine organisms.
Bluegill were found to have a 96-hour LC50 value of 3.98 mg/liter.  Daphnia
magna were more resistant, with a 48-hour LC50 of 325 mg/liter.  Fluoranthene
has a 96-hour LC50 value of 40 yg/liter and chronic value of  16 ug/liter
in mysid shrimp.  No data are available on the chronic toxicity of
fluoranthene on freshwater organisms  (USEPA 1980).
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    EPA has established an ambient water quality criterion of 42 ug/liter
for the protection of human health from the toxic properties of fluoranthene
ingested through water and contaminated organisms.

    EPA has not yet established an aquatic life water quality criterion for
fluoranthene.
    Fluorene

    No information is available on the toxic effects of fluorene on humans,
and very little information is available on the effects on animals.  The
carcinogenic potential of fluorene was tested by skin painting and
subcutaneous administration in mice and by feeding and subcutaneous
administration in rats.   Carcinogenicity was not established in any of these
tests (dose, duration unspecified; Hueper and Conway 1964).

    Only one study is available on the toxic effects of fluorene on aquatic
life.  A crude oil extract of fluorene was used in a 96-hour LC50 test on a
polychaete worm.  The LC50 value determined in this test is 1.0 mg/liter
(USEPA 1980).

    EPA has not yet established ambient water quality criteria for fluorene
because of the lack of sufficient data.  However, the agency has established
an ambient water quality criterion of zero for the maximum protection of human
health from the potential carcinogenic effects due to exposure to polynuclear
aromatic hydrocarbons, which include fluorene, through ingestion of
contaminated water and contaminated aquatic organisms.  However, since a zero
level may not be attainable at present, a level of 2.8 ng/liter, corresponding
to a lifetime incremental cancer risk of 10-6, was recommended.
    Hexachlorobenzene

    An outbreak of hexachlorobenzene-induced porphyria cutanea tarda occurred
in Turkey between 1955 and 1959 as a result of human consumption of seed grain
that had been treated with hexachlorobenzene (IARC 1979, USEPA 1980).  More
than 3,000 people were affected by the condition, characterized by blistering
and epidermolysis of the exposed skin, loss of hair, and skin atrophy.  A
mortality rate of 14% was reported within several years, and among breast-fed
infants of mothers whose milk contained hexachlorobenzene, the infant
mortality rate was greater than 95% (Cam 1960, Peters 1976, as reported in
IARC 1979 and USEPA 1980).  There was no evidence of porphyria in Louisiana
residents living near an hexachlorobenzene manufacturing plant and whose
average plasma hexachlorobenzene levels were 3.6 yg/liter; however, plasma
coproporphyrin levels were abnormally high (Burns and Miller 1975, as reported
in IARC 1979 and USEPA 1980).

    In experimental animals, the acute toxicity of hexachlorobenzene is
relatively low.  The oral LD50 in rats varies from 3,500 to 10,000 mg/kg
(Booth and McDowell 1975, as reported in IARC 1979).  With prolonged moderate
exposure, hexachlorobenzene exhibits a wide range of biological effects.  In
rats given 500 mg/kg hexachlorobenzene in their diet for 4 months,
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hepatocellular hypertrophy and necrosis, spleen enlargement, prophyria, and
death were observed (Kimbrough and Linder 1974, as reported in IARC 1979).
Immunosuppression was observed in mice fed 167 mg/kg diet for 6 weeks (Loose
et al. 1977, as reported in IARC 1979).  Pigs were administered
hexachlorobenzene in the diet at doses of 0.05-50 mg/kg/day for 90 days.
Porphyria and death occurred at the highest dose level, histopathological
changes of the liver at 5 mg/kg/day, and increased excretion of coproporphyrin
in the groups receiving 0.5 and 5 mg/kg/day (den Tonkelaar et al.  1978, as
reported in IARC 1979).  Porphyrinuria has also been observed in rabbits,
Japanese quail, guinea pigs, and mice (USEPA 1980).  Hexachlorobenzene is
fetotoxic and produces some teratogenic effects.  Mice administered 100
mg/kg/day orally on gestation days 7-16 gave birth to offspring with an
increased incidence of cleft palates and kidney malformations (Courtney et
al. 1976, as reported in IARC 1979 and USEPA 1980).  In a four-generation
study with rats treated with hexachlorobenzene at doses ranging from 0 to 640
mg/kg diet, the neonatal survival rate and neonatal body weight were reduced
at the 80 mg/kg level; birth weights were reduced at the 160 mg/kg level.  No
gross abnormalities were found in this study (Grant et al.  1977, as reported
in USEPA 1980).

    Hexachlorobenzene was shown to be carcinogenic in two studies.  Groups of
male and female rats were fed diets containing 0, 50, 100 or 200 mg
hexachlorobenzene/kg diet for 120 days, and 300 mg/kg diet for 15 weeks.  An
increased incidence of liver cell tumors was observed in the 100,  200 and 300
mg/kg diet groups (Cabral et al. 1978 and 1979, as reported in IARC 1979).
In a lifetime study with Syrian golden hamsters given dietary concentrations
of 0, 50, 100, and 200 mg hexachlorobenzene/kg diet (equivalent to 0,.4, 8,
and 16 mg/kg bw/day), a significantly increased incidence of hepatomas was
reported at all doses tested.  Liver hemangioendotheliomas and alveolar
thyroid adenomas were found at the high dose level (Cabral et al.  1977, as
reported in IARC 1979).

    Few data are available on the toxicity of hexachlorobenzene to aquatic
organisms.  In 10 to 15 day studies with the largemouth bass, no effects were
observed at concentrations of 26 and 10 yg/liter (Laska et al.  1978, as
reported in USEPA 1980).  In a study of saltwater protozoa, a 10-day exposure
to 1 ug/liter of hexachlorobenzene caused decreased growth (Geike and
Prasher 1976, as reported in USEPA 1980).  Ninety-six hour exposure of pink
shrimp to 25 ug/liter resulted in 33 percent mortality (Parrish et al.
1974, as reported in USEPA 1980).

    EPA has established an ambient water quality criterion of 0.0072
yg/liter for the protection of human health from the toxic properties of
hexachlorobenzene ingested through contaminated water and aquatic organisms.

    EPA has not yet established an aquatic life water quality criterion for
hexachlorobenzene.
    Hexachlorobutadiene

    The acute oral toxicity of hexachlorobutadiene is moderate to high.
Schwetz et al. (1977, as reported in USEPA 1980) reported oral LD50 values
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of 200-400 mg/kg for female rats, 580 mg/kg for male rats, and 64 mg/kg for
weanling rats.  Oral LD50 values reported by Gradiski et al. (1975, as
reported in USEPA 1980) for male rats and mice were 250 and 80 mg/kg; hepatic
and renal disorders and effects on the central nervous system were noted.

    In chronic and subchronic studies of hexachlorobutadiene, the kidney
appears to be the most sensitive organ.  In a 30-day feeding study, renal
tubular epithelial degeneration, necrosis, and an increase in the
kidney-to-body weight ratio occurred in female rats receiving 30, 65, or 100
mg/kg/day hexachlorobutadiene in their diets, but not at 3 mg/kg/day (Kociba
et al.  1971, as reported in USEPA 1980).  In a two-year chronic study with
rats given 0, 0.2, 2, or 20 mg/kg/day hexachlorobutadiene in their diet, a
significant increase in renal tubular adenomas and carcinomas was observed in
both male and female rats at the 20 mg/kg/day level (Kociba et al. 1977, as
reported in USEPA 1980).  Slight renal tubular epithelial hyperplasia was
noted at the 2 mg/kg/day level.  A statistically significant increase in
urinary coproporphyrin was observed in male rats ingesting 20 mg/kg/day
hexachlorobutadiene and in females ingesting 2 mg/kg/day.  Schwetz et al.
(1977,  as reported in USEPA 1980) reported renal tubular dilation,
degeneration, and regeneration in kidneys from male and female rats given
hexachlorobutadiene in their diet at a dose level of 20 mg/kg/day for 143
days; a mottled cortex was noted at the 2 mg/kg/day level.  Kidney damage has
also been induced by inhalation of hexachlorobutadiene; injury to the tubular
epithelium was reported after 15 daily six-hour exposures to 25 ppm
hexachlorobutadiene (Gage 1970, as reported in USEPA 1980).  Evidence for the
teratogenic potential of hexachlorobutadiene is inconclusive.  Poteryaeva
(1966,  as reported in USEPA 1980) reported increased neonatal mortality,
decreased birthweight, kidney damage, and degenerative changes in red blood
cells in offspring of female rats given single subcutaneous injections of 20
mg/kg hexachlorobutadiene before breeding.  Schwetz et al. (1977, as
reported in USEPA 1980) observed no effects in offspring of male and female
rats given hexachlorobutadiene in the diet at dose levels of 0.2 and 2.0
mg/kg/day for 90 days before mating, during mating, and throughout gestation
and lactation; at the 20 mg/kg/day level, a slight decrease in weanling body
weight was the only observed effect.

    Acute toxicity data have been reported for four species of freshwater
fish, with LC50 values ranging from 90 to 326 yg/liter (USEPA 1980).  In
static tests conducted with saltwater mysid shrimp, grass shrimp, pinfish, and
sheepshead minnow, the 96-hour LC50 values were 59, 32, 399, and 557
ug/liter, respectively.  In an embryo-larval test with fathead minnow, a
chronic toxicity value of 9.3 yg/liter was reported (USEPA 1980).

    EPA has established a water quality criterion of zero for the maximum
protection of human health from the potential carcinogenic effects due to
exposure to hexachlorobutadiene through ingestion of contaminated water and
contaminated aquatic organisms.  Since the zero level may not be attainable at
the present time, a criterion of 0.45 yg/liter corresponding to a lifetime
incremental cancer risk of 0.000001 was recommended.

    EPA has not yet established aquatic life ambient water quality criteria
for hexachlorobutadiene.
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    Hexachloroethane

    The acute toxic effects of hexachloroethane in humans include extensive
eye irritation including inability to close the eyelid, tearing of the eyes,
inflammation of the delicate membrane lining of the eye, and visual
intolerance to light (NIOSH 1978, as reported in USEPA 1980).

    Liver degeneration and tubular nephrosis of the kidney were observed in
rabbits administered daily oral doses of 320 or 1,000 mg/kg for 12 days (Weeks
et al. 1979, as reported in USEPA 1980).  Inhalation exposure of dogs,
guinea pigs, and rats to 260 ppm for 6 hours/day, 5 days per week, for 6 weeks
produced central nervous system toxicity in dogs and rats, and increased liver
size in guinea pigs and rats (Weeks et al.  1978, as reported in USEPA
1980).  Rats administered 500 mg/kg/day orally from day 6 through 16 of
gestation gave birth to a significantly lower number of live fetuses (Weeks
et al. 1979, as reported in USEPA 1980).  Liver cancer was produced in mice
administered 590 mg/kg/day hexachloroethane by stomach tube for 78 weeks
(National Cancer Institute 1978, as reported in USEPA 1980).

    The toxicity of hexachloroethane to freshwater organisms was demonstrated
in Daphnia magna at 8.07 mg/liter, midge at 1.7 mg/liter, rainbow trout at
0.98 mg/liter, fathead minnow at 1.53 mg/liter, and the bluegill at 0.98
mg/liter.  Toxicity to saltwater organisms  was observed in the mysid shrimp at
0.94 mg/liter and the sheepshead minnow at  2.4 mg/liter.  Chronic toxicity has
been observed in the fathead minnow in concentrations ranging from 0.41 to 0.7
mg/liter.  Toxicity to aquatic plants was observed in freshwater algae at
87-93.2 mg/liter and in saltwater algae at  7.75-8.57 mg/liter (USEPA 1980)..

    EPA has established an ambient water quality criterion of zero for the
maximum protection of human health from the potential carcinogenic effects
from exposure to hexachloroethane through ingestion of contaminated water and
contaminated aquatic organisms.  However, since a zero level may not be
attainable at present, a level of 1.9 ug/liter, corresponding to a lifetime
incremental cancer risk of 0.000001, was recommended.

    EPA has not yet established an aquatic  life water quality criterion for
hexachloroethane.
    Hexachlorocyclopentadiene

    Little human toxicity data is available on hexachlorocyclopenta- diene.
Occupational experience has shown that hexachlorocyclopentadiene is highly
irritating (USEPA 1980, ACGIH 1980).  In a recent incidence in which
approximately 200 sewage treatment plant workers were exposed to acutely toxic
levels of hexachlorocyclopentadiene from illegal disposal of the compound,
workers reported severe irritation of the eyes, nose, throat, and lungs;
headache; nausea; and respiratory difficulty (Carter 1977 and Singal 1978, as
reported in USEPA 1980).

    The acute oral toxicity of hexachlorocyclopentadiene was investigated by
Treon et al. (1955, as reported in USEPA 1980).  The LD50 for rats and
rabbits was determined to be about 500 mg/kg.  IRDC (1972) and Naishstein and
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Lisovskaya (1965, both as reported in USEPA 1980) have reported similar LDSOs
for rats of 584 mg/kg and 600 mg/kg, respectively.  Hexachlorocyclopentadiene
appears to be as acutely toxic by dermal exposure as by oral exposure (USEPA
1980).  A 7-hour inhalation exposure to 1.5 ppm hexachlorocyclopentadiene was
lethal to rabbits; five 7-hour exposures to 1.0 ppm or two 7-hour exposures to
3.2 ppm was lethal to rats (Treon et al. 1955, as reported in USEPA 1980).

    To date, no adequate subchronic or chronic oral toxicity studies of
hexachlorocyclopentadiene have been performed.  Hexachlorocyclopentadiene was
given orally to rats at levels ranging from 0.00002 to 20 mg/kg/day for six
months (Naishstein and Lisovskaya 1965, as reported in USEPA 1980).  At the
high dose level, 2 of 10 animals died; at 0.002 mg/kg/day, the only reported
effects were neutropenia and a tendency toward lymphocytosis.   Rats, rabbits,
guinea pigs, and mice exposed to vapors of hexachlorocyclopentadiene showed
irritation of the eyes and mucous membranes (Treon et al. 1955, as reported
in ACGIH 1980).  At the lowest exposure level (0.15 ppm for 7 hours on each of
150 days over a 216-day period) degenerative changes in the liver and kidneys
of all species and pulmonary irritation in mice were observed.
Hexachlorocyclopentadiene has been tested for mutagenicity and reported to be
nonmutagenic in both short-term in vitro mutagenicity assays and in a mouse
dominant lethal study (USEPA 1980).

    Hexachlorocyclopentadiene is highly toxic to freshwater fish.  EC50 levels
for Daphnia magna of 39 and 52 yg/liter have been reported.  Investigators
have reported 96-hour LC50 values for the fathead minnow ranging from 7 to 180
yg/liter.  LC50 values for the channel catfish and bluegill have been
reported to be 97 and 130 yg/liter, respectively.  The chronic toxicity
value for the fathead minnow in an embryo-larval test is 5.2 yg/liter.
Ninety-six-hour LC50 values for three saltwater invertebrate and three
saltwater fish species ranged from 7 to 48 yg/liter for all species except
the polychaete for which the LC50 value was 371 yg/liter (USEPA 1980).

    EPA has established an ambient water quality criterion of 206 yg/liter
for the protection of human health from the toxic properties of
hexachlorocyclopentadiene through ingestion of contaminated water and aquatic
organisms.

    EPA has not yet established an aquatic life ambient water quality
criterion for hexachlorocyclopentadiene.


    Indeno(1,2,3-cd)pyrene

    Indeno(l,2,3-cd)pyrene is a member of the class of polynuclear aromatic
hydrocarbons (PAHs) many of which are known for their ability to induce
cancer.

    Limited data are available on the carcinogenicity of
indeno(l,2,3-cd)pyrene.  When groups of 20 female mice were painted three
times weekly with indeno(l,2,3-cd)pyrene in acetone at concentrations of 0.01,
0.05, 0.1 and 0.5%, no tumors were produced at the 2 lower doses, 6 papillomas
and 3 carcinomas were produced at the 0.1% dose level, and 7 papillomas and 5
carcinomas were produced at the 0.5% dose level (Hoffman and Wynder 1966, as
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reported in IARC 1973).  Indeno(l,2,3-cd)pyrene also produced tumors by
subcutaneous administration.  Three injections of 0.6 mg indeno(l,2,3-cd)-
pyrene in olive oil at one month intervals to male and female mice resulted in
sarcomas in 10 of 14 male mice after 265 days and in only 1 of 14 females
after 145 days (Lacassagne et al.  1965, as reported in IARC 1973).

    No human case studies or epidemiologic studies have been conducted which
establish indeno(l,2,3-cd)pyrene as a human carcinogen.  Indirect evidence for
the compound's carcinogenicity comes from air pollution studies which indicate
an excess of lung cancer mortality among workers exposed to high
concentrations of PAH-containing material such as coal gas, tars, soot, and
coke oven emissions (IARC 1973, USEPA 1980).

    No data are available on the aquatic toxicity of indeno(l,2,3-cd)- pyrene.

    EPA has not yet established ambient water quality criteria for
indeno(l,2,3-cd)pyrene because of the lack of sufficient data.  However, the
agency has established an ambient water quality criterion of zero for the
maximum protection to human health from the potential carcinogenic effects due
to exposure to polynuclear aromatic hydrocarbons through ingestion of
contaminated water and aquatic organisms.  Since the zero level may not be
attainable at present, a level of 2.8 ng/liter corresponding to a lifetime
incremental cancer risk of 0.000001 was recommended.
    Isophorone

    Human exposure to isophorone vapor causes irritation of the eyes, hose,
and throat of unacclimatized workers at concentrations of 25 ppm.  Workers
exposed to 5 to 8 ppm complained of fatigue and malaise (Silverman et al.
1946, as reported in Clayton and Clayton 1981 and USEPA 1980).  Inhalation of
200 and 400 ppm isophorone resulted in nausea, headache, dizziness, faintness,
inebriation, and a feeling of suffocation (Smyth and Seaton 1940, as reported
in USEPA 1980).

    In rats, exposure to isophorone vapors at 750 ppm for "several" hours
produced no symptoms other than slight eye and nose irritation; "some" deaths
were reported after four hours at 1,840 ppm, usually due to paralysis of the
respiratory system or lung irritation (Smyth and Seaton 1940, as reported in
USEPA 1980).  Rats and guinea pigs exposed to 100 to 500 ppm isophorone 8
hours/day, 5 days/week, for 6 weeks showed weight loss and evidence of
pathologic changes in the lung, spleen, and kidney.  In rats at 200 ppm and
guinea pigs at 500 ppm, conjunctivitis and nasal irritation were observed.
Exposure of rats to 50 ppm produced evidence of pathologic changes in the lung
and kidney (Smyth 1941, as reported in USEPA 1980).  It has been suggested
that the material used in these two inhalation studies was an impure
commercial product containing appreciable amounts of other volative
materials.  Therefore, the reported results are of uncertain reliability
(USEPA 1980).

    Oral LD50s have been reported for rats and mice ranging from 1.87 to 2,37
g/kg.  The LD50 reported for rabbits following acute dermal exposure to
isophorone is 1.39 g/kg (USEPA 1980) .  Isophorone is weakly irritating to the
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skin of rabbits, and induces reversible irritation of the conjunctiva and
corneal opacity when applied to rabbit eyes (Truhaut et al. 1972, as
reported in USEPA 1980).  In a 90-day feeding study in rats and dogs given 750
to 3,000 ppra in the diet (rats) or 35 to 150 mg/kg/day in gelatin capsules
(dogs), no significant differences between treated and control groups
regarding hematology, blood chemistry, urinalysis, or pathologic lesions were
observed (Parkin 1972, as reported in USEPA 1980).

    For Daphnia tnagna and the bluegill, EC50 concentrations for isophorone
of 117,000 and 224,000 yg/liter, respectively, have been reported (USEPA
1980).  For a saltwater species, the mysid shrimp, the 96-hour LC50 is 12,900
yg/liter.  Chronic effects were observed in an embryo-larval test with the
sheepshead minnow, a saltwater species, at a concentration of 110,000
Vg/liter.  Because this value is greater than the 96-hour LC50 for mysid
shrimp, the sheepshead minnow was not considered to be a sensitive species
(USEPA 1980).  Cell number production and chlorophyll a content in a
freshwater alga were affected in a 96-hour test at concentrations of 122,000
to 126,000 ug/liter.  In a saltwater alga, these effects were observed at
110,000 and 105,000 ug/liter (USEPA 1980).

    EPA has established an ambient water quality criterion of 5.2 mg/liter for
protection of human health from the toxic properties of isophorone through
ingestion of contaminated water and aquatic organisms.

    EPA has not yet established an aquatic life water quality criterion for
isophorone.


    Naphthalene

    Systemic toxicity to naphthalene in humans includes nausea, headache,
diaphoresis, hematuria, fever, anemia, liver damage, convulsions, and coma
(Sax 1975).  Toxic effects have been reported in infants when the only
exposure was to the mother during pregnancy (Zinkham and Childs 1958,
Anziulewicz et al.  1959, as reported in USEPA 1980).  Occupational studies
have associated laryngeal cancer with worker exposure in a coaltar naphthalene
production facility (Wolf 1976, as reported in USEPA 1980).

    Acute toxicity in animals is reflected by the following toxicity values.
In the rat, oral LD50s range from 1.78 to 9.43 gm/kg.  In the same species, an
inhalation LC50 of 100 ppm for 8 hours and a dermal LD50 of 2.5 gm/kg were
reported.  An LD50 of 5.1 gm/kg was reported in mice injected subcutaneously
with naphthalene (Ime et al. 1973, Gaines 1969, NIOSH 1977, Union Carbide
Corporation 1968, as reported in USEPA 1980).   In subacute and chronic
studies, rats fed 2% naphthalene in the diet for at least 60 days developed
early cataracts in both groups (Fitzhugh and Buschke 1949, as reported in
USEPA 1980).  Lens changes and early cataracts were also observed in rabbits
fed 1,000 mg/kg naphthalene by gavage for various lengths of time up to 28
days (Van Heyningen and Pirie 1976, as reported in USEPA 1980).  Bronchial
epithelial changes have been observed in mice treated by intraperitoneal
injection with 67.4 mg/kg and sacrificed at different times up to 7 days
following treatment (Mahvi et aj.. 1977, as reported in USEPA 1980).
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    The offspring of rabbits administered a metabolite of naphthalene,
2-naphthol, were born with cataracts and evidence of retinal damage (Van der
Hoeve 1913, as reported in USEPA 1980).  However, naphthalene was not
mutagenic in several microsomal/bacterial assay systems (McCann et al. 1975,
Kraemer et al. 1974, as reported in USEPA 1980).

    Lymphatic leukemia was observed in mice treated (skin painting) with a
solution of 0.5% coal tar naphthalene in benzene, 5 days per week for life
(Knake 1956, as reported in USEPA 1980).  Rats, subcutaneously injected with
500 mg/kg of coal tar naphthalene every 2 weeks for a total of seven
treatments, developed metaplastic lymphosarcoma (Knake 1956, as reported in
USEPA 1980).  These studies are difficult to interpret, however, because of
the nature of the purity of the naphthalene administered.   Several skin
painting studies, using pure naphthalene on mice (Kennaway 1930, Kennaway and
Hieger 1930, as reported in USEPA 1980) and rabbits (Bogdat'eva and Bid 1955,
as reported in USEPA 1980) showed no carcinogenic effect.   The possible
carcinogenicity of pure naphthalene consequently has not yet been
established.

    The acute toxicity of naphthalene to aquatic organisms was demonstrated in
six different species in concentrations ranging from 2.3 to 8.9 mg/liter.
Mosquitofish and pacific oysters were more resistant, having 96-hour LC50
values of 150 and 199 mg/liter, respectively.  Chronic toxicity has been
demonstrated in the fathead minnow in concentrations ranging from 0.45 to 0.85
mg/liter.  Algae were affected at 33 mg/liter (USEPA 1980).

    EPA has not yet established ambient water quality criteria for naphthalene
because of the lack of sufficient information.
    Nitrobenzene

    The most characteristic acute symptom in humans, following exposure to
nitrobenzene, is cyanosis as a result of methemoglobin formation.  Anemia may
develop 1 or 2 weeks after a poisoning or in more severe, cases may lead to
coma and death.  The symptoms of chronic occupational exposure to nitrobenzene
include cyanosis, methemoglobinemia jaundice, anemia, sulfhemoglobinemia,
persistence of Heinz bodies in the erythrocytes, and dark-colored urine.
There have been reports of menstrual disturbances in women chronically exposed
to nitrobenzene, and changes have been observed in the tissues of the chorion
and placenta from pregnant women occupationally exposed to nitrobenzene
(USEPA  1980).

    Nitrobenzene has induced methemoglobin formation in dogs, cats, and rats,
but not in guinea pigs or rabbits (Levin 1927, as reported in USEPA 1980).  An
early study found that nitrobenzene fumes caused cerebellar disturbances in
dogs and birds (Dresbach and Chandler 1918, as reported in USEPA 1980).
Little information is available on the teratogenic effects of nitrobenzene.
In one study on rats, however, a subcutaneous dosage of 125 mg/kg during the
preimplantation and placentation periods was associated with delay of
embryogenesis, alteration of normal placentation, and fetal abnormalities
(Kazanina 1968, as reported in USEPA 1980).  No studies are available that
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show nitrobenzene to be mutagenic or carcinogenic.  Nitrobenzene is, however,
structurally related to known carcinogens (USEPA 1980).

    Among freshwater animal species, the 48-hour EC50 is 27 mg/liter for
Daphnia tnagna,  and the 96-hour LC50 is 42.6 mg/liter for the bluegill.  A
freshwater alga, Selenastrum capricornuum, has an EC50 value for chlorophyll
a of 44.1 mg/liter.  In saltwater animal species, the 96-hour LCSOs are 6.68
mg/liter for the mysid shrimp and 58.6 mg/liter for the sheepshead minnow.
The saltwater alga Skeletonema costatum had an EC50 value for chlorophyll a
of 10.3 mg/liter (USEPA 1980).

    EPA has established an ambient water quality criterion of 19.8 mg/liter
for the maximum protection of human health from the toxic properties of
nitrobenzene through the ingestion of water and contaminated aquatic
organisms.

    EPA has not yet established an aquatic life water quality criterion for
nitrobenzene.
    N-Nitrosodimethylamine

    Dialkyl N-nitrosoamines are characteristically hepatotoxic, producing
hemorrhagic centrilobular necrosis.  A few cases of human poisoning from
exposure to N-nitrosodimethylamine have been reported.  Symptoms included
abdominal pains, exhaustion, headaches, and distended abdomens.  Clinical
examination showed signs of liver damage and bronchopneumonia in one case, and
autopsies have revealed cirrhotic livers (USEPA 1980).

    Acute exposure of experimental animals to N-nitrosodimethylamine produces
liver lesions in 24 to 48 hours, peritoneal and sometimes pleural exudate, and
in some cases kidney lesions (USEPA 1980).  An acute oral LD50 of 40 mg/kg has
been reported for the rat (USEPA 1980).  N-nitrosodimethylamine has been
reported to induce forward and reverse mutations in several bacterial species,
gene recombination and conversion in Saccharomyces cerevisiae, recessive
lethal mutation in Drosophila melanogaster, and chromosome aberrations in
mammalian cells (Montesano and Bartsch 1976, as reported in USEPA 1980).
N-nitrosodimethylamine is carcinogenic in all species tested:  mice, rats,
hamsters, guinea pigs, rabbits, ducks, mastomys, various fish, newts, and
frogs (IARC 1978).  In mice, chronic administration in the drinking water at a
concentration corresponding to a dose of 0.4 mg/kg/day produced lung adenomas
and hemangiocellular tumors in 13/17 and 2/10 mice, respectively (Clapp and
Toya 1970, as reported in IARC 1978).  Numerous studies in the rat have shown
that administration of 50-100 mg/kg in the diet or drinking water (or 4
mg/kg/day) leads to the development of high incidences of hepatocellular
carcinomas and cholangiocellular tumors.  Kidney tumors have been produced by
short-term or single-dose treatment with high oral doses (up to 30 mg/kg body
weight) (IARC 1978).  Lung adenocarcinomas and squamous-cell carcinomas have
also been observed after oral N-nitrosodimethylamine treatment (IARC 1980).
Druckrey et al. (1967, as reported in IARC 1978) reported tumors of the
nasal cavity in rats exposed by inhalation twice weekly for 30 minutes at a
concentration corresponding to 2 mg/kg body weight.  Single subcutaneous
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administration of N-nitrosodimethylamine in mice at doses of 1, 2, 4, and 8
mg/kg produced lung tumor incidences of 29%, 35%, 39%, and 67%, respectively
(Cardesa et al. 1974, as reported in IARC 1978).  A thorough review of the
available carcinogenicity data for N-nitrosodimethylamine is presented in IARC
(1978) and USEPA (1980).

    No acute aquatic toxicity information is available for
N-nitrosodimethylamine.   However, available data for nitrosamines indicates
that acute toxicity to freshwater aquatic life occurs at concentrations as low
as 5,850 ug/liter (USEPA 1980).   In a 52-week feeding study with rainbow
trout, a dose-related response of hepatocellular carcinoma occurred in trout
fed 200 to 800 mg N-nitrosodimethylamine (Grieco et al.  1978, as reported in
USEPA 1980).  In a study by Harshbarger et al. 1971 (as  reported in USEPA
1980), crayfish exposed for six months to N-nitrosodimethylamine developed
extensive degeneration of the antennal gland at 200,000  ug/liter and
hyperplasia of the hepatopancreas at 100,000 yg/liter.  No toxicity data are
available for saltwater species.

    EPA has established an ambient water quality criterion of zero for the
maximum protection of human health from the potential carcinogenic effects due
to exposure to N-nitrosodimethylamine through ingestion  of contaminated water
and aquatic organisms.  Since the zero level may not be  attainable at the
present time, a level of 1.4 ng/liter, corresponding to  a lifetime incremental
cancer risk of 0.000001, was recommended.

    EPA has not yet established an aquatic life water quality criterion for
N-nitrosodimethylamine.


    N-Nitrosodiphenylamine

    The dialkyl N-nitrosamines are characteristically hepatotoxic, producing
hermorrhagic centrilobular necrosis.  Acute oral LD50 values in the rat have
been given as  1,650 and 3,000 mg/kg (USEPA 1980).  The class of N-nitroso
compounds includes some of the most powerful chemical mutagens known.
However, N-nitrosodiphenylamine is reported to give a negative response in
both Salmonella typhimurium and E. coli mutagenicity assays after
activation with a rat liver microsomal preparation (USEPA 1980).  In a recent
National Cancer Institute bioassay (Cardy et al. 1979, as reported in USEPA
1980) rats developed neoplastic and non-neoplastic urinary bladder lesions
after two years of dietary administration of N-nitrosodiphenylamine at a
dose-level of 200 mg/kg/day.

    Acute toxicity from exposure to N-nitrosodiphenylamine has been reported
for Daphnia magna and the bluegill at concentrations of 7,760 and 5,850
Vg/liter, respectively.   A 96-hour LC50 for the mummichog, a saltwater
species, of 3,300 mg/liter has been reported  (USEPA 1980).  No chronic aquatic
studies are available for N-nitrosodiphenylamine.

    EPA has established an ambient water quality criterion of zero for the
maximum protection of human health from the potential carcinogenic effects due
to exposure to N-nitrosodiphenylamine through ingestion of contaminated water
and aquatic organisms.  Since the zero level may not be attainable at the
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present time, a level of 4.9 ug/liter, corresponding to a lifetime
incremental cancer risk of 0.000001, was recommended.

    EPA has not yet established an aquatic life water quality criterion for
N-nitrosodiphenylamine.
    N-Nitrosodi-n-propylamine

    No information on the toxicity of N-nitrosodi-n-propylamine in humans is
available.

    The dialkyl N-nitrosamines are characteristically hepatotoxic, producing
hemorrhagic centrilobular necrosis.  An acute oral LD50 in the rat is reported
as 480 mg/kg.  The subcutaneous LD50 for the rat is given as 487 mg/kg and for
the Syrian golden hamster as 600 mg/kg (IARC 1978).  N-nitrosodi-n-propylamine
is carcinogenic in experimental animals.  Administration in drinking water at
doses of 4, 8, 15, or 30 mg/kg/day produced liver carcinomas in 45 of the 48
rats tested after induction times ranging from 120 to 300 days (Druckrey et
al. 1967, as reported in IARC 1978).  Male and female rats injected
subcutaneously with 24.4, 48.7, or 97.4 mg/kg N-nitrosodi-n-propylamine once
weekly for life developed a high incidence of neoplasms of the nasal or
paranasal cavities (45 of 58 treated rats).  In addition, 13 liver tumors, 11
lung cancers, and 11 squamous-cell papillomas of the esophagus were seen
(Althoff et al. 1973, as reported in IARC 1978).  Syrian golden hamsters
were treated subcutaneously with 1.2% N-nitrosodi-n-propylamine in olive oil
once weekly for life at doses of 3.75, 7.5, 15, 30, or 60 mg/kg.  A high
incidence of tumors of the nasal and paranasal cavities, laryngobronchial
tract, and lung were observed in treated guinea pigs but not in controls
(Althoff et al. 1973, as reported in IARC 1978).  N-nitrosodi-n-propylamine
is mutagenic in in vitro assays with the bacteria Salmonella typhimurium
and E. coli and Chinese hamster V79 cells (IARC 1978).

    No aquatic toxicity studies are available for N-nitrosodi-n- propylamine.
However, available data for nitrosamines indicate that acute toxicity to
freshwater aquatic life occurs at concentrations as low as 5,850 yg/liter
(USEPA 1980).

    EPA has established an ambient water quality criterion of zero for the
maximum protection of human health from the potential carcinogenic effects due
to exposure to N-nitrosodi-n-propylamine through ingestion of contaminated
water and aquatic organisms.  Since the zero level may not be attainable at
the present time, a level of 0.8 ng/liter, corresponding to a lifetime
incremental cancer risk of 0.000001, was recommended.

    EPA has not yet established an aquatic life water quality criterion for
N-nitrosodi-n-propylamine.
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    Phenanthrene

    Phenanthrene is a polynuclear aromatic hydrocarbon that causes skin
photosensitization in humans and has produced cancer in animals (Sax 1975).
The oral LD50 in mice is 700 mg/kg (USDHHS 1980).

    The information on the toxicity of phenanthrene to aquatic organisms is
limited to one study of a crude oil fraction of phenanthrene that produced a
96-hour LC50 value of 600 yg/liter in the polychaete worm (USEPA 1980).

    EPA has not yet established ambient water quality criteria for
phenanthrene because of the lack of sufficient data.  However, the agency has
established an ambient water quality criterion of zero for the maximum
protection of human health from the potential carcinogenic effects due to
exposure to polynuclear aromatic hydrocarbons, which include phenanthrene,
through ingestion of contaminated water and contaminated aquatic organisms.
However, since a zero level may not be attainable at present, a level of 2.8
ng/liter, corresponding to a lifetime incremental cancer risk of 10-6, was
recommended.
    Pyrene

    No information is available on the toxicity of pyrene in humans, animals,
or aquatic life.  In an in vitro assay, pyrene exhibited toxicity to
transplanted rat respiratory epithelium and the submucosa of the trachea
(Topping et al. 1978).  Derivatives of pyrene, however, such as
benzoCa!pyrene, are highly potent animal carcinogens.

    EPA has not yet established ambient water quality criteria for pyrene
because of the lack of sufficient data.  However, the agency has established
an ambient water quality criterion of zero for the maximum protection of human
health from the potential carcinogenic effects due to exposure to polynuclear
aromatic hydrocarbons, which include pyrene, through ingestion of contaminated
water and contaminated aquatic organisms.  However, since a zero level may not
be attainable at present, a level of 2.8 ng/liter, corresponding to a life
time incremental cancer risk of 10-6, was recommended.
    2,3,7,8-Tetrachlorodibenzo-p-dioxin

    2,3,7,8-Tetrachlorodibenzo-p-dioxin (TCDD) is one of the most toxic
substances known.  It produces a delayed biological response in many species
and is highly toxic at low doses to aquatic organisms and mammals, including
humans.  Many human exposures to TCDD result from occupational exposure to
2,4,5-trichlorophenol (2,4,5-TCP) or 2,4,5-trichlorophenoxyacetic acid
(2,4,5-T), in which TCDD is a contaminant.

    TCDD has been identified as the cause of numerous outbreaks of chloracne
in humans.  In addition, investigators have reported muscular weakness, loss
of appetite and weight, sleep disturbances, hypotension, abdominal pain, liver
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impairment, peripheral neuropathy, psychopathological changes, hyperlipaemia
and hypercholesterolaemia, and porphyria cutanea tarda among exposed persons
(USEPA 1979).

    TCDD is extremely toxic in all animal species tested, with oral LD50
values for several species ranging between 0.6 and 115 yg/kg (NAS 1977).
Rats given single doses of 25 and 50 yg/kg of TCDD showed moderate to severe
thymic atrophy and liver damage; rats that received 100 Vg/kg showed 43%
mortality, severe liver damage, thymic atrophy, and icterus (Gupta et al.
1973, as reported in NAS 1977).  Mortality following acute oral doses may be
delayed.  In female rats given single oral doses up to 300 yg/kg, delayed
mortality was observed over a 90-day period (Greig et al. 1973, as reported
in NAS 1977).  McConnell et al. (1978, as reported in USEPA 1979) observed
weight loss, blepharitis, facial alopecia with acneform eruptions, and anemia
in rhesus monkeys given single oral doses of 70 to 350 yg/kg TCDD.  Deaths
were also reported.

    Damage to the liver and thymus are the predominant effects of subchronic
administration of TCDD.  In a 13-week study conducted by Kociba et al.
(1976, as reported in NAS 1977), degenerative changes in the liver and thymus,
porphyria, altered serum enzyme concentrations, and loss of body weight were
reported in rats given 0.1 yg/kg TCDD five days a week.  Young female rhesus
monkeys given a diet containing 500 ppt TCDD for up to nine months showed loss
of facial hair and eyelashes, edema, accentuated hair follicles, and dry scaly
skin (Allen et al. 1977, as reported in USEPA 1979).  Five of the eight
monkeys died from severe pancytopenia.

    TCDD is fetotoxic and teratogenic in various animal species.  Fetuses from
rats that had received 0.125 yg/kg/day showed reduced body weight and a
slight increase in intestinal hemorrhage and edema.  At 0.5 yg/kg/day, a
reduction in fetal number and increase in fetal deaths were reported (Sparschu
et al. 1971, as reported in NAS 1977). Courtney and Moore (1971, as reported
in NAS 1977) reported an increase in fetal kidney malformations in rats that
received TCDD subcutaneously at 0.5 yg/kg/day on days 9, 10 or 13 and 14 of
gestation.  Increased incidences of cleft palate and kidney abnormalities were
reported in mice that received 1.0 and 3.0 yg/kg/day on days 6 to 16 of
gestation (Smith et al. 1976, as reported in USEPA 1979).  The Advisory
Committee on 2,4,5-T (1971, as reported in NAS 1977) reported gastrointestinal
hemorrhage in the fetuses of hamsters that received 0.5 yg/kg/day TCDD on
days 6-10 of gestation.

    TCDD is a potent carcinogen.  Ingestion by rats of 2.2 ppb or 0.1
yg/kg/day induced squamous cancer of the respiratory tract and oral cavity
in males and females and liver cancer in females only (Kociba et al. 1978).
Van Miller et al. (1977, as reported in USEPA 1979) fed rats diets
containing 0.001 to 1,000 yg TCDD/kg diet.  An increased incidence of liver
tumors was reported in groups of rats receiving TCDD at levels of 0.005 to 5
yg/kg of diet; animals in the higher dose groups died between the second and
fourth weeks of treatment.

    TCDD has been shown to be mutagenic in three bacterial systems (Hussain
1972, as reported in USEPA 1979).  However, this finding has not been
confirmed by other researchers.
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    The data on aquatic toxicity of TCDD is not extensive.  Miller et al.
(1973, as reported in USEPA 1979) exposed coho salmon to 0.000056 yg/liter
of TCDD for 96 hours under static conditions and then transferred the fish to
control water.  Sixty days after exposure, the mortality among the exposed
fish was 12 percent compared to 2 percent among controls.   An exposure of
0.056 yg/liter for 24 hours was lethal to all salmon within 40 days.
Reduced reproduction was reported in the snail, Physa sp.  and worm, Paranis
sp., exposed to 0.2 yg/liter for approximately 1,175 hours (Miller e*t al.
1973, as reported in USEPA 1979).

    No data on the toxicity of TCDD to saltwater organisms or to aquatic
plants are available.

    EPA has proposed an ambient water quality criterion of zero for the
maximum protection of human health from the potential carcinogenic effects due
to exposure to TCDD through ingestion of contaminated water and aquatic
organisms.  Since the zero level may not be attainable at the present time,
the Agency considered establishing an interim criterion of 4.55 x 10 -8
yg/liter, corresponding to a lifetime risk of 0.000001.  A final criterion
will be established upon completion of a review of the carcinogenic potential
of TCDD by the, Agency.

    EPA has not yet established an aquatic life water quality criterion for
TCDD.
    1,2,4-Trichlorobenzene

    Human exposure to 1,2,4-trichlorobenzene vapor at 3 and 5 ppm causes minor
eye and respiratory irritation (Rowe 1975 in USEPA 1980).  No apparent
"serious" illness, change in liver function, or alteration of blood components
were observed over a period of 4 years in workers employed in a plant where
benzene was chlorinated.  One worker inhaled a "massive" amount of
trichlorobenzene and experienced lung hemorrhaging (NAS 1977).

    The single dose acute oral LD50 for 1,2,4-trichlorobenzene is 756 mg/kg in
rats and 766 mg/kg in mice (Brown et al. 1969 in USEPA 1980).  The rats'
deaths occured within 5 days of exposure, and the mice died within 3 days of
exposure.  For both species, decreased signs of activity were observed at low
doses, and convulsions occurred at higher doses.  1,2,4-Trichloro- benzene was
not irritating in subchronic skin irritation studies with rabbits and guinea
pigs (Brown et al. 1969 in USEPA 1980).  However, skin inflammation in
rabbits was noted after 3 weeks of exposure.  1,2,4-Trichlorobenzene applied
to rabbit ears for 13 weeks produced some dermal irritation.

    Rats, rabbits, and monkeys were administered 1,2,4-trichlorobenzene by
inhalation at concentrations of 25, 50, and 100 ppm for up to 26 weeks  (Coate
et al. 1977 in USEPA 1980).  No "exposure-related" ophthalmologic,
hematologic, pulmonary, or metabolic (blood urea nitrogen, bilirubin, serum
glutamic oxaloacetic transaminase, serum glutamic-pyruvic transaminase, lactic
dehydrogenase, and alkaline phosphatase) changes were observed.  Histologic
changes were noted in the livers and kidneys of rats necropsied at 4 weeks.
The changes were dose-related and were observed in animals from each treatment
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group.  However, after 20 weeks, no compound-related histopathological changes
were noted in rabbits or monkeys.  Mice exposed to 600 ppm of 1,2,4-
trichlorobenzene for 6 months did not develop hepatomas.   No other information
is available on the carcinogenicity, mutagenicity, or teratogenicity of
1,2,4-trichlorobenzene (USEPA 1980).

    The acute toxicity of 1,2,4-trichlorobenzene to various saltwater and
freshwater species is reflected by the 96-hour LC50 values in cladoceran of
50.2 mg/liter, rainbow trout of 1.5 mg/liter, fathead minnow of 2.9 mg/liter,
mysid shrimp of 0.45 mg/liter, and sheepshead minnow of 21.4 mg/liter.  The
chronic toxicity value for 1,2,4-trichlorobenzene to fathead minnow ranges
from 0.28 to 0.71 mg/liter.  1,2,4-Trichlorobenzene has also demonstrated
acute toxic effects to freshwater and saltwater algae with 96-hour EC50 values
ranging from 8.7 to 36.7 mg/liter.  The whole-body, 28-day bioconcentration
factor of 1,2,4-trichlorobenzene in the bluegill is 182 (USEPA 1980).

    EPA has not yet established ambient water quality criteria for
1,2,4-trichlorobenzene because of the lack of sufficient information.
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    4.   Metals and Cyanide

    Ant imony

    The major toxic symptoms that are associated with antimonial compounds in
humans involve the gastrointestinal tract, heart, respiratory tract, skin, and
liver.  The most serious effects of these compounds have been observed during
antimonial therapy and during industrial exposure (National Institute for
Occupational Safety and Health 1978, as reported in NAS 1980).  Symptoms
include cardiac alterations, bradycardia, and fluctuations in blood pressure
(Brieger et al. 1954, NIOSH 1978, as reported in NAS 1980).  Respiratory
changes include irritation of the mucous membranes, upper respiratory tract
irritation, and, more seriously, pneumonoconiosis.   Pneumonia has also been
cited as a side effect to the therapeutic use of antimony.  Gastrointestinal
symptoms include cramps, nausea, pain, anorexia, diarrhea, and vomiting (NAS
1980).  Chromosomal damage in human leukocytes studied in vitro occurred
with exposure to as little as 280 mg/liter of antimony (Paton and Allison
1972, as reported in USEPA 1980 and NAS 1980).  A greater incidence of
spontaneous abortion, premature deaths, and gynecological problems were
reported in antimony workers at a metallurgical plant (Belyayeva 1967, as
reported in NAS 1980).

    Acute poisoning of antimonial compounds in animals produce labored
breathing, general weakness, and other signs of cardiovascular insufficiency
leading to death among many animals within several days after exposure.  Oral
LD50 values are 300 mg/kg (tartar emetic) for the rat and 804 mg/kg (antimony
trifluoride) for the mouse (Bradley and Fredrick 1941, as reported in USEPA
1980).

    In chronic animals studies, rats fed 135 mg/kg trivalent antimony chloride
for 10 days developed toxic symptoms including myocardial degeneration
(Arzamastsev 1964, as reported in NAS 1980).  Decreased hemoglobin and
increased reticulocyte count were observed in guinea pigs treated for 10 days
with 12 and 20 mg/kg trivalent antimony chloride (Arzamastsev 1964, as
reported in NAS 1980).   In a longer study, rats orally fed 200 mg antimony
potassium tartrate died after 85 days (Flury 1927, as reported by NAS 1980).
Decreased fertility was reported in rats exposed to 50 mg/kg metallic antimony
by inhalation  (Belyayeva 1967, as reported in NAS 1980).  No evidence of
carcinogenicity was observed in mice given 5 ug of antimony potassium
tartrate per milliliter of drinking water throughout their lifetime (Kanisawa
and Schroeder  1969, as reported in USEPA 1980).

    The acute toxicity of antimony compounds on aquatic organisms is reflected
by 96-hour LC50 values in cladoceran of 9 mg/liter for antimony potassium
tartrate, and 21.9 mg/liter in the fathead minnow and 18.8 mg/liter in
cladoceran for antimony trichloride.  96-Hour LC50 values for antimony
trioxide are greater than 530 mg/liter in the bluegill and greater than 4.2
mg/liter in the mysid shrimp.  For this same compound the 96-hour LC50 ranges
from 6.1 to 8.3 mg/liter.  Chronic toxicity was observed in cladoceran exposed
to between 4.2-7.0 mg/liter antimony trichloride; and the fathead minnow
exposed to greater than 7.5 yg/liter for antimony trioxide and between 1.1
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and 2.3 mg/liter for antimony trichloride.  Freshwater algae were affected by
0.61-0.63 mg/liter antimony trioxide while freshwater algae were not affected
by levels of 4.2 mg/liter antimony trioxide (USEPA 1980).

    EPA has established an ambient water quality criterion of 146 yg/liter
for the protection of human health from the toxic properties of antimony
ingested through water and contaminated aquatic organisms.

    EPA has not yet established an aquatic life water quality criterion for
antimony.
     Arsenic

    The toxicity of arsenic varies according to the physical form and the
oxidation state of the compound.  In general, soluble trivalent arsenic
compounds are more toxic than the pentavalent species, and inorganic
arsenicals are also more toxic than organic arsenicals.  Inorganic arsenate
predominates in most waterways because of its stability and solubility.

    Many epidemiological studies have linked the development of cancer to
exposure to inorganic arsenic compounds.   Evidence has come from the use of
arsenicals as drugs, from geographical areas with high arsenic levels in the
drinking water, and from occupational exposures of workers in mining
operations, smelters, pesticide manufacture and vineyards.  However, this
evidence associating inorganic arsenic compounds with lung cancer in humans is
still open to question.  For skin cancer, however, a causal relationship
between incidence and high-level exposures to inorganic arsenic compounds has
been reported (Tseng et al.  1968, as reported in NAS 1977).

    Symptoms of acute arsenic poisoning by ingestion include abdominal pain
and vomiting, while acute poisoning by inhalation produces giddiness,
headache, extreme general weakness, and later nausea, vomiting, colic,
diarrhea, and pains in the limbs (Browning 1961, as reported in NAS 1977).

    Although no animal experiments have demonstrated carcinogenicity of
arsenic, several have shown that sodium arsenate and arsenite induce
developmental malformations in a variety of test animals including chick
embryos, hamsters, rats, and mice (USEPA 1980).

    Arsenic has been shown to be toxic to both vertebrate and invertebrate
freshwater aquatic organisms and saltwater aquatic organisms.  Cladocerans
have been reported to be more sensitive than fish, although certain
invertebrates such as stoneflies may be more tolerant than fish.  Static
96-hour LC50 values range from 0.812 mg/liter sodium arsenite for the scud to
22 mg/liter for the stonefish.  However,  less sensitive static 96-hour LC50
values of 26 mg/liter and 41.76 mg/liter sodium arsenite, respectively, were
reported for goldfish and bluegill.  One hundred percent of three different
strains of freshwater algae were killed in 2 weeks in 2.32 mg/liter sodium
arsenite.  Arsenic has been shown to bioconcentrate in both fresh and
saltwater organisms (USEPA 1980).
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    EPA has established an ambient water quality criterion of zero for the
maximum protection of human health from the potential carcinogenic effects due
to exposure to arsenic through the ingestion of contaminated water and
contaminated aquatic organisms.  Since the zero level may not be attainable at
the present time, a level of 2.2 ng/liter, corresponding to an estimated
lifetime incremental increase of cancer risk of 10-6, was recommended.

    EPA has not yet established an aquatic life water quality criterion for
arsenic.
    Asbestos

    Asbestos is a term applied to numerous fibrous mineral silicates composed
of silicon, oxygen, hydrogen, and metal cations.  The two major groups of
asbestos are serpentine (chrysotile) and amphibole.  Numerous epidemiological
studies have shown that long-term exposure to asbestos dust can lead to
asbestosis and an increased risk of cancer.

    Asbestosis is a chronic, progressive pneumoconiosis,  characterized by
fibrosis of the lung parenchyma.  Other symptoms of the disease include cough,
rales, finger clubbing, restrictive pulmonary dysfunction, and weight loss.
In some cases the disease can lead to death.  X-rays typically reveal small,
irregular opacities in the lungs, often accompanied by pleural fibrosis,
thickening, or calcification.

    An association between inhalation of asbestos and an increased rislc of
cancer has been clearly established in epidemiologic studies.  In a study of
the mortality experience of 17,800 asbestos insulation workers from 1967 to
1976 by Selikoff et al. (1979, as reported in USEPA 1980), significantly
increased incidences of lung tumors, mesotheliomas, cancer of the
gastrointestinal tract, larynx, pharyxn, and buccal cavity, and renal tumors
were reported.

    Several studies of cancer incidence among factory workers employed in the
manufacture of asbestos products have been reported (USEPA 1980).
Investigators have shown a significant excess in total mortality in exposed
workers, with important contributions from asbestosis, cancer of the lung,
bronchus, and trachea, and neoplasms of the digestive organs and peritoneum
(including peritoneal mesothelioma).  Mesothelioma is a form of cancer that is
very rare among individuals not exposed to asbestos.  Increased risks of lung
cancer and mesothelioma have also been reported among individuals exposed only
indirectly to asbestos, including shipyard workers and groups living or
working in an area of asbestos mining (USEPA 1980).

    Several studies have considered the relationship between ingestion of
asbestos in drinking water and gastrointestinal cancer.  The human data is,
however, inconclus ive.

    The carcinogenicity of asbestos has also been demonstrated in animals.
Gross et al.  (1967, as reported in USEPA 1980) reported 19 adenocarcinomas,
4 squamous cell carcinomas, and one mesothelioma among 72 rats exposed by
inhalation to 86 mg/cu m chrysotile for 16 months or longer.  No malignant
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tumors were found in 39 controls.  Rats exposed to various forms of asbestos
at concentrations ranging from 10 to 15 mg/cu m for periods ranging from 1 day
to 24 months showed an increased incidence of adenocarcinomas, squamous-cell
carcinomas, and mesotheliomas.   No tumors appeared prior to 300 days from
first exposure, and none of these tumors appeared in control animals (Wagner
et al. 1974, as reported in USEPA 1980).

    Mesotheliomas have been produced in rats by intrapleural injection of 10
mg of asbestos (Reeves et al. 1971, as reported in USEPA 1980) and by
intraperitoneal injection (Maltoni and Annoscia 1974, as reported in USEPA
1980).  The carcinogenicity of asbestos administered by ingestion has not been
demonstrated.

    No data were available on the potential toxicity of asbestiform material
to freshwater or saltwater organisms.

    EPA has established an ambient water quality criterion of zero for the
maximum protection of human health from the potential carcinogenic effects due
to exposure to asbestos through ingestion of contaminated water and aquatic
organisms.  Since the zero level may not be attainable at the present time, a
level of 30,000 fibers/liter, corresponding to a lifetime cancer risk of
0.000001, was recommended.

    EPA has not yet established an aquatic life water quality criterion for
asbestos.
    Beryllium

    Beryllium is relatively nontoxic to humans when ingested in food and water
because absorption from the digestive tract is slight (NAS 1977).  However,
beryllium and several beryllium compounds can cause acute and chronic effects
in humans.  The most common effects of industrial exposure to beryllium are
skin lesions:  dermatitis, ulceration, and granulomas.  Dermatitis has been
regarded as a sensitizing reaction (Doull et al. 1980).  Acute effects on
the respiratory system -- known as acute berylliosis -- may occur following
inhalation of beryllium at levels of 30 mg/cu m for the high-fired oxide, 1-3
mg/cu m for the low-fired oxide, and 0.1-0.5 mg/cu m for beryllium sulfate;
effects are usually reversible after weeks or months (Reeves et al. 1979, as
reported in IARC 1980).  The acute response is characterized by
nasopharyngistis, tracheobronch.itis, and fulminating pneumonia (Doull et al.
1980).

    Repeated inhalation exposure can lead to chronic berylliosis, with latent
periods of 10 to 20 years from the first exposure commonly observed.  Chronic
berylliosis is characterized by dyspnea, chronic cough, weight loss, weakness,
fatigue, and chest pain.  Systemic impairments include granulomatous
inflammation of the lungs; involvement of the striated muscle, liver, spleen,
kidneys, and heart; disturbances in nitrogen and calcium metabolism; and
immunological sensitization (Doull et al. 1980).  Human case reports and
epidemiologic studies provide suggestive but inconclusive evidence that
beryllium is carcinogenic in humans.  A positive correlation between beryllium
concentrations in drinking water and cancer deaths in 15 regions of the
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country was reported (Berg and Burbank 1972, as reported in USEPA 1980).  The
results of three epidemiological studies suggest that beryllium exposure
increased the risk of cancer mortality; however, confirmatory studies are
needed to evaluate the importance of other risk factors in beryllium-
associated lung cancer cases (USEPA 1980).

    In animal studies, beryllium has been shown to be acutely toxic to rats by
intravenous injection at 0.44 to 0.51 mg Be/kg (as soluble beryllium salts),
by the oral route at 9.7 mg/kg, and by inhalation at 42-194 yg/cu m (USEPA
1980).  Chronic beryllium disease can be produced in experimental animals by
inhalation of low concentrations of soluble beryllium salts.  Rats exposed for
up to 6 months to 35 yg/cu m of beryllium sulfate aerosol developed typical
chronic pneumonitis along with granulomatous lesions and some neoplasms
(Schepers et al. 1957, as reported in USEPA 1980).  Exposure of monkeys to
35 yg/cu m of beryllium sulfate or intratracheal instillation of a 5 percent
suspension of beryllium oxide resulted in chronic pneumonitis in all animals
(Vorwald et al. 1966, as reported in USEPA 1980).  Macrocytic anemia and
osteosclerotic changes have also been reported in animals following chronic
exposure to beryllium (USEPA 1980).  Lung cancer and bone cancer
(osteosarcoma) are the two types of malignancies commonly induced in
experimental animals by exposure to beryllium compounds.  In an inhalation
study in which rats were exposed to beryllium sulfate at 2.8, 21, and 42 yg
Be/cu m for 7 hours/day, 5 days/week, for a period of 18 months, pulmonary
cancers were found in almost all animals at the two highest doses and in 62
percent at the low dose (Vorwald et al. 1966, as reported in USEPA 1980).
Groups of rats were administered beryllium oxide calcined at temperatures of
500-1600oC by intratracheal instillation at a dose of 25 mg/kg; pulmonary
cancers were reported in 25 to 100% of the animals (Spencer et al. 1968, as
reported in USEPA 1980).  Osteosarcomas have been produced in rabbits by
intravenous injections or injections into the bone by numerous investigators.
In one study, osteosarcomas were produced in 89% and 100% of the rabbits
injected with beryllium oxide into the femur at doses of 220-400 and 420-600
mg, respectively, twice weekly for 1-43 weeks (Yamaguchi and Katsura 1963, as
reported in USEPA 1980).

    Acute beryllium aquatic toxicity data are available for the fathead
minnow, guppy, and bluegill at levels of hardness ranging from about 20 to 400
mg calcium carbonate/liter.  For these species, acute toxic effects were
reported at concentrations ranging from 130 yg/liter to 3,200 yg/liter
(USEPA 1980).  A 48-hour EC50 for Daphnia magna of 2,500 yg/liter was
reported.  In a chronic life-cycle study with Daphnia magna, toxic effects
were observed at 5.3 yg/liter (USEPA 1980).  Toxic effects of beryllium on
saltwater organisms have not been reported.  In one study of freshwater
plants, the growth of a green alga was inhibited at a beryllium concentration
of 100,000 yg/liter (USEPA 1980).

    EPA has established an ambient water quality criterion of zero for the
maximum protection of human health from the potential carcinogenic effects due
to exposure to beryllium through ingestion of contaminated water and aquatic
organisms.  Since the zero level may not be attainable at present, a level of
3.7 ng/liter, corresponding to a lifetime incremental cancer risk of 0.000001,
was recommended.
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    EPA has not yet established an aquatic life water quality criterion for
beryllium.
    Cadmium

    Human toxicity resulting from exposure to cadmium is well-documented, the
major effects being respiratory and renal toxicity.  Numerous cases of acute
cadmium poisoning in humans have been reported.  Acute lethal doses by
inhalation vary considerably depending on chemical form, particle size, and
duration of exposure; the product of concentration x time representing a
lethal dose of cadmium fumes has been estimated to be 2,600 mg/cu m. min,
i.e., 2,600 mg/cu m for one minute, 26 mg/cu m for 100 minutes, and so on
(Doull et al. 1980).  The minimal toxic dose for an 8-hour inhalation
exposure is estimated to be 1 to 3 mg/cu m (CEC 1978, as reported in Doull et
al. 1980).  Acute toxic effects of cadmium inhalation include irritation of
the upper respiratory tract, chest pains, nausea and diarrhea, dizziness, and
death usually due to massive pulmonary edema (Doull et al. 1980).  Acute
lethal cadmium doses by oral exposure in humans are estimated to range from
350 to 8,900 mg; major toxic effects of cadmium ingestion include nausea,
vomiting, salivation, diarrhea, and abdominal cramps.  Death due to shock,
dehydration or delayed systemic effects (notably renal and cardiopulmonary
failure) may occur (Doull et al. 1980).

    The principal target organs following chronic exposure to cadmium are the
lungs and kidney.  Chronic inhalation of cadmium fumes and dust can lead to an
emphysema-like condition with loss of ventilatory capacity, increased residual
lung volume, and shortness of breath (Lauwerys et al. 1974, as reported in
Doull et al. 1980).  The kidney appears to be the most cadmium-sensitive
organ, primarily because of its prediliction for accumulation of cadmium.
Renal toxicity of cadmium was first reported in a study of industrial exposure
to cadmium oxide dust in an alkaline storage battery factory (Friberg 1948, as
reported in Doull et al.  1980).  Workers exhibited consistent proteinuria
and a reduced ability to concentrate urine.  Glycosuria, hypercalciuria,
aminoaciduria, and increased uric acid excretion have also been reported in
workers (Kazantzis et al. 1963, as reported in Doull et al. 1980).  Based
on limited renal biopsies of affected and nonaffected workers, Friberg e_t
al. (1974, as reported in Doull et al.  1980) have proposed a threshold
concentration for renal toxicity of 200 ug Cd/g kidney cortex.  An incident
of chronic cadmium poisoning resulting from dietary intake was reported in
Japan in the 1940's.  The disease was named Itai-itai (or ouch-ouch).  People
consuming cadmium-contaminated rice developed osteomalacia with attendant
spontaneous multiple bone fractures as well as porteinuria and glycosuria
(Doull et al. 1980).

    Several epidemiologic studies provide suggestive evidence that cadmium
increases the risk of prostatic cancer in men.  Lemen et al. (1976, as
reported in Clayton and Clayton 1981) found an excess of cancers of the
prostate among cadmium smelter workers.  Five of eight deaths among a group of
74 alkaline cadmium battery workers who had been exposed to CdO dust for ten
or more years were due to cancer, including three carcinomas of the prostate
(Potts 1965, as reported in Clayton and Clayton 1981).  In a survey of 248
workers exposed to CdO for one or more years, four deaths from prostatic
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cancer, significantly more than expected, were observed (Kipling and
Waterhouse 1967, as reported in Clayton and Clayton 1981).  The evidence for
carcinogenicity of cadmium in humans is not conclusive, however, because of
the small study populations and confounding exposures to other elements which
are known to be human carcinogens (USEPA 1980).

    The toxic effects of cadmium observed in humans have been reproduced in
experimental animals.  The acute oral LD50 varies from approximately 100 mg/kg
for soluble salts of cadmium to several thousand mg/kg for metallic cadmium
powder or the insoluble selenide and sulfide.  Rats exposed to a cadmium
aerosol for 15 days developed lung inflammation followed by emphysema and
fibrosis (Snider et al. 1973, as reported in Doull et al.  1980).
Itai-itai disease has also been reproduced experimentally in rats given an
excess of cadmium in a calcium deficient diet (Itokawa e,t al. 1974, as
reported in Doull et al. 1980).  In newborn animals, cadmium has been shown
to cause cerebral and cerebellar damage.  Cadmium also is toxic to the testes
of rats and mice, and causes hyperglycemia and glucose intolerance in animals
(Doull et al. 1980).

    Animal studies have demonstrated that the injection of cadmium metals or
salts causes sarcomas at the site of injection and testicular tumors (Leydig
or interstitial cell tumors).  Interstitial cell tumors and subcutaneous
sarcomas were reported in rats following a single subcutaneous injection of
0.03 mmol cadmium chloride (Gunn 1963, as reported in Clayton and Clayton
1981).  Cadmium metal, CdO, CdS, and cadmium sulfate have also elicited
injection-site sarcomas (Clayton and Clayton 1981 and USEPA 1980).  Several
long-term feeding and inhalation studies have been carried out with cadmium
compounds; the induction of tumors by these routes of exposure has not been
observed (USEPA 1980).

    Predicting the impact of cadmium on aquatic organisms is complicated by
the variety of forms in which cadmium may be present, the differences in
toxicity and availability of the various forms, hardness of the water, pH,
temperature, and presence of other metal ions (USEPA 1980).  The results of
acute toxicity tests on cadmium with 29 freshwater fish and invertibrate
species range from 1 to 73,500 yg/liter (as Cd); both EC50 and LD50 values
are included in this range.  Chronic toxicity was observed in Daphnia magna
at concentrations ranging from 0.15 to 0.44 yg/liter, and in 12 freshwater
fish species at concentrations ranging from 1.7 to 50 yg/liter  (USEPA
1980).  In a 42-day study of cadmium toxicity to the bay scallop, exposure to
60 and 120 yg/liter reduced growth by 42 and 69 percent, respectively (Pesch
and Stewart 1980, as reported in USEPA 1980).  A 48-day exposure of copepods
to cadmium inhibited reproduction at concentrations greater than 44 yg/liter
(D'Agostino and Finney 1974, as reported in USEPA 1980).  Acute toxicity
values for 5 species of saltwater fish ranged from 577 yg/liter for larval
Atlantic silversides to 114,000 yg/liter for juvenile mummichog.  Acute
toxicity values for 26 species of saltwater invertibrates ranged from 15.5
yg/liter for the mysid shrimp to 46,600 yg/liter for the fiddler crab.  In
two life-cycle studies of mysid shrimp, toxic effects were observed at
concentrations of 5.5 and 8.0 yg/liter  (USEPA 1980).  Growth reduction was
the major toxic effect observed in several species of freshwater plants at
concentrations ranging from 2 to 7,400 yg/liter  (USEPA 1980).   In studies of
two species of saltwater phytoplankton, EC50 values of 160 and  175 yg/liter,
based on growth inhibition, were reported  (USEPA 1980).
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    EPA has established an ambient water quality criterion of 10 yg/liter
for the protection of human health from the toxic properties of cadmium
through ingestion of contaminated water and contaminated aquatic organisms.

    EPA has established an aquatic life water quality criterion for freshwater
species of 0.012 yg/liter (24-hour average), with a maximum not to be
exceeded of 1.5 yg/liter.  For saltwater species, the 24-hour average
criterion is 4.5 yg/liter, with a maximum not to be exceeded of 59
yg/liter.
    Chromium

    The toxicity of chromium varies according to its valence state.  The
hexavalent and trivalent moieties are the biologically significant forms.
Hexavalent chromium has long been recognized as a toxic substance, while
trivalent chromium is considered to be relatively innocuous (NAS 1977).

    Chromium has been shown to cause a variety of toxic effects.  Certain
chromium (VI) compounds are carcinogenic in humans (IARC 1980, USEPA 1980, NAS
1974, as cited in USEPA 1980).  In occupational exposures, dermatitis,
irritation of mucous membranes, injury to nasal tissue, changes in pulmonary
dynamics, lung cancer, and renal and hepatic toxicity have been observed (NAS
1974, Borett et al. 1977, Mancuso 1951, Bloomfield and Blum 1928, USPHS
1953, and IARC 1980, as reported in USEPA 1980).

    In animals, acute toxicity has been observed only when high doses were
administered.  For example, rats tolerated hexavalent chromium in drinking
water at 25 ppm for 1 year, and dogs showed no effect from chromium as
potassium chromate at 0.45-11.2 ppm over a 4-year period (NAS 1974, as
reported in NAS 1977).  Chromates, however, have been shown to be mutagenic in
a wide variety of test systems (USEPA 1980).  Chromium compounds also caused
terata in hamsters (IARC 1980).  With regard to carcinogenicity, intraosseous,
intramuscular, subcutaneous, intrapleural, and intraperitoneal injections of
chromium compounds produced tumors at the site of administration in rabbits,
mice, and rats (NAS 1977).   Intramuscular administration of lead chromate in
rats produced renal carcinomas (IARC 1980).

    Acute toxicity data for hexavalent chromium are available for 13
freshwater animal species;  96-hour LC50 values range from 67 ug/liter for a
scud to 59,900 yg/liter for a midge.  In saltwater species 96-hour LC50
values of hexavalent chromate range from 2,000 yg/liter for polychaete
annelids and mysid shrimp to 105,000 yg/liter for the mud snail.  Soft water
96-hour LC50 values for hexavalent chromium range from 17.6 mg/liter for
fathead minnows to 118 mg/liter for bluegill; hard water 96-hour LC50 values
for hexavalent chromium range from 27.3 mg/liter for fathead minnows to 133
mg/liter for bluegill.  96-Hour LC50 trivalent chromium values (chromium
potassium sulfate) range from 3.33 mg/liter for guppies to 7.46 mg/liter for
bluegill in soft water.  The LC50 for fathead minnows exposed to potassium
chromate in soft water was  reported to be 45.6 mg/liter.  Hexavalent chromium
was also found to significantly reduce the growth and survival of chinook
salmon at concentrations of 0.2 mg/liter.  Chronic toxicity of hexavalent
chromium was observed in the polychaete worm at concentrations ranging from 17
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to 38 yg/liter; the mysid shrimp at concentrations ranging from 88 to 198
yg/liter; the rainbow and brook trout at concentrations ranging from 200 to
350 yg/liter; and the fathead minnow at concentrations ranging from 1,000 to
3,950 yg/liter.  Algae and the giant kelp were affected at concentrations
ranging from 1,000 to 5,000 yg/liter (USEPA 1980).

    EPA has established an ambient water quality criterion of 50 yg/liter
for the protection of human health from the toxic properties of chromium (VI)
through ingestion of water and contaminated aquatic organisms.  A human health
criterion of 170 mg/liter was established for chromium III.

    EPA has established an aquatic life water quality criterion for freshwater
species of 0.29 yg/liter (24-hour average) for chromium VI,  and a criterion
of 2200 yg/liter (maximum level not to be exceeded) for chromium III.  The
aquatic life water quality criterion for saltwater species is 18 yg/liter
(24-hour average) for chromium VI.
    Copper produces a metallic taste in the mouth,  nausea, vomiting,
epigastric pain, diarrhea, and depending on the severity,  jaundice, hemolysis,
hemoglobinuria, hematuria, and oliguria.  In severe cases, hepatic necrosis,
gastrointestinal bleeding, anuria, hypotension, tachycardia, convulsions, and
coma can occur (USEPA 1980).   The toxic intake of inorganic copper for an
adult male was reported to be greater than 15 mg per dose (Burch et al.
1975, as reported in USEPA 1980).  Chronic oral exposure to copper has
resulted in behavioral changes, diarrhea, and progressive marasmus in an
infant (Salmon and Wright 1971, as reported in USEPA 1980).

    Chronic toxicity in animals varies considerably in different species.
Sheep are highly susceptible while rats are resistant to the effects of copper
(USEPA 1980).   Copper poisoning has been reported in swine at levels of 250
yg/g in the diet (Suttle and Mills 1966, as reported in USEPA 1980).
Hepatic hemosiderosis developed in swine and rats fed copper acetate in a
chronic oral feeding study (Mailory and Parker 1931, as reported in USEPA
1980).  No information is available on the teratogenicity or mutagenicity of
copper, although one report suggested that copper may increase the mutagenic
activity of other compounds.    The carcinogenic potential of copper has not
been established (USEPA 1980).

    Acute toxicity testing on copper has been conducted with 45 freshwater
species and chronic tests with 15 species.  Acute toxicity levels range from
0.0072 mg/liter for cladocerna in soft water to 10.2 mg/liter for the bluefish
in hard water.  Toxicity appears to decrease as the hardness of the water
increases.  Additional data for several species indicate, that toxicity also
decreases with increasing alkalinity and total organic carbon.  Among the more
sensitive species are daphnids, scuds, midges, and snails, which form the
major food webs for both warm and cold water fish (USEPA 1980).

    The acute toxicity of copper to saltwater animals ranges from 17
yg/liter for a Calonoid copepod to 600 yg/liter for the shore crab.  A
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chronic lifecycle test on mysid shrimp showed adverse effects at 77
Tig/liter.  Saltwater algae were adversely affected in concentrations ranging
from 5 to 100 yg/liter.  Oysters have been reported to bioaccumulate copper
up to 28,200 times the ambient concentration.  In long-term exposures, the bay
scallop was killed at 0.005 mg/liter (USEPA 1980).

    Chronic toxicity values for 15 species ranged from a low of 3.9 yg/liter
for brook trout to 6.4 yg/liter for the northern pike.  The two most
sensitive species, bluntnose minnow and G. pseudolimnia, are both important
food organisms.  Copper toxicity has been evaluated on a wide range of plant
species, with results similar to those for animals.  Bioaccummulation does not
appear to occur often in the edible portion of freshwater aquatic species
(USEPA 1980).

    EPA has not yet established ambient water quality criteria for the
protection of human health from the toxic effects of copper because of the
lack of sufficient information.  However, using organoleptic data for
controlling undesirable taste and odor of ambient water, the estimated level
is 1 mg/liter.

    The aquatic life water quality criterion for freshwater species is 5.6
yg/liter (24-hour average), with a level not to be exceeded of 12
yg/liter.  For saltwater species, the 24-hour average criterion is 4
yg/liter; the maximum level not to be exceed is 23 yg/liter.


    Cyanide

    Hydrogen cyanide and its alkali metal salts are extremely toxic to humans
and other mammals (USEPA 1980).  By ingestion, the mean lethal dose of these
substances is estimated to range from 50 to 200 mg for humans with death
occurring generally within 1 hour (Gosselin et al. 1976, as reported in
USEPA 1980).  Inhalation of hydrogen cyanide gas at 0.1-0.3 mg/liter has
caused death in 10-60 minutes in humans (Prentiss 1937 and Fassett 1963 as
reported in USEPA 1980).  The acute effects of cyanide poisoning mostly result
from inhibition of cytochrome C oxidase, resulting in a blockage of oxidative
metabolism and phosphorylation (Gosselin et al. 1976, as reported in USEPA
1980).  The organ systems most profoundly affected are the heart and brain
because of their high dependence on oxidative metabolism.  Cyanide poisoning
can also cause increased blood pressure (Heymans and Neil 1958, as reported in
USEPA 1980).  Exposure of humans to small amounts of cyanide compounds over
long periods of time is reported to cause loss of appetite, headache, weakness
nausea, dizziness, and symptoms of toxicity in the upper respiratory tract and
eyes (Sax 1975).

    Despite the high acute toxicity of cyanide, chronic exposure to sublethal
doses does not appear to have serious adverse effects (USEPA 1980).  Animal
studies with dogs administered 0.5-2 rag/kg sodium cyanide once or twice each
day for 15 months showed no evidence of pathophysiological changes in organ
function or permanent alteration in intermediary metabolism (Hertting et a1.
1960, as reported in USEPA 1980).  In other studies rats were fed a potassium
cyanide mixture equivalent to the LD50 for 25 days and dogs were fed 150 ppm
sodium cyanide for 30 days without observing significant adverse effects
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(Hayes 1967 and American Cyanamid 1959, as reported in USEPA 1980).  No
information is available on the mutagenicity and carcinogenicity of cyanides
(USEPA 1980).   However, thiocyanate, the major metabolic product of cyanide,
has produced,  jji vivo, developmental abnormalities in the chick and ascidian
embryo.  (Nowinski and Pandra 1946 and Ortolani 1969, as reported in USEPA
1980)

    The acute toxicity of cyanide to aquatic organisms has been demonstrated
in over 35 species of fresh and saltwater animals.  The 96-hour LC50 values
range from 30 yg/liter for the saltwater copopod to 2326 yg/liter for the
freshwater isopod.  Most values, however, cluster between 50 and 200
yg/liter.  Teratogenic effects have been observed in the Atlantic salmon,
and reproductive disturbances have occurred in the bluegill, fathead minnow,
brook trout, and rainbow trout at concentrations ranging from 5.4 to 62
yg/liter (USEPA 1980).

    Chronic toxicity has been observed in the brook trout, fathead minnow, the
bluegill, the isopod, and the scud in concentrations ranging from 8 to 34
yg/liter, depending on the species.  Reduced swimming capacity was observed
in the brook trout at 10 yg/liter, in rainbow trout at 20 yg/liter, and in
the Cichlasoma binaculatum at 40 yg/liter.  Aquatic plants are much more
resistant to the effects of cyanide; effects are not observed until
concentrations reach 3,000 yg/liter (USEPA 1980).

    EPA has established an ambient water quality criterion of 200 yg/liter
for the protection of human health from the toxic properties of cyanide
through ingestion of water and contaminated aquatic organisms.

    EPA has established an aquatic life water quality criterion for freshwater
species of 3.5 yg/liter (24-hour average), with a maximum not to be exceeded
of 52 yg/liter.  EPA has not yet set a criterion for saltwater species.
    Lead

    Acute inorganic lead intoxication is rare (Casarett and Doull 1975).  The
most serious effects of chronic exposure in humans are seen in the
hematopoietic system (decreased heme synthesis), nervous system
(encephalopathy), and renal system (NAS 1977 and USEPA 1980).  Blood lead
concentrations of 25-30 yg/day in children and women and 35-40 yg/day in
men have been associated with statistically significant increases in red-cell
protoporphyrin (Zielhuis 1975, as reported in USEPA 1980).  The noeffect
concentration of lead in the blood on the developing human nervous system has
been estimated at 55-60 yg/day whole blood (NAS 1977).  Blood-lead
concentrations in excess of about 50-60 yg/day have been associated with
spermatoxic effects in men (Lancranjan et al. 1975, as reported in USEPA
1980).  Lead has not been shown to be carcinogenic in humans, although one
researcher has questioned the statistical methodology used in the
epidemiological studies (Kanj et al. 1980, as reported in USEPA 1980).

    Certain lead compounds have been found to produce tumors in some species
of experimental animals.  For example, in a 2-year feeding study on rats, lead
acetate at concentrations of 1,000 ppm or more was found to induce renal
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tumors; furthermore, the number of tumor bearing animals was dose dependent
(Azar et al. 1973, as reported in USEPA 1980).  Lead has been associated
with teratogenic effects in chick embryos and rodents (USEPA 1980).
Teratogenic effects were seen in the offspring of rats that had received a
single intraperitoneal dose of 25-70 mg/kg on day 9 of gestation.
Administration later in pregnancy induced fetal resorption without teratogenic
effects (McClain and Beeker 1975, as reported in USEPA 1980).  Chronic
administration of lead in the drinking water of pregnant rats at
concentrations up to 250 mg/liter was found to delay fetal development and
increase fetal resorption; no teratogenic effects were seen (Kimmel et al.
1976, as reported in USEPA 1980).

    Lead has been shown to be acutely toxic to freshwater animals over a range
of concentrations from 124 to 542,000 yg/liter, depending on the species
tested and the hardness of the water.  The acute toxicity values for saltwater
invertebrates ranged from 668 yg/liter to 27,000 yg/liter.  Chronic tests
have been conducted with two invertibrate species and six fish species with
the chronic values ranging from 12 yg/liter for Daphnia magna to 174
yg/liter for the white sucker (USEPA 1980).  Concentrations as low as 500
yg/liter were found to inhibit the growth of freshwater algae (USEPA 1980).

    EPA has established an ambient water criterion of 50 yg/liter for the
protection of human health from the toxic properties of lead through ingestion
of water and contaminated aquatic organisms.

    EPA has established an aquatic life water quality criterion for freshwater
species of 0.75 yg/liter (24-hour average), with a maximum level not to be
exceeded of 74 yg/liter.
    Mercury

    Elemental mercury is extremely toxic but is very poorly absorbed from the
gastrointestinal tract.  The oral toxicity of inorganic mercury salts depends
on their solubility.  Elemental mercury is transformed biochemically in bottom
sediments to methyl mercury or other organic mercurial compounds (USEPA
1976).  The organic form readily enters the food chain with concentration
factors as great as 3,000 in fish (Hannerz 1968, as reported in USEPA 1976).

    Acute poisoning in man has resulted from exposure to mercury vapor in
concentrations ranging from 1.2 to 8.5 mg Hg/cu m with symptoms related to
pulmonary effects (Casarett and Doull 1975).  Chronic exposure to mercury
vapor results in central nervous system effects including psychic and
emotional disturbances, increased irritability, combativeness, defective
patterns, ocular disturbances, and tremors.  Kidney and gastrointestinal
disturbances are often associated with chronic mercury exposure (AIHA 1966, as
reported by Casarett and Doull 1975).

    Symptoms of acute inorganic mercury poisoning include pharyngitis,
gastroenteritis, vomiting followed by ulcerative hemorrhagic colitis,
nephritis, hepatitis, and circulatory collapse (USEPA 1976).  Renal toxicity
occurs with chronic exposure to inorganic mercury (Casarett and Doull 1975).
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    The toxicity of alkyl mercury compounds, particularly methyl mercury,
differs significantly from other organic mercurials.   In addition to the
environmental transformation of other forms of mercury to methyl mercury, this
compound is readily absorbed through the lungs, and skin and gastrointestinal
absorption under most circumstances is nearly complete (Casarett and Doull
1975).  Methyl mercury will also readily cross the placental barrier causing
fetal toxicity.  In humans methyl mercury poisoning has produced fatalities,
birth defects, and severe central nervous system effects (NAS 1977).  The
ingestion of fish containing mercury in Minamata, Japan, and the ingestion of
wheat seed treated with phenyl mercuric acetate resulted in similar toxic
effects including mental disturbance, ataxia, speech disturbances, hearing
impairment, constriction of visual fields, increased tendon reflex, and
involuntary movement.  Hypoplasia and atrophy of the brain tissue have also
been reported (Casarett and Doull 1975).

    The toxicity of inorganic mercury to freshwater aquatic organisms was
demonstrated in nine taxonomic orders from rotifers to fish.  Acute toxicity
values ranged from 0.02 to 2,000 yg/liter.  The acute toxicity of mercuric
chloride was reported for 26 species of saltwater animals including annelids,
molluscs, crustaceans, echinoderms, and fishes.  Species mean acute values
range from 3.5 to 1,680 yg/liter.  Fish are more resistant while molluscs
and crustaceans are more sensitive.  The acute toxicity of methyl mercury and
other mercury compounds is available only for fish, limiting an estimate of
the range of species sensitivity to the compound.  Methyl mercury is the most
toxic of the mercury compounds with chronic values for cladoceran and brook
trout being 1.0 and 0.52 yg/liter, respectively.  For inorganic mercury the
chronic value for cladoceran is reported to be 1.6 yg/liter.  Concentrations
that affected growth and photosynthetic activity of one saltwater diatom and
six species of brown algae range from 10 to 160 yg/liter.  Adverse effects
on reproduction of the mysid shrimp occurred at a concentration of 1.6
yg/liter.  A bioconcentration factor of 40,000 was reported for methyl
mercuric chloride in the oyster.  In freshwater organisms, a bioconcentration
factor of 23,000 was reported for inorganic mercury (USEPA 1980).

    EPA has established a water quality criterion of 144 ng/liter for the
protection of human health from the toxic effects of mercury ingested through
water and contaminated aquatic organisms.

    EPA has established an aquatic life water quality criterion for freshwater
species of 0.20 yg/liter (24-hour average), with a maximum level not to be
exceeded of 4.1 yg/liter.  For saltwater species, the 24-hour average
criterion is 0.10 yg/liter, with a maximum not be exceeded of 3.7
yg/liter.


    Nickel

    A significantly increased incidence of cancers of the lungs and nasal
cavities has been found in epidemiologic studies of workmen in nickel smelters
and refineries (NAS 1977).  The implicated compounds are nickel subsulfide,
nickel oxides, nickel carbonyl vapor, and soluble aerosols of nickel sulfate,
nitrate, or chloride  (NAS 1980).  Toxic effects depend on the nickel compound
to which a subject is exposed.  Acute nickel carbonyl poisoning results  in
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immediate symptoms of headache, nausea, and insomnia, followed by constrictive
chest pains, hyperpnea, cyanosis, and severe weakness (Sunderman 1970, Vuopala
1979, as reported in USEPA 1980).  Nickel carbonyl exposures have also been
associated with nephrotoxicity (Blandes 1934, Carmichael 1953, as reported in
USEPA 1980).  Exposure to occupational sources of nickel and exposure to such
nickel-containing items as jewelry and tools have been associated with a
characteristic nickel dermatitis (USEPA 1980).

    Animal studies have shown that the oral toxicity of nickel and nickel
salts is relatively low, but that parenteral injections of nickel salts are
much more toxic (NAS 1977).  The major symptoms of acute nickel toxicity are
hyperglycemia and gastrointestinal and central nervous system effects (NAS
1977).  One researcher found malformations in hamster embryos when the mother
was exposed to unidentified nickel compounds administered parenterally at
dosages ranging from 0.7 to 10.0 mg/kg (Perm 1972, as reported in USEPA
1980).  No teratogenic effects were seen when either nickel chloride (16
mg/kg) or nickel subsulfide (80 mg/kg) was administered to rats (Sunderman et
al.  1978, as reported in USEPA 1980).  Multigenerational reproductive
studies have linked nickel to decreases in litter size, increased numbers of
runts, and increased neonatal mortality (USEPA 1980).  Male rats given daily
oral doses of nickel sulfate at 25 mg/kg were completely sterile after 120
days (Watschewa et al. 1972, as reported in USEPA 1980).  Several
nickel-containing substances including nickel dust, nickel subsulfide, nickel
oxide, nickel carbonyl, and nickel bicyclopentadiene have been found to be
carcinogenic in animals upon inhalation or parenteral administration (NAS
1977).

    The toxicity of nickel to freshwater animals decreases with increasing
hardness of the water.  For example, the LC50 for Daphnia magna was 510
yg/liter at a water hardness of 45 mg of calcium carbonate/liter.  By
comparison, the LC50 for the fathead minnow was 5.21 mg/liter at 45 mg of
calcium carbonate/liter.  In several life cycle or early life stage studies in
freshwater fish, the fathead minnow, chronic toxicity was observed at
concentrations ranging from 109 to 527 yg/liter (USEPA 1980).  Nickel has
also been shown to reduce the growth of several freshwater algae species at
concentration ranging from 100 to 700 yg/liter.  The LC50 values for
saltwater animal species ranged from 152 yg/liter for mysid shrimp to
350,000 yg/liter for the mummichog fish.  Growth reductions have been
reported for a species of saltwater algae (USEPA 1980).

    EPA has established an ambient water criterion of 13.4 yg/liter for the
protection of human health from the toxic properties of nickel through
ingestion of contaminated water and contaminated aquatic organisms.

    EPA has established an aquatic life water quality criterion for nickel.
For freshwater species, the 24-hour average criterion is 0.20 yg/liter, with
a maximum not to be exceeded of 4.1 yg/liter.  The 24-hour average criterion
for saltwater species is 0.10 yg/liter, with a maximum not to be exceeded of
3.7 yg/liter.
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    Selenium

         Although elemental selenium is relatively nontoxic, the soluble salts
of selenium dioxide, selenium trioxide, some halogen compounds, and especially
hydrogen selenite are toxic in humans (NAS 1977).   Acute human exposure
generally produces irritation to the eyes, skin, and mucous membranes and
nausea, headaches, and a variety of respiratory disorders (NAS 1977).  Chronic
human exposures have produced such symptoms as depression, nervousness,
occasional dermatitis, and gastrointestinal disturbance (NAS 1977).  In
addition, epidemiologic studies of children indicated a relationship between
increased incidence of dental caries and consumption of small amounts of
selenium while the teeth were developing; similar results have been seen in
experimental studies of rats (NAS 1977).

    Acute and chronic selenium toxicity have been observed experimentally in
laboratory animals and also in domestic animals consuming plants with a high
selenium content.  Selenium disease in domestic animals, in its most serious
form, first manifests itself by impaired vision, then paralysis, and
ultimately death by respiratory failure (USEPA 1980).   The concentrations of
selenium in the diet which will produce chronic toxic effects depend on the
chemical form of the selenium and other dietary components.  (Fishbein 1977,
as reported in USEPA 1980) .  In a chronic feeding study, young rats treated
with sodium selenite showed growth depression when the diet contained 6.4 ppm
selenium or more.  Animals receiving concentration of 8 ppm or more died after
the fourth week and showed enlargement of the pancreas, reduction of
hemoglobin content, and increased serum bilirubin (Halverson et al. 1966, as
reported in NAS 1977).  Selenium has not been positively established as a
carcinogen.  Although some studies have reported increased tumor incidences in
animals fed selenium, these results have not been sufficiently documented and
are not in accord with other studies (NAS 1977).  No reports of mutagenicity
by selenium compounds are available.  Selenium has been shown to be
teratogenic in chick embryo tests, even when exposure is at low concentrations
(NAS 1977).  Malformations have also been seen in domestic mammals, but they
were not reproduced in the only available study on laboratory animals in which
hamsters received a near lethal intravenous dose of 2 mg/kg sodium selenite
(Holmberg and Ferm 1969, as reported in USEPA 1980 and NAS 1977).  In
reproduction tests on rats, selenium has been associated with decreases in
fertility and pup survival (NAS 1977).

    Selenium is acutely toxic to aquatic invertebrates and to fish.  Acute
toxicity data for inorganic selenite is available for 13 species of freshwater
animals and ranges from 340 yg/liter for the scud to 42,000 yg/liter for
the midge.  For selenate, acutely toxic concentrations range from 760
yg/liter for the scud to 12,500 yg/liter for the fathead minnow.  Chronic
toxicity for selenite and selenate compounds in freshwater organisms range
from 88 yg/liter for rainbow trout to 690 yg/liter for Daphnia magna
(USEPA 1980).  Selenium compounds have also been shown to be toxic to aquatic
and terrestial plants (USEPA 1980).

    EPA has recommended an ambient water quality criterion of 10 ug/liter for
the protection of human health from the toxic properties of selenium through
ingestion of contaminated water and contaminated aquatic organisms  (USEPA
1980).
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         EPA has established an aquatic life water quality criterion for
freshwater species of 35 yg/liter (24-hour average), with a maximum not to
be exceeded of 260 yg/liter.  For saltwater species, the 24-hour average
criterion is 54 yg/liter, with a maximum not to be exceeded of 410
yg/liter.
    Silver

    Silver exhibits moderate toxicity in humans.  Acute oral doses of silver
nitrate can cause abdominal pain and rigidity, vomiting, and convulsions.
Exposure information for the case reports of acute poisonings is generally
scanty.  However, ingestion of 10 g is usually fatal (USEPA 1980).

    The most common effect of chronic human exposure to silver is argyria
(either generalized or localized) resulting from medical or occupational
exposure.  Generalized argyria is characterized by slate gray pigmentation of
the skin, hair, conjunctiva of the eye, and internal organs resulting from
deposition of silver in tissue.  In severe cases of argyria, the respiratory
tract may be affected.  In localized argyria, only limited areas are
pigmented, and in a condition called argyrosis, the tissues of the eye are
pigmented (Clayton and Clayton 1981, Doull et al. 1980, and USEPA 1980).
With improved work conditions, no cases of argyria from industrial exposures
have been reported since the 1930's (Clayton and Clayton 1981).

    Acute toxicity in experimental animals is associated predominantly with
intravenous administration.  Dogs injected with approximately 32 mg Ag/kg (as
silver nitrate) in the pulmonary system developed edema, myocardial ischemia
and lesions, and hypertension.  When inorganic silver compounds were injected
into animals intravenously, effects were primarily on the central nervous
system (Hills and Pillsbury 1939, as reported in USEPA 1980).  Large doses of
colloidal silver administered intravenously have produced death due to
pulmonary edema and congestion (USEPA 1980).

    In subchronic and chronic animal studies, the predominant effects of
silver administration have been on conditioned reflex activity and on the
kidney.  Klein et al. (1978, as reported in USEPA 1980) reported hemorrhages
in the kidneys of rats given silver at 0.4 mg/liter drinking water for 100
days.  At 1 mg/liter, changes in both the kidney and liver were observed (form
of the metal unspecified).   Several investigators have reported effects on
conditioned reflex activity in rats given silver in drinking water (form of
the metal unspecified) at concentrations between 0.5 and 20 mg/liter for
periods of 1 to 11 months (Barkov and El'piner 1968, Kharchenko and Stepanenko
1972, and Zapadnyuk et al.  1973,  as reported in USEPA 1980).  Brain nucleic
acid content in rats was also reduced at 0.5 mg/liter drinking water (form of
the metal unspecified) (Kharchenko et al. 1973, as reported in USEPA 1980).
In several studies, implanted foils and disks and injected colloidal
suspensions of metallic silver have been found to produce tumors or
hyperplasia.  These effects are considered to be due to the particular form of
the metal or to its being an exogenous irritant.  Thus, silver is not
considered to be carcinogenic (USEPA 1980).
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    In natural waters, silver exists primarily in the 0 and +1 oxidation
states; the monovalent species is the form of greatest environmental concern.
Silver is one of the most toxic metals to freshwater aquatic life.  For
invertibrate species, acute toxicity values range from 0.25 yg/liter for
Daphnia magna to 4,500 yg/liter for the scud Gammarus pseudolitnnaeus.
Acute toxicity values for fish range from 3.9 yg/liter for the fathead
minnow in soft water to 280 yg/liter for rainbow trout in hard water (USEPA
1980).  In an 18-month study conducted by Davies et al. (1978, as reported
in USEPA 1980) with freshwater trout, the rate of growth was decreased in fish
exposed for two months at a concentration of 0.17 yg/liter, and mortality
was 17 percent greater than the control in this dose group at the study end.

    Acute toxicity values for saltwater organisms ranged from 4.7 yg/liter
for the summer flounder to 1,400 yg/liter for the sheepshead minnow (USEPA
1980).  In a life-cycle toxicity study with mysid shrimp, brood size was
smaller than the control at a concentration of 33 yg/liter of silver
(Lussier and Gentile 1980, as reported in USEPA 1980).

    In various strains of freshwater algae, growth inhibition has been
reported at silver concentrations ranging from 30 to 200 yg/liter (USEPA
1980).  Phytotoxicity was reported in duckweed at a silver concentration of
270 yg/liter, and in waterweed at a concentration of 7,500 yg/liter (Brown
and Rattigan 1979, as reported in USEPA 1980).  In saltwater algae, reduced
cell numbers were reported at 130 yg/liter (USEPA 1978, as reported in USEPA
1980).

    EPA has established an ambient water quality criterion of 50 yg/liter
for the protection of human health from the toxic properties of silver through
ingestion of contaminated water and aquatic organisms.

    EPA has not yet established an aquatic life water quality criterion for
silver.  However, EPA has set maximum limits not to be exceeded of 1.2
yg/liter for freshwater organisms and 2.3 yg/liter for saltwater
organisms.
    Thallium

    Numerous cases of thallium poisonings have been recorded, largely as a
result of thallium's medicinal or rodenticidal uses.  Minimum toxic doses in
humans of between 3 and 15 mg Tl/kg have been reported (Clayton and Clayton
1981).  Acute poisoning is characterized by gastrointestinal irritation, acute
ascending paralysis, psychic disturbances, alopecia, and abnormalities of
cardiac function (Clayton and Clayton 1981, Doull et al.  1980, and USEPA
1980).  Autopsies in fatal cases have revealed damage to the gastric and
intestinal mucosa, fatty infiltration of the liver and kidneys, and damage to
the adrenal glands and central nervous system (Clayton arid Clayton 1981).  In
the few reported cases of subchronic and chronic poisoning in humans, symptoms
are similar to those for acute poisoning (USEPA 1980).

    In animal studies, the acute toxicity of thallium compounds exhibits a
particularly narrow range.  Of 14 inorganic thallium compounds administered by
various routes to five animal species, the lowest lethal doses or LD50 values
                                   H-90

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ranged from about 15 to 50 mg Tl/kg (Clayton and Clayton 1981).  In a 90-day
feeding study in rats, doses as low as 30 to 35 ppm in the diet produced
marked growth depression after 30 days.  The major histological change at
these dietary levels was atrophy of the hair follicles and sebaceous glands of
the skin.  At 15 ppm in the diet, the major effect was alopecia (Downs et
al. 1960, as reported in Clayton and Clayton 1981).  Evidence for the
teratogenicity of thallium is inconclusive.  Thallium was administered to
pregnant rats on gestation days 8-10 at 2.5 mg/kg/day or on days 12-14 at 2.5
and 10 mg/kg/day; both dose levels caused maternal toxicity.  In the
offspring, reduced fetal weight and increased incidences of hydronephrosis and
missing or non-ossified vertibrae were reported (Gibson and Becker (1970, as
reported in USEPA 1980).  Dwarfism (achondroplasia) in rats has also been
described as a teratogenic response to thallium salts (Nogami and Terashima
1973, as reported in Doull et al. 1980).  Information is not available on
the carcinogenicity of thallium; however, thallium has shown some mild
anti-carcinogenic effects in experimental animals (USEPA 1980).

    Acute toxicity of thallium to freshwater organisms is reflected in mean
LC50 values for Daphnia magna of 1,400 yg/liter, for the fathead minnow of
1,800 yg/liter, and for the bluegill of 126,000 yg/liter (Dawson et al.
1977, Kimball manuscript, and USEPA 1978, as reported in USEPA 1980).  Chronic
effects have been observed in Daphnia magna at 100-181 yg/liter and in the
fathead minnow at 40-81 yg/liter (Kimball manuscript, as reported in USEPA
1980).

    In saltwater species, an LC50 value of 2,130 yg/liter has been reported
for the mysid shrimp.  The sheepshead minnow and tidewater silverside were
less sensitive to thallium with 96-hour LC50 values of 20,900 and 24,000
yg/liter, respectively (USEPA 1978 and Dawson et al. 1977, as reported in
USEPA 1980).  Chronic effects were observed in the sheepshead minnow at
concentrations between 4,300 and 8,400 yg/liter (USEPA 1978, as reported in
USEPA 1980).

    In freshwater algae, a 50% reduction in chlorophyll a and cell numbers
was observed at 100-110 yg/liter (USEPA 1978, as reported in USEPA 1980).  A
50% inhibition of photosynthesis at 4,080 yg/liter was reported for
saltwater algae (Overnell 1975, as reported in USEPA 1980).

    EPA has established an ambient water quality criterion of 13 yg/liter
for protection of human health from the toxic properties of thallium through
ingestion of contaminated water and aquatic organisms.

    EPA has not yet established an aquatic life water quality criterion for
thallium.
    Zinc

    Zinc salts are astringent, corrosive to the skin, and irritating to the
gastrointestinal tract.  Accidental oral poisonings in humans have produced
such symptoms as fever, vomiting, stomach cramps, and diarrhea (Patty 1963).
Occupational exposure to zinc oxide may result in a characteristic short-term
syndrome.  It generally occurs after a lapse of exposure, for example on
                                   H-91

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Monday mornings or after a holiday.   The symptoms include chills and fever
followed by remission after 24-48 hours, despite continued exposure (Casarett
and Doull 1975).  Zinc chloride fumes may give rise to a grey cyanosis,
dermatosis, and ulceration of the nasal passages and in severe cases may
result in acute pulmonary damage or death (Casarett and Doull 1975).

    In feeding tests on rats, no adverse effects were observed at dosages up
to 5,000 rag/kg.  At 10,000 mg/kg, however, a cessation of growth and some
deaths were seen (Rothstein 1953, as reported in CSWRCB 1963).  No studies are
available showing zinc to be teratogenic, mutagenic, or carcinogenic.

    Zinc has been shown to be acutely toxic to freshwater animals over a range
of concentrations from 0.090 to 58.1 mg/liter, depending on the species tested
and the hardness and temperature  of the water.  In saltwater animals, the
range was from 0.166 mg/ liter to 83 mg/liter.  Zinc concentration from 0.030
to 21.65 mg/liter have been shown to reduce the growth of various freshwater
plant species.  A range of 0.050 to 25.5 mg/liter was found to inhibit growth
in several saltwater plant species (USEPA 1980).

    EPA has not yet established ambient water quality criteria for the
protection of human health from the toxic properties of zinc because of the
lack of sufficient data.  However, using available organoleptic data for
controlling undesirable taste and odor of ambient water, the estimated level
is 5 mg/liter.

    EPA has established an aquatic life water quality criterion for zinc.  For
freshwater species, the 24-hour average criterion is 47 yg/liter, with a
maximum not to be exceeded of 180 yg/liter.  The 24-hour average criterion
for saltwater species is 58 yg/liter, with a maximum not to be exceeded of
170 yg/liter.
                                   H-92

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    5.    Polychlorinated Biphenyls

    The toxic effects of polychlorinated biphenyls (PCBs) in humans are
well-established.  Most human exposures have occurred as a result of the
episode in Japan in 1968 resulting from ingestion of rice oil contaminated
with Kanechlor 400 or from industrial exposure to PCBs (USEPA 1980).  In the
Japanese poisoning incident, initial symptoms included eye discharge, acneform
eruptions, pigmentation of the skin, dermatologic problems, swelling,
jaundice, numbness of limbs, spasms, hearing and vision problems, and
gastrointestinal disturbances.  Blood changes were noted and liver biopsies
revealed histopathological changes.  It has been estimated that the average
amount of PCB ingested by those affected was 2 g (Kuratsune et al.  1972, as
reported in USEPA 1980).  During 1968, ten live and two stillborn infants were
delivered to parents poisoned with PCBs.  Nine of the ten had abnormally
pigmented skin.  Birth weight and growth of the children was significantly
lower than Japanese national standards.  In four babies, gingival hyperplasia,
tooth eruption at birth, bone abnormalities, facial edema, and exophthalmic
eyes were also observed (Yamashita 1977, as reported in USEPA 1980).  Many
symptoms, reported in affected individuals four years after the poisoning
episode, were highly persistent.

         In an occupational setting in which PCB air levels were reported to
be 5.2 to 6.8 mg/cu m, three cases of severe chloracne have been reported
(Puccinelli 1954, as reported in USEPA 1980).  Laboratory workers exposed to
breathing zone concentrations of 0.014 to 0.073 mg/cu m complained of dry sore
throat, skin rash, gastrointestinal disturbances, eye irritation, and headache
(Levy et al. 1977, as reported in USEPA 1980).  Changes in a liver function
test (increased antipyrene clearance) was observed in workers occupationally
exposed to PCBs for at least four years (Alvares et al. 1977, as reported in
USEPA 1980).

         In acute animal studies, PCBs are only slightly toxic.  Oral LD50
values for the rat range from 0.79 to 3.17 g/kg (USEPA 1980).  Toxic effects
of acute doses of Aroclor 1242 include diarrhea, chromoacryorrhea,  weight
loss, unusual stance and gait, CNS deterioration, and histopathologic changes
of the liver and kidney (USEPA 1980).  The more significant toxic effects of
PCBs are observed as a result of repeated exposures and are similar to those
observed in humans.  Adult Rhesus monkeys are particularly sensitive to PCBs.
Aroclor 1248 at 100 or 300 ppm in the diet for 2 to 3 months (total intakes of
0.8-1.0 g and 3.6-5.4 g, respectively) caused high morbidity within one month
and almost 100 percent mortality within three months (Allen 1975, as reported
in USEPA 1980).  Pathological changes of the liver are the most consistent
changes occurring in mammals after exposure to PCBs.  In one study by
Kimbrough et al. (1972, as reported in USEPA 1980), rats fed Aroclor 1254 or
1260 at levels between 20 and 1,000 ppm for eight months showed
histopathologic changes of the liver and porphyria.  Adenofibrosis of the
liver was observed at the higher doses.  Liver pathology similar to that seen
in rats has been reported in mice exposed to 1.5 mg PCB/day (Nishizumi 1970,
as reported in USEPA 1980).  PCB applied dermally to rabbits results in skin
lesions and pathological changes in the liver and kidney (Vos and Beems 1971,
as reported in USEPA 1980).  Female Rhesus monkeys fed low levels of Aroclor
1248 (2.5 and 5 ppm) for 52 weeks developed periorbital edema, alopecia,
erythema, and acneform lesions (Barsotti and Allen 1975, as reported in USEPA
                                   H-93

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1980); effects in males was less pronounced.  Induction of liver microsomal
enzymes has been demonstrated at dietary levels as low as 0.5 to 25 ppm.
Other systemic effects in experimental animals include porphyria, increased
thyroxin metabolism, ultrastructural changes in the thyroid,
immunosuppression, and alterations in steroid metabolism'(USEPA 1980).
Administration of PCBs has resulted in adverse reproductive effects in rats,
rabbits, mice, mink, and Rhesus monkeys.  An increased estrus cycle and a
decreased rate of implantation were observed in mice treated for ten weeks
with 0.025 mg/day Clophen A60 (Orberg and Kihlstrom 1973, as reported in USEPA
1980).  In a study of female Rhesus monkeys fed 2.5 or 5.0 ppm Aroclor 1248 in
the diet for six months before mating, Barsotti and Allen (1975, as reported
in USEPA 1980) observed a decreased rate of conception, live births, and
neonatal body weights and an increase in neonatal deaths.  The carcinogenicity
of PCBs has been demonstrated in mice and rats.  Liver tumors were reported in
mice given PCB in the diet at levels of 500 ppm for 224 days (Ito et al.
1973, as reported in USEPA 1980) and 300 ppm for 330 days (Kimbrough and
Linder 1974, as reported in USEPA 1980).  Kimbrough et al. (1975, as
reported in USEPA 1980) fed Aroclor 1260 to rats at levels of 100 ppm for 21
months and found hepatocellular carcinomas in 26/184 experimental animals but
only one out of 173 controls.  A 1978 National Cancer Institute bioassay (as
reported in USEPA 1980) concluded that Aroclor 1254 was not carcinogenic in
Fischer 344 rats, although a high frequency of hepatocellular proliferative
lesions and an increase in carcinomas of the gastrointestinal tract (not
statistically significant) were considered possibly associated with
treatment.

    The acute toxicity of PCBs to freshwater organisms has been measured in
three invertibrate species with acute values ranging between 10 and 2,400
Vg/liter, and in four fish species with acute values ranging between 2 and
300 yg/liter (USEPA 1980).  In eleven life-cycle or partial life-cycle tests
with three vertibrate and two fish species, chronic effects were reported from
0.2 to 15 yg/liter (USEPA 1980).  In saltwater species, the mean acute
values for the eastern oyster, brown shrimp, and grass shrimp were 20, 10.5
and 12.5 ug/liter, respectively (USEPA 1980).  Two chronic studies have been
performed on the sheepshead minnow; chronic effects were observed at 0.098 to
7.14 ug/liter (USEPA 1980).  Available data for saltwater plants indicate
that unicellular plants are affected by concentrations similar to
concentrations that are chronically toxic to animals, while freshwater algae
are somewhat less sensitive to PCBs (USEPA 1980).

    EPA has established an ambient water quality criterion of zero for the
maximum protection of human health from the potential carcinogenic effects due
to exposure to PCBs through ingestion of contaminated water and aquatic
organisms.  Since the zero level may not be attainable at the present time, a
criterion of 0.079 ng/liter, corresponding to a lifetime incremental cancer
risk of 0.000001, was recommended.

    EPA has established an aquatic life water quality criterion for freshwater
organisms of 0.014 yg/liter as a 24-hour average and for saltwater organisms
of 0.030 yg/liter as a 24-hour average.
                                   H-94

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                                 REFERENCES
AMERICAN CONFERENCE OF GOVERNMENT INDUSTRIAL HYGENISTS, INC (ACGIH).   1980.
Documentation of the Threshold Limit Values.  Fourth Edition.   Cincinnati,  Ohio

CALIFORNIA STATE WATER RESOURCES CONTROL BOARD (CSWRCB).  1963.  Water Quality
Criteria, 2nd ed.  Publication 3-A.  Sacramento,  California

CASARETT, L.J., and DOULL, J.  1975.  Toxicology, the Basic Science of
Poisons.  New York, New York

CLAYTON, G.D., and CLAYTON, F.E., eds.   1981.  Patty's Industrial Hygiene and
Toxicology.  Third Revised Edition.  Volume 2--Toxicology.  John Wiley and
Sons, New York

DOULL, J., KLAASSEN, C.D., and AMDUR, M.O.  1980.  Casarett and Doull's
Toxicology.  2nd Edition.  Macmillan Publishing Company, Inc., New York

ENERGY RESEARCH AND DEVELOPMENT ADMINISTRATION.  1977.  Environmental, Health
and Control Aspects of Coal Conversion:  An Informational Overview.  Vols.  1
and 2.  Oak Ridge National Laboratory,  Oak Ridge, Tennessee.  ORNL/E15-95

ENCYCLOPEDIA OF OCCUPATIONAL HEALTH AND SAFETY.  1971.  International Labor
Organization.  McGraw-Hill, New York

HUEPER, W.C., and CONWAY, W.D.  1964.  Chemical Carcinogenesis and Cancers.
Charles C. Thomas, Springfield, Illinois

INTERNATIONAL AGENCY FOR RESEARCH ON CANCER (IARC).  1972.  IARC Monographs on
the Evaluation of the Carcinogenic Risk of Chemicals to Man.  Volume 1.  World
Health Organization, Lyon, France

INTERNATIONAL AGENCY FOR RESEARCH ON CANCER (IARC).  1972.  IARC Monographs on
the Evaluation of the Carcinogenic Risk of the Chemical to Man.  Volume 3.
Certain Polycyclic Aromatic Hydrocarbons and Heterocyclic Compounds.   World
Health Organization, Lyon, France

INTERNATIONAL AGENCY FOR RESEARCH ON CANCER (IARC).  1973.  IARC Monographs on
the Evaluation of the Carcinogenic Risk of Chemicals to Humans.  Vol. 2:  Some
Inorganic and Organometallic Compounds.  World Health Organization, Lyon,
France

INTERNATIONAL AGENCY FOR RESEARCH ON CANCER (IARC).  1974.  IARC Monographs on
the Evaluation of the Carcinogenic Risk of Chemicals to Humans.  Vol. 3:
Certain Polycyclic Aromatic Hydrocarbons and Heterocyclic Compounds.   World
Health Organization, Lyon, France

INTERNATIONAL AGENCY FOR RESEARCH ON CANCER (IARC).  1979.  IARC Monographs on
the Evaluation of the Carcinogenic Risk of Chemicals to Humans.  Volume 20:
Some Halogenated Hydrocarbons.  World Health Organization, Lyon, France
                                   H-95

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INTERNATIONAL AGENCY FOR RESEARCH ON CANCER (IARC).   1978.   IARC Monographs on
the Evaluation of the Carcinogenic Risk of Chemicals to Humans.  Volume 17.
Some N-Nitroso Compounds.  World Health Organization, Lyon, France

INTERNATIONAL AGENCY FOR RESEARCH ON CANCER (IARC).   1980.   IARC Monographs on
the Evaluation of the Carcinogenic Risk of Chemicals to Humans.  Vol.  23:
Some Metals and Metallic Compounds.  World Health Organization.  Lyon, France

KOCIBA, R.J., KEYES, D.G., BEYER, J.E., CARREON,  R.M., WADE, C.E., DITTENBER,
D.A., KALNINS, R.P., FRAUSON, L.E., PARK, C.N., BARNARD, S.D., HUMMEL, R.A.,
and HUMISTON, C.G.  1978.  Results of a two-year chronic toxicity and
oncogenicity study of 2,3,7,8-tetrachlorodibenzo-p-dioxin in rats.  Toxicol.
Appl. Pharmacol. 46:279-303

NATIONAL ACADEMY OF SCIENCES (NAS).  1977.  Drinking Water and Health.
Washington, D.C.

NATIONAL ACADEMY OF SCIENCES (NAS).  1980.  Drinking Water and Health.  Vol.
3.  Washington, D.C.

NATIONAL INSTITUTE FOR OCCUPATIONAL SAFETY AND HEALTH (NIOSH).  1980.
Registry of Toxic Effects of Chemical Substances.  1979 Edition.  U. S.
Department of Health and Human Services, Cincinnati, Ohio.   DHHS (NIOSH)
Publication No. 80-111

NATIONAL TOXICOLOGY PROGRAM (NTP).  1982.  NTP Technical Report on the
Carcinogenesis Bioassay of Di(2-Ethylhexyl) Phthalate (CAS No. 117-81-7) in
F344 Rats and B6C3F1 Mice.  Technical Report Series No. 217.  U. S. Department
of Health and Human Services, NIH Publication No. 82-1773

PATTY, F.A.  1963.  Industrial Hygiene and Toxicology.  Vol. II.  John Wiley
and Sons, New York

SAWYER, C.N., and McCARTHY, P.L.  1967.  Chemistry for Sanitary Engineers.
McGraw-Hill Book Company, New York

SAX, NI.I.  1975.  Dangerous Properties of INdustrial Materials, 4th ed.  Van
Nostrand Reinhold Company, New York

SEARLE, C.E.  1976.  Chemical Carcinogens.  ACS Monograph 173, Washington, D.C.

STANDARD METHODS FOR THE EXAMINATION OF WATER AND WASTEWATER.  1971.  American
Public Health Association, American Water Works Association, and Water
Pollution Control Association.  13th ed.

TOPPING, D.C., PAL, B.C., MARTIN, B.A., NELSON, F.R., and NETTESHEIM, P.
1978.  Pathological changes induced in respiratory tract mucosa by polycyclic
hydrocarbons of differing carcinogenic activity.  Am. J. Pathol.  93:311-324

U.S. DEPARTMENT OF HEALTH AND HUMAN SERVICES (USDHHS).  1980.  Registry of
Toxic Effects of Chemical Substances.  Cincinnati, Ohio
                                   H-96

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U.S. ENVIRONMENTAL PROTECTION AGENCY (USEPA).   1976.   Quality Criteria for
Water.  Office of Water and Hazardous Materials.   Division of Water Planning
and Standards, Washington, B.C.

U.S. ENVIRONMENTAL PROTECTION AGENCY (USEPA).   1979.   Ambient Water Quality
Criterion for 2,3,7,8-Tetrachlorodibenzo-p-dioxin.  Draft report.   Ofice of
Water Regulations and Standards, Criteria and Standards Division,  Washington,
D.C.

U.S. ENVIRONMENTAL PROTECTION AGENCY (USEPA).   1980.   Ambient Water Quality
Criteria.  Office of Water Regulations and Standards, Criteria and Standards
Division, Washington, D.C.

WASTEWATER ENGINEERING:  COLLECTION, TREATMENT DISPOSAL.  1972.   Metcalf and
Eddy, Inc.  McGraw-Hill Book Company, New York
                                   H-97

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         APPENDIX I
 FATE OF PRIORITY POLLUTANTS  IN
PUBLICLY OWNED TREATMENT WORKS
      Executive Summary

-------
              United States
              Environmental Protection
              Agency
              Effluent Guidelines Division
              WH-552
              Washington DC 20460
EPA 440/1 -82/303
September 1982
vvEPA
              Water and Waste Management
Fate of Priority Pollutants
in Publicly Owned
Treatment Works
             Final Report
              Volume  I
                         1-1

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    PATE OF PRIORITY TOXIC POLLUTANTS



                    IN




      PUBLICLY OWNED TREATMENT WORKS
               FINAL  REPORT






                 VOLUME  I
               PREPARED FOR:




        EFFLUENT GUIDELINES DIVISION




 OFFICE OF WATER REGULATIONS AND STANDARDS




    U.S. ENVIRONMENTAL PROTECTION AGENCY




          WASHINGTON,  D.C.   20460
                 PREPARED BY:






BURNS AND ROE INDUSTRIAL SERVICES CORPORATION




        PARAMUS, NEW JERSEY   07652
                    1-2

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                            PREFACE


This document is being  issued  as  the  Final  Report on a project
initiated by the United States  Environmental  Protection Agency in
1978 to study the occurrence and  fate of  the  129 priority toxic
pollutants in 40 Publicly Owned Treatment Works (POTW) and a
supplemental study conducted at 10  additional POTW.   This report
consists of two volumes.  Volume  I  contains the background and
purpose of study, the POTW  selection  criteria,  the sampling
program details, the overall POTW data, evaluation of analytical
results, and the preliminary conclusions  of the study.  Volume II
contains the Daily Analytical  Results which embody the basic data
generated during the course of  this study and which  are the
source for all other data compilations and  analyses.
                               1-3

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                       TABLE OF CONTENTS

                            VOLUME I


SECTION                                                   PAGE

  I.     SUMMARY, RESULTS AND CONCLUSIONS                   1

         Summary                                            1
         Results and Conclusions                            1

  II.    INTRODUCTION                                       3

         Background                                         3
         Purpose                                            4

  III.   POTW SELECTION AND DESCRIPTION                     5

         Selection Criteria                                 5
         POTW Characteristics                               7

  IV.    DESCRIPTION OF FIELD SAMPLING PROGRAM             15

         Sampling Frequency                                15
         Sampling Techniques                               16
         Sample Points                                     17

  V.     DATA ORGANIZATION AND INTERPRETATION              27

         Data Organization                                 27
         Laboratory Data Reporting Protocol                27
         Data Interpretation and Presentation              30
         Quality Assurance Program                         31

  VI.    EVALUATION AND DISCUSSION OF ANALYTICAL DATA      35

         Overview of Priority Pollutant Occurrence         35
         Summary of Influent Pollutant Concentrations      51
         Impact of Industrial Contribution on Influent     51
           Quality
         Treatment or Removal of Priority Pollutants in    56
           POTWs
         Reduction of Priority Pollutants by POTW          58
           Treatment Processes
         POTW Priority Pollutant Mass Balances             62
         Daily Variation of Influent Pollutant Concen-     64
           trations
         Effect of Rainfall on Influent Concentrations     66
         Formation of Chlorinated Hydrocarbons             66
         Pollutants Detected in Sludges When Not           70
           Measured in the Influent
         Correlation of Influent and Effluent Concen-      70
           trations
         Discussion of 10-Plant Study Results              73

                               1-4

                               iii

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                       TABLE  OF  CONTENTS  (Continued)
SECTION

APPENDIX A



APPENDIX B
APPENDIX C



APPENDIX D




APPENDIX E
Flow Diagrams - Plants  1 to  40  and
51 to 60

Cumulative Distribution Curves  of
Effluent Concentrations and  Percent
Removals for the Twenty-four Most
Frequently Found Priority Pollutants

Summary of Analytical Data - Plants 1
to 40 and 51 to 60

Percent Occurrence of Pollutant
Parameters - Plants 1 to 40  and  51
to 60

Mass Balance in Pounds Per Day
Plants 1 to 40 and 51 to 60
   PAGE

A-1 to A-52


B-1 to B-14
C-1 to C-108


D-1 to D-74



E-1 to E-102
                              1-5

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                               I.

               SUMMARY, RESULTS AND CONCLUSIONS
SUMMARY
In 1978, the United States Environmental Protection Agency  (EPA)
initiated a program to study the occurrence and  fate of the  129
priority pollutants in 40 Publicly Owned Treatment Works  (POTWs).
The first phase of this work was a two-plant pilot study  designed
to set operating parameters for the remainder of the 40 POTW
study.  In October 1979, EPA's Effluent Guidelines Division  (EGD)
published a report summarizing "the findings of the pilot  study
work,  "Fate of Priority Pollutants in Publicly Owned Treatment
Works-Pilot Study," EPA 440/1-79-300.  Upon completion of half of
the POTW project EGD published a report summarizing the findings
for the first 20 POTWs, "Fate of Priority Pollutants in Publicly
Owned  Treatment Works-Interim Report," EPA 440/1-80-301.

In this final report, data from all 40 POTWs plus 10 supplemental
POTWs  sampled under a parallel project are presented.  At most of
these  plants, a minimum of 6 days of 24-hour sampling of
influent, effluent and sludge streams was completed.  Each sample
was analyzed for conventional, selected non-conventional, and
priority pollutants.

Beyond presenting the occurrence and concentration of priority
pollutants in the 40 POTWs (and 10 supplemental POTWs) other spe-
cific  phenomena and relationships are evaluated  in this report.
These  items include:

o Impact of industrial contribution on influent quality
o Treatment or removal of priority pollutants in POTWs
o Reduction of priority pollutants by individual POTW treatment
  processes
o POTW priority pollutant mass balances
o Daily variation of influent pollutant concentrations
o Effect of rainfall on priority pollutant levels in POTW influents
o Formation of chlorinated hydrocarbons through  chlorine  disin-
  fection
o Quantification of pollutants found in sludges but not detected
  in POTW influents
o Correlation of influent and effluent priority  pollutant levels.

RESULTS AND CONCLUSIONS

1.  A total of 102 priority pollutants were detected, at  least
    once, in POTW influents.

2.  In general, the higher the industrial contribution to a  POTW,
    the higher the concentration of priority pollutants in  the
    POTW influents.


                              1-6


                              1

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3.  Based on the 40 POTW data  base,  50  percent  of  secondary
    treatment plants  achieved  a  minimum of  70 percent  reduction
    of total priority pollutant  metals,  82  percent reduction of
    total volatile priority pollutants,  and 65  percent reduction
    of the total base neutral  priority  pollutants.

4.  Tertiary treatment processes reduced priority  pollutants
    slightly better than secondary processes.   Primary treatment
    was less effective than either secondary or tertiary  pro-
    cesses.  Activated sludge, trickling filter, rotating biolo-
    gical contactor and pure oxygen  activated sludge processes
    were approximately equally effective in reducing priority
    pollutant concentrations.

5.  At plants where the metal priority  pollutant mass  balance was
    good, some organic priority  pollutants  in the  influent were
    not always accounted for in  the  effluent or sludges.   This
    indicates that, in general,  a portion of the organic  priority
    pollutants are biodegraded or, in the case  of  volatiles,
    stripped out of the wastewater.

6.  The mass loading of priority pollutants in  POTW influents was
    higher on weekdays than on weekends.  This  was true for the
    metals, volatiles and base neutral  priority pollutants.

7.  Heavy rainfall increased metallic priority  pollutant  mass
    loading at POTWs.

8.  Certain priority pollutant chlorinated  hydrocarbons increased
    slightly in concentration during chlorine disinfection.

9.  Some pollutants not measured in  POTW influents were regularly
    measured at high levels in the corresponding sludge streams.

10. For many conventional and priority pollutants,  as  influent
    concentrations increased effluent concentrations also
    increased.   This implies that the removal rates for the
    priority pollutants are relatively  constant and a  fixed  per-
    centage of incremental loadings  of these pollutants will be
    removed by secondary treatment.
                               1-7

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      APPENDIX J
TREATMENT CATALOG FOR THE



CATALYTIC COMPUTER MODEL

-------
       TREATS NT CATALOG
FOR THE CATALYTIC COMPUTER MODEL
         Catalytic,  Inc.
   Philadelphia, Pennsylvania
         September 1980
               J-l

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                             TABLE  OF  CONTENTS

                                                                      Page
GENERAL DESCRIPTION 	   1
     Process 	   2
     Function 	    2
     Parameters Affected 	   2
     Effectiveness 	   2
     Appl icati on L imits 	   3
     Design Basis 	   3
     Treatability Factor 	   4
     Cost Parameter 	   4
     Cost Curve Scale Factor 	   4
     Resi dues 	   5
     Major Equipment 	   5
TREATABILITY 	   5
TREATMENT CATALOG AND MODEL SEQUENCING RULES  	  11
UNIT PROCESS COST DEVELOPMENT 	  12
UNIT PROCESSES  	  14
     Equalization and Surge Storage 	  14
     Neutralizati on 	  16
     Oil Separation and Dissolved-Air  Flotation  	  18
     Chemical Precipitation, Coagulation,  and Flocculation 	  21
     Clarification 	  23
     Filtration, Dual-Media 	  27
                                     J-2

                                      i

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                 TABLE OF CONTENTS  (Continued)

                                                                Page
Activated SIudge 	 29
Aeration, Biological  Processes  	 34
Nutrients, Biological Processes  	 37
Nitrification, Biological  	 39
Denitrification, Biological  	 42
Ozonation 	 45
Chemical Oxidation 	 47
Activated Carbon Adsorption 	 49
Activated Carbon Regeneration 	 52
I on Exchange 	 54
Sludge Handling And Disposal  -  General  	 56
     Gravity Thickening 	 58
     Aerobic Digestion 	 60
     Vacuum Filtration 	 62
     Pressure Filtration 	 64
     Landfill 	 66
     Incineration 	 68
Ammoni a Strippi ng 	 72
Steam Stripping 	 74
So"vent Extraction 	 76
Cooling Tower/Heat Exchanger/Steam Injector  	 78
Deep-Well Disposal  	 81
Lime Handl ing 	 83
                                 J-3

                                 ii

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                             TREATMENT CATALOG
                     FOR THE CATALYTIC COMPUTER MODEL

     The Treatment Catalog  defines  the basis for  applying  the  unit  pro-
cesses that are to be considered for treatment and disposal  of wastewaters
and their residues.  The unit processes  now in the catalog are not  to
be construed as an all-inclusive list of  commercially available wastewater
treatment processes;  however, they  are sufficiently comprehensive to provide
a "typical" treatment method for any of  the pollutants expected to  be
encountered.

GENERAL DESCRIPTION
     Each unit process  is represented by  a separate entry  in the Catalog.
The first part is a general  description  of the process,  with a discussion
of the design basis and applicable  assumptions for simplification of the
design procedure.  The second part  is a  design data sheet  (or  sheets)
in which the performance characteristics, design  criteria, and key  design
features are specified  under the following headings:
          PROCESS
          FUNCTION
          PARAMETERS  AFFECTED
          EFFECTIVENESS
          APPLICATION LIMITS
          DESIGN
          TREATABILITY FACTOR
          COST PARAMETER
          COST CURVE  SCALE  FACTOR
          RESIDUES
                                       1
                                     J-4

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          MAJOR EQUIPMENT
     The following paragraphs indicate the type of information presented
under each of these headings and provide guidelines for your review and
comment.
Process
     The name of the process is shown at the top of the page.   The unit
processes are arranged in the catalog in three groups:   wastewater treat-
ment processes, sludge treatment processes; and special systems.
Function
     The purpose of the unit process is stated in broad terms, for example,
"Removal of dissolved organics" (Activated Sludge), and "Removal  of suspended
solids" (Filtration, Dual-Media).   Different processes  could have the,
same general function, as in the cases of Activated Sludge and Activated
Carbon Adsorption.
Parameters Affected
     Pollutants which are altered by the process are listed.  The list
is not necessarily all-inclusive,  but includes at least the following:
     1.   Parameters for which effluent limitations were previously
          promulgated by the U.S.  Environmental Protection Agency for
          the organic chemicals industry for BPT.
     2.   Parameters which may affect the applicability, effectiveness,
          and/or cost of other (downstream) unit processes.
     3.   General  classes of pollutants (e.g., dissolved organics) are
          specified when a listing would be too lengthy.  These classes
          include priority pollutants.
     Pollutant characteristics which do not fall into any of the  foregoing
categories are generally omitted (e.g., color), even though they  may be
altered by the process.  In some instances, a parameter may be included
because of prevailing state regulations.
                                       2
                                      0-5

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Effectiveness
     The effectiveness of the process  in reducing  the  affected  parameters  is stated.
In some cases,  this statement may consist simply of  a  percentage  removal or  some
other reliably achievable result (e.g.,  effluent concentration).   In  other  cases,  the
statement is more complex because the  effectiveness  of the  process  is sensitive
to various design parameters  and to the  relative treatability of  the  waste  stream.
In those cases, it is necessary to relate the effectiveness  of  the  process  both to the
waste to which  it is applied  and to the  chosen design  criteria.   These relationships
are expressed or implied in the effectiveness statement and are further defined under
other headings  in the catalog (e.g., Design Basis).
     For most unit processes  there are practical limitations  on effectiveness.   A
"Limit of Effectiveness" statement is  sometimes needed to stipulate that there  is
a limit on percentage removal achievable or that the effluent concentration  will
not be below a particular achievable level.
     For those unit processes involving  consideration  of relative treatability  of
the particular wastewater, a  "reference  case" has  been included in  the effectiveness
statement.  This specifies the effectiveness achieved  for a given wastewater with
a defined treatability and specified design basis.   The design  of this unit  process
for other wastes with different treatability is relatable to the  reference  case.   (See
Treatability Factor and Cost  Curve Scale Factor).
Application Limits
     Waste characteristics that must be  controlled within certain ranges  in  order
for the process to function properly are described.  For example, the pH of  wastewater
generally must be controlled  within a range of 6.0-8.5 in order that  a biological  proc
such as activated sludge, can be applied.  (These  are  exceptions, however.   For examp-
if the wastewater exists as a buffered solution in an  aeration  basin, then  excursions
of pH in the influent stream  can be tolerated.  These  exceptions  are  not definable
with the data available for this study.)  If the waste characteristics are  not  within
the prescribed range, then a  preceding unit process  (e.g.,
                                    3
                                   J-6

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neutralization) is applied so as to bring the characteristic withTn the
required range.
Design Basis
     The process design basis is specified.   In some cases,  this consists
of specifying a design loading such as' an overflow rate or hydraulic residence
time.  In others, particularly when relative treatability has a major
impact upon cost, a functional relationship  between design ("size") and
performance is indicated.
Treatability Factor
     For each unit process, this heading will include absolute and relative
treatability information for each pollutant  affected by that unit  process.
This information is discussed systematically in the TREATABILITY Section
of this document.
Cost Parameter
     A cost curve has been developed for each unit process,  relating capital
cost to a basic parameter representative of  the size (and, therefore, the
cost).  In some cases, a second cost parameter is required for adequate
description of the cost of the system in terms of its size.   The cost curve
will then be a family of curves on the same  graph.
Cost Curve Scale Factor
     For those unit processes involving a treatability factor, the cost
estimates (and cost curves) are based upon a reference case.  The  design
of the process and its cost were determined  for a given value of the treata-
bility factor.  The cost parameter, in those cases, does not fully define
the system size; it is necessary to refer to the reference case to do
so.  For example, the cost parameter for activated sludge is flow  rate.
However, the cost of an aeration basin is determined by the  volume of
the basin, which is a function of both the flow rate and the detention
time.  The detention time is directly related to the treatability  of the
waste.  In order to disassociate the system  cost curve from  the treatability
                                       4
                                      J-7

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of the particular waste encountered in the reference  case,  flow rate was
chosen as the cost parameter.   Although the cost curve is based upon the
reference case (at different flow rates),  the size of a basin  (and therefore
the cost) can be determined for any application once  the detention time
is specified.  This is achieved by comparing the detention  time with that
of the reference case and scaling the flow rate up or down  as  indicated.
The detention time in this case (activated sludge),  is termed  the Cost
Curve Scale Factor.
     Another use of the Cost Curve Scale Factor is as a multiplier of
a unit cost.  This is used, for instance,  in aeration, where the cost
factor is individual-aerator horsepower and the scale factor  is the number
of aerators.  The cost estimate for one aerator (including  associated
instrumentation, electrical connections, structural  supports,  etc.) appears
in the cost curves and then is multiplied  by the number of  aerators (of
the same horsepower)  required.
Residues
     Any residues (solid, gaseous, or liquid) generated by  the process
are identified as to type and quantity.  Either additional  unit processes
are provided for their treatment and disposal,  or processes already included
in the treatment scheme for some other purpose  are designed to handle them.
Major Equipment
     The major equipment and facilities that must be  installed for this
unit process are identified.  The key features  that  affect  cost (such
as materials of construction,  operating mode, and process variants) are
also indicated,

TREATABILITY
     The treatability of various pollutants and product/process waste
streams had to be assessed and quantified to enable the model  to predict
contaminant removals in the various unit processes.   The problem of predic-
                                      5
                                     J-8

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tion is different for conventional  parameters (e.g.,  BOD,  TSS)  than for
specific pollutants.   These differences in assessment of treatabi1ity
are highlighted in the following discussion of the requirements for modeling
each treatment unit processes.
Equalization
     No treatabi 1 ity factors are involved in this unit process.  The function
of equalization is to lessen the variability of the raw waste load.   The
average values of parameters are unaffected.  The only exception is waste-
water temperature, which will  move toward the ambient air  temperature
during the 1-day holding time in the equalization basin.
Neutral ization
     Again, there are no treatabi1ity factors involved.  The size of the
basin is determined by the wastewater flow, while the chemical  requirements
are determined by acidity/alkal inity values (if available) or by pH values
if acidity/alkalinity are not reported.  When no data (acidity/alkalinity
or pH) are reported,  a neutral pH is assumed.
Oil Separation and Dissolved Air Flotation
     There are no treatability factors for oil and suspended so'lids removal.
Basin size is determined by wastewater flow rate.  Oil and TSS  removal  are
predicted on the basis of operating experience.   Organic pollutants are
assumed to be removed down to their solubility in water.  (These solubilities
are taken from chemical handbooks.)
Coagulation and Flocculation
     The treatability factors required for this unit process are the chemical
coagulant used, the ratio of chemical  to pollutant, and the remaining
solubility of the precipitate formed for ion being removed.  These factors
are obtained from operating experience and chemical handbooks,  supplemented
as necessary by laboratory tests on metal-ion compounds for which the
literature provided inadequate solubility data.
                                      6
                                      J-9

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Clarification
     Specific treatability factors are required.   Different overflow rates, effluent
TSS concentrations, and  underflow TSS concentrations for various types of suspended
solids are given in the  design data sheet for the clarification unit process.
Activated Sludge
     The treatabil ity factors required for this unit process are the biological reacti
rate coefficient (k factor) and the maximum attainable percent removal.   The k
factor has been estimated by grouping chemicals according to relative biological
degradability;  k rates  for five classes, ranging from extremely biodegradable to
bio-static or toxic, have been assigned.   The biological treatability of different che:
has been related to chemical structure and functional  group.  The k factors for produc
BOD's have been estimated by taking the average of the k's for the raw materials,
intermediates, and  products that make up  a particular  product process.  Other sources
of biological kinetics data and maximum percent removals are Screening/Verification
data and responses  to the 308 questionnaire.
 Aeration, Biological Processes
     There are no treatability factors involved.   The  power required depends on
the oxygen transfer rate in the wastewater, oxygen solubility, and oxygen utilization
rate, which in turn depends on the amount of  BOD to be removed and the amount
of MLVSS under aeration.
Nutrients, Biological Processes
     There are no treatabi1ity factors involved.   The  amounts of nitrogen and phosphor;
to be added are the amounts necessary to  maintain a BOD:N:P ratio of 100:5:1, based
on using anhydrous  ammonia and 75 percent phosphoric acid.
Nitrification
     The treatabil ity factor is a temperature correction, which affects the design
nitrification rate.  The design data sheet includes a  plot
                                       7

                                     J-10

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of temperature vs. percent of design nitrification rate.
Denitrification
     As with nitrification, the treatability is a temperature correction.
The design data sheet includes a plot of temperature vs.  percent of  design
denitrification rate.
Ozonation
     Three treatability parameters are involved:   1) the  ozone/pollutant
ratio required for treatment;  2) the normal lower level  of effluent treat-
ment achieved; and  3) the upper level of effluent treatment normally
expected.  These values have been obtained for a few pollutant parameters
from surveys of the technical literature.

Chemical Oxidation
     The treatability factors are similar to those for ozonation,  but
the oxidation chemical must be specified in addition to the chemical/pollutant
ratio and the lower  and upper expected effluent values.
Activated Carbon Adsorption
     There are four  treatability factors needed,  and they are:
          1.   Isotherm constant - Langmuir constant related to the
               slope of the isotherm plot.
          2.   Isotherm constant - Langmuir constant related to the
               intercept and slope of the isotherm plot.
          3.   Final value - lowest  attainable effluent value mg/1.
          4.   Peclet number.
Activated Carbon Regeneration
     There is no  treatability factor  involved.  The function of the  regenera-
tion furnace is to remove the adsorbed organics from the  spent activated
carbon, so that the  carbon can be reused in the adsorption unit.
                                                                          2
     Regeneration loadings have  all  been given the same value: 40 Ib/hr/ft  .
This rate may vary for different chemicals  adsorbed onto the carbon, as
                                      J-ll

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indicated by activated-carbon  and incineration  equipment manufacturers.
The value selected for the model  is probably on the  low side  of  the  actual
average.
Ion Exchange
     The treatability factors  needed for this unit process  are resin type
(cationic or anionic), resin  exchange capacity,  effluent concentration
attainable,  regeneration chemical to be  used,  and regeneration chemical
dosage.  These have been obtained from the  literature  and from vendor
data.
Gravity Thickening
     There are no treatability factors.   The function  of this unit process
is to increase the solids concentration, and thus facilitate  the operation
of the subsequent sludge-handling processes.
Aerobic Digestion
     The treatability factor  in this unit process is a temperature correction,
which has a significant effect on the rate  of reduction of  the volatile
suspended solids  in waste activated sludge  from biological  treatment.
The equation for this effect  is included in the design data sheet for
Aerobic Digestion.
Vacuum Filtration/Pressure Filtration
     There are no treatabi 1 ity factors.   The function  of either  of these
unit processes is further removal of water  from the  sludge  to prepare
the sludge for landfill ing or incineration.  Pressure  filtration is  the
preferred pretreatment for incineration  because it yields a drier sludge.
Landfill
     There are no treatability factors.   This is a method of  ultimate
disposal for ash residues and dewatered  sludges.
I nc i ner at i on
     Sludge moisture content  is the treatabi1ity factor in  this  unit process.
                                     9
                                    J-12

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The moisture content determines whether the incineration of the sludge
is self-sustaining, or whether (and how much) auxiliary fuel is required.
Ammonia Stripping
     There are no treatability factors.  The function of this unit process
is to remove ammonia from wastewater by direct injection of steam, and
thus meeet the limitation on ammonia concentration in the effluent.
Steam Stripping
     The factors required for steam stripping are pollutant latent heat,
azeotropic composition, molecular weight, achievable effluent concentration,
activity coefficient, K-value (function of the activity coefficient and
the partial pressure), stripping-steam requirements, and tray efficiency.
This information is available from chemical manufacturers and handbooks.
Steam stripping tray effieciencies at low effluent concentration must
be verified by laboratory experiment, to confirm or modify the calculated
values currently being used.
Solvent Extraction
     Treatabil ity factors needed for this unit process are:  the solubility,
latent heat, 'and specific heat of the pollutant; identification of the
solvent; the solvent density; and solvent-pollutant distribution coefficient.
Pollutant properties are obtained from manufacturers and chemical  handbooks.
     Two solvents have been chosen for solvent extraction:   tricresyl
phosphate and a mixture of C,Q-C-,? paraffins (mostly straight-chain).
Solvent density can be obtained from manufacturers or from the literature.
The distribution coefficient for tricresyl phosphate was estimated from
the literature.   Its affinity for phenol  is estimated to be eight times
that of benzene for phenol; since the distribution coefficient for a benzene-
phenol system is about 2.5, the distribution coefficient for tricresyl
phosphate has been assumed to be  20.  The distribution coefficient for
the C]Q-C-i2 paraffin has been assumed to be 30,  based on textbook discussions
and examples of solvent extraction where it was  used to remove chlorinated
                                     10
                                     J-13

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hydrocarbons.  These assumptions need to be confirmed by laboratory experiment.
Cooling Tower/Heat Exchanger/Steam Injector
     There are no treatability factors.   A cooling tower or  heat exchanger
is introduced into the unit process trail to reduce the  wastewater temperature
to meet the operating requirement of a biological  treatment  system, or
to conform to the temperature limitation on discharge of treated wastewater
to a receiving stream or other body of surface water. A steam injector
may be required in winter to heat a waste stream for biological  treatment.
Deep-Well Disposal
     There are no treatability factors.   The function of the deep well
is ultimate disposal of liquid wastes.
Lime Hand! ing
     There are no treatability factors.   The function of this unit process
is to provide lime (or caustic) for neutralization and other unit processes.

TREATMENT CATALOG AND MODEL SEQUENCING RULES
     This treatment catalog and the computer model derived from it do
not include  all the possible treatment unit process alternatives.  The
inclusion or exclusion of specific unit-process types or configurations
does not  imply that the process types included in this treatment catalog
are the only ones applicable to the treatment of the subject waste streams.
The processes that have been included were chosen because they are widely
used and  provide representative treatment costs.
     Chemical plants should have flow and/or contaminant equalization
someplace in the treatment system, and possibly also in  connection with
storage or monitoring of the treated effluent.  The cost of  this unit
can be effectively represented by the rules stated herein.
     Many plants will have to transfer the waste  streams by  means of  a
lift station someplace in the treatment system.   If they do  not so require,
sewer complexities or other waste-hand! ing problems will add some increment
                                     11
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of cost, and that increment is assumed to be equivalent in  cost impact
to a lift (pumping) station.
     Almost every plant requires some form of neutralization,  even if
only on an intermittent basis, and some type of facilities  for this  purpose
will be provided.
     Liners for large earthen basins will be of the synthetic-membrane
type, rather than clay.  Landfill liners will also be of the synthetic-
membrane type.

 UNIT PROCESS COST DEVELOPMENT
     The unit process costs were developed by preparing detailed Flow
Sheets, sizing the equipment, obtaining vendor quotations for major  items,
and then using standard estimating procedures to determine  installed costs.
The basic design parameters appear in the Treatment Catalog.   Flow Sheets
were constructed to establish the kinds of equipment required for a  unit
process. Equipment was sized according to specifications in the Treatment
Catalog where specified,  and by standard engineering calculations for
equipment items or processes that were not so specified. After equipment
was sized, an equipment list was prepared for estimating purposes.
     This equipment list includes the identification and size of each
significant item of hardware for each size range of each treatment unit
process.  It includes all  mechanical equipment, basins, structures,  vessels,
and piping, but does not  cover labor costs or instrumentation.   The  Catalytic
Estimating Department estimators used this list as the basis for determination
of the installed cost of  a unit process (based on costs in  the St. Louis,
Mo. area as of June 1977).  These installed costs included taxes, insurance,
legal fees, contingencies,  and overhead.  The flow diagram  for each  unit
process shows all instrumentation and thus serves as a basis for estimating
the instrumentation costs.
     Obviously, it is not practical  to prepare cost estimates  for all
possible sizes of a unit  process.  On the other hand, it is not good practice
                                     12
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to use one cost estimate (base case) as the basis for all  sizes, 'because
the cost of a treatment facility is not necessarily directly proportional
to its size.  Consequently, a compromise approach was taken, involving
four separate cost estimates generally covering a unit process size range
of three orders of magnitude.  For all  unit processes designed to treat
the wastewater forward flow to a treatment plant, flow rates of 0.2,  1,
5, and 20 MGD were used as the basis for the cost estimates.
     The four ensuing cost estimates were used to establish the cost curves,
which indicate the installed cost of each unit process as  a function of
the "cost parameter" involved.  This cost parameter,  for example, may
be a flow rate, basin volume, or surface area.  Although there can be
only one "cost parameter" for a given unit process, there are other variables
that may affect  the cost curve.   Thus, the "cost parameter" may be multiplied
by a "scale factor" to provide the necessary adjustment.  These scale
factors are indicated on the design data sheet for each unit process.
     In addition to the costs of the individual unit processes, there
are many miscellaneous costs that must be considered such as: home office
engineering, site development work, utility and general piping, electrical
requirements, a control building, and a sanitary sewage pumping station.
These costs are introduced into the model as functions of the total capital
cost of the unit processes, the total operating horsepower, and the number
of unit processes.  The overall  miscellaneous cost is then allocated back
to the individual unit processes.  This allocation of the miscellaneous
costs to each unit process reflects the ratio of the individual unit process
cost to the total cost of all the unit processes, as defined by the cost
curves.
                                       13
                                     J-16

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                      EQUALIZATION AND SURGE STORAGE

     Start with an equalization basin with capacity  equivalent  to  the 24-hour filling
volume based on average total  wastewater  forward flow,  and  with a  separate surge
basin with a capacity equivalent to a similar  12-hour filling  volume.  Provide  a pumpir
station, equipped with two  pumps each with a capacity equal to  120 percent of the
daily average total  wastewater forward flow.
     If the ratio of the maximum daily flow to the  average  daily flow (or the ratio
of the average to the minimum) exceeds 2.0,  increase the  size  of the basins in  accordar
with the following formula:
          New Size = Base Size x    (Larger Flow Ratio  -  2.0) + 1.0
     If the ratio of the maximum calendar-month flow to the average daily flow
(or the ratio of the average to the minimum) exceeds 1.5, increase the size of  the
basins in accordance with the  following formula:
          New Size = Base Size x    1.5 (Larger Flow Ratio  -  1.5)  + 1.0
     If both ratios* are in  excess of  the  designated  limits, calculate both increases,
but use only the larger of  the two.
     All equalization basins are equipped with mixers.  The design power demand
on the mixers is 0.01 HP per 1,000 gallons of  wastewater  volume, and costs are  based
on floating mechanical mixers.*
     In addition to reducing the flow variability  and pollutant concentrations, equali;
will cause the wastewater temperature to  approach  ambient temperature.  This change
is accounted for with a temperature balance model  that  includes heat gains from
influent wastewater, mechanical  action, and solar radiation,  and heat losses from
effluent flow, evaporation,  and surface and sidewall convection/conduction.
     See the attached design data sheet for additional  details.
     This power requirement  is based on providing  adequate mixing, and
     is not intended to prevent all  influent  suspended  solids from settling.
                                      14
                                      J-17

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                        EQUALIZATION/SURGE STORAGE
FUNCTION:


PARAMETERS
AFFECTED:

EFFECTIVENESS
APPLICATION
LIMITS:

DESIGN BASIS:
TREATABILITY
FACTOR:

COST PARAMETER:

COST CURVE SCALE
FACTOR:

RESIDUES:

MAJOR
EQUIPMENT:
Equalization of flow and concentration.
Capture of concentrated spills to process sewer.
Hourly fluctuations of flow and pollutant concentration.
Wastewater temperature

Essentially complete homogeneity of average daily
     flow, excluding major spills.
Spills diverted to separate surge basin if detected
     in time.
Reduces excessive temperature.

None
Equalization Basin C.apacity:   24-hour detention time
     for average daily flow.*
Mixing Energy:  0.01 HP/1,000 gallons.
Surge Basin Capacity:   12-hour detention time for
     average daily flow.*
Equalization will always be provided.

None

Flow rate

Based on flow variability
Solids accumulation dredged every 5 years.
Equalization Basin and Surge Basin Construction.
 550,000 gal: earthen basin with membrane liner
     (concrete abrasion pads under mixers)
200,000-550,000 gal: earthen basin with concrete-lined sides
** 20,000-200,000 gal:  lined carbon steel tank
**  20,000 gal: stainless steel tank
Mixers:
     Floating mechanical mixers
Lift Station for each basin
                                     15

                                     J-18

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**
Capacity will  be greater if the maximum:average or average:mini mum
flow ratios exceed the limits specified in the general  discussion.
No surge basin for these sizes.
                              NEUTRALIZATION

     The basic component of the neutralization unit is a 2-chamber tank
with design retention times of 5 minutes for the first chamber and 20
minutes for the second chamber.   Normally, the value of 120 percent of
the average wastewater flow is used in conjunction with these residence
times to calculate the size of the chambers.  However, if neutralization
is to precede equalization for any reason (e.g., to avoid the use of expensive
corrosion-resistant materials in an oil  separator, which must precede
equalization), the flow value used in this calculation is 200 percent
of the average wastewater flow.
     Both chambers are equipped with mixers and with pH controllers for
acid and base addition.  Facility design and capital costs for acid addition
are based on sulfuric acid addition for all ranges.  The base-addition
facilities (and the related costs) are different for systems of different
sizes.  Caustic is specified for small systems (less than 500 Ib/day),
hydrated lime for systems requiring 500-800 Ib/day, and quick lime for
those requiring more than 8,000 lb/d-ay.   Lime storage silos and slakers,
and caustic make-up facilities are not part of this unit process; they
are included under "LIME HANDLING".
     Chemical dosages are calculated whenever the acidity or alkalinity
of the raw wastewater is known.   For cases where this information is not
available, a continuous demand of 200 mg/1 of sulfuric acid is assumed.
This value is considered valid for these cases where no acidity or alkalinity
information is available because it is highly likely that alkalinity or
pH data would be available if higher alkalinity were present.  For systems
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                                      J-19

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whose data indicate an essentially neutral  condition,  a continuous demand
of 50 mg/1 is used, to accomodate the occasional  pH swings  that can be
expected in normal  operation.
                                    17
                                   J-20

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                              NEUTRALIZATION
FUNCTION:

PARAMETERS
AFFECTED:
EFFECTIVENESS:


APPLICATION
LIMITS:

DESIGN BASIS:
TREATABILITY
FACTOR:

COST PARAMETER:

COST CURVE SCALE
FACTOR:

RESIDUES:
MAJOR
EQUIPMENT:
pH Adjustment
pH
Acidity
Alkalinity
Will achieve control within a pH unit range of  -0.5
to +1.0 of target.


None
Dual (acid/base) titration with lime and sulfuric acid.
Dosages:
     50 mg/1 of lime or H2S04 for neutral  wastes
     200 mg/1 of lime or H^SO* for undetermined wastes
     Actual alkalinity or acidity where data are  available
Two-stage reaction chamber, having five-(5) and twenty-
     (20) minute detention times, based on 120  percent
     of average flow.

None
Flow Rate


2.0, when neutralization precedes equalization.

To be determined on case-by-case basis.
Depending upon waste characteristics, gases may evolve
     (e.g., HpS), or inert solids may be generated.
Reaction chambers with mixers:
  0.2 MGD - Concrete, Acid-Brick-Lined
  0.2 MGD - Fiberglass Tanks
Sulfuric Acid Storage Tank, carbon steel
Sulfuric Acid Feed Pumps (centrifugal type) with  a
     closed-loop recycle.
Dual pH Control Units (one for coarse controls, one
     for fine control) with panel.
Caustic or Lime Storage and Feed Equipment, carbon steel
                                      18

                                      J-21

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                OIL SEPARATION AND DISSOLVED-AIR FLOTATION

     Since these two unit process are so frequently and so closely related,  they
are discussed together.   However, each process  is  available to  the model  separately.
     Before selecting the unit process to be applied,  determine the characteristics
of the oil, grease, and other floating and floatable materials  present in the subject
product/process, to determine the applicability (effectiveness) of each of these two
treatment process.   This is the basis for selection of either process  or  of  both proce:
in series.  In all  cases, the design  flow rate  is  120  percent of the average wastewatei
flow, and a minimum of two (2) units, each at 50 percent of design capacity, will
be provided.
     A chemical (coagulant) mix tank  and a feed system are listed for  Dissolved
Air Flotation (DAF).  This equipment  is to be used only with DAF and not  with gravity
oil separation.
     When no information is available, the following rules apply:
For oil and grease concentrations:
     Greater than 150 mg/1         Oil Separation  followed by Dissolved-
                                   Air Flotation for all cases.
     Between 35 and 150 mg/1
       Feed to subsequent          Oil Separation  with effluent at 35  mg/1
       activated sludge or         or 50 percent removal,  whichever is
       chemical coagulation        lower.
       steps.
       All others,  including       Oil Separation  followed by Dissolved-Air
       direct discharge.           Flotation with  effluent at  10 mg/1.
     Below 35 mg/1                 Oil Separation with effluent at 10  mg/1.
For floatable solids:              Dissol ved-Air Flotation in  all cases.
     See  the attached design data sheets for more details.
     Disposal of separated solids and oils is described at the  beginning
of the Sludge-Handling section of this treatment catalog,  and  the available
Sludge-treatment trains  are listed in the accompanying table there.
                                      19
                                     J-22

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                              OIL SEPARATION
FUNCTION:

PARAMETERS
AFFECTED:

EFFECTIVENESS:
APPLICATION
LIMITS:

DESIGN BASIS:
TREATABILITY
FACTOR:

COST PARAMETER:

SCALE FACTOR:

RESIDUES:


MAJOR
EQUIPMENT:
Removal of floating oil  and solids
Floati ng oil
Floatable or Floating Solids
Can achieve effluent concentration  of 35 mg/1  floating  oil,
or 10 mg/1 floating oil  for low-influent  concentrations.


None
                            p
Overflow Rate = 1,000 gpd/ft  unless specific  data
     indicate otherwise.
Maximum horizontal velocity = 3 ft/min.


None
Flow rate

None
Oil and sludge
Quantity to be determined upon application
Splitter box, concrete,  with acid-proof  lining
*0il Separation Unit, concrete with acid-proof coating
*Skimming Mechanism
*Bottom Flight Scrapers
Sludge Removal Pumps (positive-displacement  type)
Oil Sump, concrete, with acid-proof coating
Oil Pumps
Slop-Oil Tank, FRP
          Minimum of two (2) units
                                      20

                                      J-23

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                          DISSOLVED-AIR FLOTATION
FUNCTION:

PARAMETERS
AFFECTED:

EFFECTIVENESS
APPLICATION:


DESIGN BASIS:
TREATABILITY
FACTOR:

COST PARAMETER:

RESIDUES:

SCALE FACTOR:

MAJOR
EQUIPMENT:
Removal of suspended and colloidal  materials.

TSS
Free oil

80 percent removal efficiency
Limits of effectiveness:
     TSS will not be reduced below 30 mg/1
     Free oil will not be reduced below 10 mg/1

Flow, TSS, temperature and pH must not be highly
f luctuati ng.

50 percent recycle
Pressurized recycle aeration for 2 minutes ?@  50 psig
Overflow rate  2 gpm/ft
Preceded by flocculation


None

Flow rate

Float: Characteristics to be defined upon application

None

Rectangular flotation clarifier with skimmer and bottom
     sludge removal; pressure tank; controls (carbon
     steel or concrete)
Centrifugal compressor, carbon steel
Flocculation chamber, carbon steel or concrete
Polymer storage and feed system (housed in steel-sided
     building), fiber-reinforced plastic
Chemical mix tank, concrete
Chemical mix tank agitator, carbon steel
Sludge pump, carbon steel
Float  sump, concrete or carbon steel
Float  pump, carbon steel
                                      21

                                     J-24

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           CHEMICAL PRECIPITATION,  COAGULATION,  AND FLOCCULATION

     This unit process is used for  removal  of heavy metals and  solids
specifically noted as requiring coagulation,  and for removal  of specific
dissolved materials such as sulfates or fluorides.   Proper design  requires
a file of solubility data for each  potential  parameter.   (Dissolved-air
flotation has its own chemical feed system,  and  does not utilize  this
unit process).
     Coagulation/flocculation is followed by  clarification or filtration,
depending upon the quantity and nature of the solids produced.  The occurrence
of a large amount of good floe favors the use of clarification; conversely,
small amounts and relatively poor floe favor  the use of  filtration.
     Separate mixing and flocculation chambers are  used, with a mix time
of two (2) minutes and a floe time  of twenty  (20) minutes, based on 120
percent of the average flow.  Since it is seldom possible in  practice
to achieve theoretical levels, dissolved materials  will  be removed to
a level 1.5 times the solubility of the resultant precipitated  material
in water.  Lime and polyelectrolyte will be  used as typical chemicals
for costing purposes.  A polyelectrolyte dosage  of  1 mg/1 is  used  in all
c as es.
     See the attached design data sheet for  more details.
                                      22
                                      J-25

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                       COAGULATION AND FLOCCULATION
FUNCTION:


PARAMETERS
AFFECTED:

EFFECTIVENESS:


APPLICATION
LIMITS:

DESIGN BASIS:
TREATABILITY
FACTOR:

COST PARAMETER:

SCALE FACTOR:

RESIDUES:
MAJOR
EQUIPMENT:
Conversion of dissolved,  colloidal,  and certain
suspended solids to settleable suspended solids.
Dissolved solids (TDS)
Heavy metals

Dissolved ion removal  to 1.5 times the solubility
of the precipitated material in water.


pH, depending upon ions to be removed.

Mix time:  two (2) minutes for coagulation.
Floe time:  twenty (20) minutes.
Chemical dosage:  1.5  x stoichiometric requirement
     for precipitation.
Polyelectrolyte dosage:  1 ppm.


None
Flow
Square root of the number of treatment chemicals used
Precipitate is removed by CLARIFICATION or DUAL-MEDIA
     FILTRATION, depending upon concentration and
     floe characteristics.

Influent splitter box  (concrete)
*Reactor Chambers (concrete), with agitators
*Flocculation chambers (concrete), with flocculators
Polymer  storage and feed systems
          Minimum of two (2) units
                                      23

                                     J-26

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                               CLARIFICATION

     The clarification process is used for removal  of primary suspended
solids, chemically-produced suspended solids from coagulation and floccula-
tion, and biological suspended solids from biological unit processes.
Pollution parameters affected are total suspended solids (TSS),  plus  those
specific parameters made insoluble through chemical  precipitation.
     All clarification is categorized as one'of three types:   primary
clarification without chemical treatment, primary clarification  with  chemical
treatment, and secondary clarification following biological  treatment.
Special applications, such as lime settling prior to ammonia stripping,
may be associated with any of the three basic forms.
     The design basis and effectiveness for the clarification process
are based on separate overflow rates for primary sludges,  activated sludge
(based on the Food/Microorganism (F/M) ratio), other biological  sludges
(nitrif ication/denitrif ication), alum sludges, iron  sludges,  and lime
sludges.  In the case of activated sludge, correction factors for effluent
quality are included for influent MLSS concentrations and  dissolved solids.
These correction factors are included in the design  data sheet which  follows.
     In all cases, two clarifiers (in parallel) are  included, to insure
continuous operation.  Each clarifier has a capacity of 50 percent  of
the total design flow.
     The effluent suspended solids (TSS) levels indicated  on the specifica-
tion sheet for activated sludge - 30 mg/1 for F/M range of 0.2-0.6  and
40 mg/1 for F/M range of 0.05-0.19 - seem well supported by the  analysis
of the November 1977 308 data.  (The data involved in this analysis represent
long-term averages of all the plants for which data  were available.)
     These data, however, do not support any consistent relationship  between
influent BOD to the activated sludge system and the  effluent TSS from
the clarifier.  Nevertheless, there is a sound basis for a relationship
                                        24
                                       0-27

-------
between the solids loading in the  clarifier  and the effluent TSS.  As
the activated  sludge mixed liquor suspended solids (MLSS) increases for
a given size of clarifier, there should  also be an increase in the suspended
solids concentration in the clarifier  overflow.  Consequently, an increase
in effluent TSS from this relationship would take into account the higher
MLSS required when the influent BOD is higher and/ or  where the biological
reaction is lower because of a lower temperature.
     The proposed TSS correction in the  Treatment Catalog for a  change
in MLSS is:
          Addition to base- level effluent  TSS = ^SS-IOOO
This correction, plus a TSS correction for change in  Total Dissolved Solids
-* — ing    would provide for a maximum clarifier effluent TSS, as shown
in the following sample calculation for  a  system with an F/M ratio of
0.2-0.6, an MLSS concentration of  4000 mg/1, and an influent TDS concentration
of of 10,000 mg/1:
                     on + 4000-1000 ,  10,000-4000
                   - JU f           f
                   =30+60+60
                   = 150 mg/1
     This correction procedure is in agreement  with  industry's  comments
on the Treatment Catalog on a previous  organic  chemicals study  for the
National Commission on Water Quality (NCWQ).
                               CLARIFICATION

FUNCTION:           Removal of suspended solids
PARAMETERS
AFFECTED:           Suspended solids (TSS)
APPLICATION
LIMITS:             None
                                     25
                                    J-28

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EFFECTIVENESS/
DESIGN BASIS:
TREATABILITY
FACTOR:

COST
PARAMETER:

COST CURVE SCALE
FACTOR:

RESIDUES:
Type of Sol ids


Primary Chemical
  Alum
  Iron
  Lime
  Sulfide

Activated Sludge*
  F/M:  0.2-0.6
  F/M:  0.05-0.19
Other Biological**
Overflow
  Rate
   800
   500
   700
   800
   500


   500
   500
   400
                      *Influent MLSS correction =
  Effluent
    TSS
   (mq/1)

     50
     20
     20
     20
     50


     30
     40*
     30

MLSS-1000
   50
 'Underflow
Concentration
                       Influent TDS correction  =
                                                _ TDS-4000
                                                     100
                                                                    3
                                                                    1.5
                                                                    3
                                                                   10
                                                                    2
                                                                    1
                                          Addition to effluent
                                          TSS as described in
                                          the preceeding
                                          discussion
 **For biological nitrification and denitrification systems,
   the lowest overflow rate will be used.   Effluent and TSS
   and underflow concentrations will be weighted averages.

As per design basis

Surface area
None
Depending upon application (source):
Clarifier bottom sludge of the quantity and characteristics
     defined above.
                                     26

                                     J-29

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                         CLARIFICATION  (Continued)


MAJOR               Clarifiers:
EQUIPMENT:               Two provided,  each  with  capacity for 50 percent
                         of  the  waste water  flow*
                         Concrete bottom and side  walls
                         Clarifier mechanism with  gear drive and motor
                         Peripheral  weir and baffle
                         Surface skimmer and scum  pit
                         Scum pump

                    Sludge pumps (applies for primary or other  chemical
                         sludges only;  for recycle pumps for activated
                         sludge  process, see ACTIVATED SLUDGE).

                    Influent splitter box (concrete)
     Could be more than two clarifiers.   These would be equal  in size,
     and together would have capacity for 100% of the wastewater flow.
                                       27

                                     J-30

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                          FILTRATION, DUAL-MEDIA

     The filtration process  is used for the removal  of  suspended  solids,  such  as  residi
biological solids in settled effluents from secondary treatment and residual chemical
solids after alum, iron, or  lime precipitation and settling.   In  these  applications,
filtration may serve either  as a necessary preliminary  step to further  treatment
(such as carbon adsorption or ion exchange),  or as a final polishing  step following
other processes.  In cases where chemical  treatment is  used and only  a  small quantity
of floe is generated, filtration rather than  clarification is  used to remove the  solids
from the wastewater.
     Oil, at low influent levels, can also be removed by  this  unit process.
     The design for filtration is based on a hydraulic  loading that varies with influer
                                 ?              ?                                   2
TSS concentration from 2.5 gpm/ft  to 7.9  gpm/ft , with a backwash rate of 20  gprn/fr"
for 15 minutes per cycle.  In conjunction  with the water  backwash, air  scouring is
                               o
provided at a rate of 5 SCFM/ft .  An agitated holding  tank, to receive backwash,
is sized to hold 125 percent of the anticipated backwash  from  one filter.  Even for
low flows, a minimum of two  operating filters and  one spare will  be specified.  For
higher flows (those requiring three or more operating filters) there  will be no design;
spare, but calculation of the required surface area will  be based on  120  percent  of
the average wastewater flow, to facilitate switching from the  operating mode to
the backwash or standby mode without sacrifice of  performance.
     The cost parameters are based on pressurized  downflow dual-media filters.
     Backwash handling could vary for different applications of dual-media filtration.
The backwash water may be recycled to the  head end of the treatment plant, sent
to the sludge-treatment facilities, or handled in  a separate disposal system.  This
Treatment Catalog, however,  specifies a separate backwash holding tank  and then
incorporates the solids handling into the  sludge-treatment train.
                                     28
                                     J-31

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                          FILTRATION, DUAL-MEDIA
FUNCTION:
PARAMETERS
AFFECTED:
EFFECTIVENESS:
APPLICATION
LIMITS:
DESIGN BASIS:
TREATABILITY
FACTOR:
COST PARAMETER:
COST CURVE SCALE
FACTOR:
Removal of suspended solids

TSS
Limits of effectiveness:
     90 percent TSS removal
     75 percent oil removal
     Effluent TSS not less than 5 mg/1
Free oil:   35 mg/1
Influent TSS:   200 mg/1
Hydraulic loading = 8.1  x lo^0'00255)  TSS
Backwash water @ 20 gpm/ft  for 15 minutes per cycle
Backwash air (3 5 SCFM/ft2 for 3 minutes

None
Flow rate
None
                                      29
                                     J-32

-------
RESIDUES:           Filter backwash waste

MAJOR               Filters
EQUIPMENT:            Pressurized downflow dual-medi a f il ters  with
                         5-ft total bed depth,  carbon steel
                      Influent collection sump, concrete
                      Feed pumps (centrifugal  type)
                      Filter effluent holding  tank,  carbon steel  (if
                         requi red)*
                      Backwash pumps (if required)*
                      Air compressors for backwash air
          Large units can utilize filtered forward flow from adjacent
          filter compartments for backwash.
                                      30

                                     J-33

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                             ACTIVATED SLUDGE

     The activated sludge process is used to remove dissolved and colloidal
biodegradable organic material.   Pollution parameters  affected are BOD,  COD,
TOC, TOD, and specific soluble organic materials proven  to be degradable
(e.g., phenol).   Other parameters,  such as ammonia and suspended solids,
are affected by the installation of this process,  but  are not the reason
for its use.
     Activated sludge is available to the sensitivity  model  in only two
forms:  conventional  activated sludge; and extended aeration.   Since chemical
industry wastes tend to require long detention times,  there are two elements
in the breakpoint between the two forms for the model:  12-24 hours detention
time; and 90 percent removal.  The logic here is that  if treatment (at
whatever degree of removal) is accomplished in 12  hours  or less, then
conventional activated sludge is adequately descriptive.  On the other
hand, if 90 percent removal has not been achieved in 24  hours, then extended
aeration is indeed the process in operation.  Between  12 and 24 hours,
conventional activated sludge will  be used with a sliding scale on operational
limits, as  listed in the design data sheet.
     Today, there are many forms of biological treatment, and each has
its own particular features or advantages.  In general,  the alternatives
to activated sludge are used either to lower the cost  from that of activated
sludge for  the same or better performance, or to take  advantage of a particular
feature of the alternative system in order to bring the  effluent of a
problem waste to the quality usually expected from activated sludge.
As an example of the second reason, some wastes will produce a biological
floe that will not settle well, thus the making effluent suspended solids
concentration high.  Certain variations of the activated sludge process
enhance settleability and can be the reason for varying  the process.
                                     31
                                    0-34

-------
     These variations are available to new sources, but generally -are not readily
available to a plant that had installed a treatment plant before such variations were
invented or sufficiently tested.  Therefore, both forms of this process are available
to the model in two modes.  The first is the new-source mode, which involves the
assumption that proper design of pretreatment and  proper selection of the specific
form of the biological treatment process can produce an effluent with "normal  activate
sludge process characteristics" at equivalent activated sludge cost (plus the cost
of appropriate pretreatment).  The second mode is the existing-source mode, which
includes specific allowances for those factors that have an impact  on effluent qualitx
Typical examples are the effects on effluent suspended solids from  influent BOD
concentration and from dissolved solids in the wastewater.
     Biological treatability reaction rate coefficients are determined as accurately
as possible from actual  treatment plant data in the industry.  Where such data are
unavailable, pilot or laboratory-scale data are used.   The values chosen represent
the treatment mode most widely used for the wastes in question.  If pilot or laborator
data are used, K rates are chosen from systems with aeration-basin  detention times
as close as possible to 24 hours.  Only single-stage systems are used.
     Application limits, as shown in the following design data pages, trigger the
need for pretreatment if exceeded.  (The various unit processes used for pretreatment
and the manner of their  application are detailed in other sections  of this catalog).
The suspended solids limitation is intended to protect the activated sludge biomass
from becoming too heavily loaded with non-volatile solids.  The ammonia limitation
is to prevent ammonia toxicity.  The decision as to whether ammonia must be removed
(because of its status as a pollutant) is made elsewhere in the treatment catalog.
                                     32
                                    J-35

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                             ACTIVATED SLUDGE


FUNCTION:           Removal of dissolved organics

PARAMETERS          BOD
AFFECTED:           COD (TOC,  TOD)
                    Phenol
                    Other specific organic materials

EFFECTIVENESS:      Soluble BOD£:  removal up to 99 percent for easily de-
                         gradabie materials and 97  percent for those difficult
                         to degrade.  Conventional  activated sludge (CS)
                         will  be used up to 24 hours detention or 90 percent
                         soluble BOD removal, whichever is greater.  Beyond
                         that  level, extended aeration (EA) will  be used.

                    Effluent BOD5:  Soluble fraction not less than 10 mg/1;
                         suspended solids fraction = 0.3 Ib of BOD,, per Ib
                         of solids leaving final clarification.

                    Phenol Removal:  Although cases will vary, pure phenol
                         removal will be high (99% or greater) in steady-
                         load, acclimated systems,  with removal dropping
                         off as the phenol" analysis reflects substituted
                         phenols and other phenolic compounds.  Regardless
                         of removal rates, bottom level limits will, reflect
                         the influent concentration and expected variability.

                    Oil Removal:  50 percent

                    COD, TOC and TOD removal:  Although cases will vary,
                         in general the removal of these parameters will
                         reflect the biodegradable fraction of each parameter.
                                      33

                                     J-36

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APPLICATION
LIMITS:
pH
Temperature
Oil
TDS
TSS
Heavy Metals:
                                  Pb
                                  Zn
                                  Cr
                                  Cu
                                  Ni
                                  CN
Phenol:

NH,:
 6.0 - 9.1
 50 - 1001
_35 mg/1
_10,000 mg/1
_(25
    mg/1
    mg/1
    mg/1
    mg/1
    mg/1
    mg/1
  0 mg/1
300 mg/1
'100 mg/1
(500 + 0.
                                                   .05 MLVSS)
                                                (steady load)
                                                (fluctuating load)
                                                05 BODK)
                                                           Revised 8/4/80
                                     34

                                     0-37

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                       ACTIVATED SLUDGE  (Continued)
DESIGN BASIS:
TREATABILITY
FACTOR:

TEMPERATURE LOSS
RATE:
COST PARAMETERS:

COST CURVE SCALE
FACTOR:

RESIDUES:
MAJOR
EQUIPMENT:
vs<
where
                          K   =
   = effluent BOD concentration  (dissolved), mg/1
   = influent BOD concentration  (dissolved), mg/1
 T = reaction rate coefficient at  operating temp.
 T       (°C),  day -1
X  = mixed liquor volatile  suspended  solids, mg/1
t  = aeration time,  day
                    F/M=   v|
       So
       Xt
                             .05
                             .20
             to 0.
             to 0,
              day"]
              day"
                            0.05  to 0.2 day"
overall  range
range for a conventional
   system
range for extended aeration
                    X  =  4,000 mg/1
   = K
      20°C
     (1.06)
                                    T-20
     where T = temperature (  C)
A model that includes heat gains  from the  influent
wastewater flow, mechanical  action,  and from  biological
and chemical reactions,  plus  solar  radiation  and
losses including evaporation  from the liquid  surface
and the sidewalls.
Flow rate
Aeration time

Excess activated sludge
  Ib dry solids produced (net)/lb BOD removed =
     up to 24 hours detention:  0.3 Ib/lb
     24 hours detention: 0.3-(t-24)(0.003)  Ib/lb
  solids 80 percent volatile

Aeration basins
  Two (2) basins, each with capacity for 50 percent  of
                                     35

                                     J-38

-------
     design wastewater flow;  common influent splitter box,
  Construction:
      550,000 gallons - all concrete
     _550,000 gallons - earthen basin with
     membrane liner; concrete abrasion pads under
     aerators (see AERATION)

Aerators - See AERATION
Clarifiers - See CLARIFICATION
                                        Revised 8/4/80
                36

               J-39

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      ACTIVATED SLUDGE  (Continued)


Sludge recycle pumps:  Three centrifugal pumps (including
   spare), each with capacity to pump 33.3 percent of
   the design wastewater flow at 1 percent solids con-
   centration.
Monitoring and control devices
   Sludge-wasting control
   Sludge-recycle control
   DO monitor, temperature monitor
   pH monitor and control system
Nutrient storage and feed - See NUTRIENTS
Defoamer storage and feed
                    37

                   J-40

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                                                            Revised 8/4/80
                      AERATION, BIOLOGICAL PROCESSES

     Aeration is required in a biological  unit process  to supply the  dissolved
oxygen needed for sustaining biological growth reactions, and to provide
mixing to keep the bio-mass suspended in the system.   The biological  processes
requiring aeration are activated sludge, nitrification,  and aerobic digestion.
Aeration requirements and the equipment for activated sludge and nitrifica-
tion are covered in this section,  while the aeration  facilities for aerobic
digesters are covered under AEROBIC DIGESTION.
     The design basis is the power required either to supply oxygen or
to accomplish mixing, whichever is greater.  The oxygen  requirement for
activated sludge is based on the Ib 0~/lb  BODr removed.   For nitrification,
a requirement for nitrogen oxygen demand is added to  the oxygen required
for BOD removal.  The mixing requirement is determined on the basis of
horsepower per 1000 gallons of wastewater  under aeration.
     The cost parameters for these aeration systems are  based on platform-
mounted surface turbine aerators.   See the attached design data sheet
for a more detailed description of the design basis.
                                     38
                                     J-41

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                      AERATION, BIOLOGICAL PROCESSES
FUNCTION:

PARAMETERS
AFFECTED:
EFFECTIVENESS:

APPLICATION
LIMITS:
DESIGN BASIS:
Supply dissolved oxygen and mixing for activated
sludge and nitrification processes.

Dissolved oxygen (DO)
Will maintain at least 2.0 mg/1 DO in aeration basin
at 30 C (summer conditions).

lOOmg 02/1 per hour
Power Supplied = Power Required plus one extra aerator
horsepower equivalent.
Activated Sludge
Power Required (at 85% motor and gear efficiency)
               NT
P  = 	,	 '	
 r   3.0 Ib 02/hr/horsepower
     subject to a minimum of 0.1 HP/1,000 gallons
     (under aeration).
Required Oxygen Transfer (Ib/hr) at Standard Conditions
                               N.
                                   N
        CssP - CL
                                       (1.025)
                                              1-20    °'4756
                        = 0.7
                        = 0.9
                    Css = 7.63 mg/1 @ 30°C
                    C$  = 9.17 mg/1 9 20°C
                    CL  = 2.0 mg/1
                    P   - Barometric pressure at plant  site _  -,
                          Barometric pressure at sea level
                    T   = 30°C
                    Oxygen Utilization Rate (Ib/hr)
                                    39
                                    J-42

-------
N  = a' (Ib BOD removed/hr) + b1
        (Ib MLVSS under aeration)
a1 = 0.7 Ib 02/lb BOD removed
b1 = see grapn (on following page)
                40

               J-43

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TREATABILITY
FACTOR:

COST
PARAMETER:
COST CURVE SCALE
FACTOR:

RESIDUES:
MAJOR
EQUIPMENT:
Nitrification

Oxygen Utilization Rate (Ib/hr)
N =a'(lb BOD removed/hr)  + b'(lb MLVSS  under  aeration)
   + 4.6 (Ib NH3 -N + Organic-N  applied/hr)
Power Required is then computed  as for  activated sludge.


None

Installed horsepower per  aerator


Number of aerators

None
Surface turbine-type aerators, mounting platforms,
walkways, and concrete abrasion  pads.
                                      41
                                     J-44

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                      NITTRIENTS,  BIOLOGICAL PROCESSES

     A nutrient addition system is required for a biological  unit process so that
sufficient nitrogen and phosphorus will  be present in the wastewater to insure that
neither nutrient becomes the limiting factor in the biological  growth reactions.
In some cases, a sufficient amount of either one or both nutrients may already be
present in the wastewater,  which  reduces or eliminates the need for a nutrient supply
system.  This is determined on a  case-by-case basis.  Capital  costs are based on  stora
and feeding facilities for  phosphoric acid and/or anhydrous ammonia.
                                      42
                                     J-45

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                      NUTRIENTS,  BIOLOGICAL PROCESSES
FUNCTION:
PARAMETERS
AFFECTED:

EFFECTIVENESS:
APPLICATION
LIMITS:


DESIGN RATES:
TREATABILITY
FACTOR:

COST
PARAMETER:

COST CURVE SCALE
FACTOR:

RESIDUES:

MAJOR
EQUIPMENT:
Supply nutrients to biological processes, such as
activated sludge, if not already present in wastewater
in required amounts.


None
Supply enough nitrogen (N)  and phosphorus (P) to maintain
biological unit processes.

Only enough nitrogen and phosphorus added to maintain a
small residual of nitrogen  and phosphorus in effluent
from biological unit process.

BOD:N:P ratio = 100:5:1
     using 75 percent phosphoric acid (H3PO.) and
     anhydrous ammonia (NH,)


None

Nitrogen deficiency
Phosphate deficiency


None

None
Ammonia storage tank (carbon  steel), with ammonia
     feed system, including water bath, irrmersion
     heater, evaporator, and  ejector - if usage is
     over 2 tons/week.
Ammonia cylinders and ejector - if usage is equal to
     or less than 2 tons/week.
Phosphoric acid storage tank, - fiber-reinforced plastic,
     (if usage is over 200 Ibs/day)
Phosphoric acid, feed pumps  (metering type).
                                      A3

                                     J-46

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                         NITRIFICATION, BIOLOGICAL

     The biological  nitrification unit process is used for ammonia removal,  when
required, following an activated sludge system with a detention time of less than
24 hours.  Because activated sludge systems with detention times  greater than 24
hours (extended aeration) operate at an F:M of 0.2 or lower,  it is assumed that nitrif-
takes place concurrently with carbonaceous BOD removal, and does  not always  require
an additional step.   In almost all cases,  the nitrification unit  process follows  an act
sludge process.  However, if the discharge from some other type of treatment unit
process has an easily biodegradable waste with a BODg of less than 125  mg/1  and
a BOD5/TKN ratio of less than 3.0, then the nitrification unit process  can be considere
for direct use.  The pollution parameters affected by this unit process are ammonia
nitrogen (NH3-N), organic nitrogen (TKN),  BOD, COD, and TOC.   Ammonia compounds
are converted biologically, first to nitrites (NOp) and then  to nitrates (NO^).  Nitrog
in these forms can be converted to nitrogen gas (N?) by anaerobic denitrification
(See DENITRIFICATION, BIOLOGICAL).
     The design parameters are based on Ib NH--N and Ib TKN removed per Ib MLVSS
per day, with a correction factor for temperature.  The cost  parameter  is  based
on flow, with a cost-curve scale factor for aeration time.
     Application limits, as shown in the specification pages, will either  trigger the
need for pretreatment or rule out this unit process for ammonia removal.
                                       44
                                      J-47

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                         NITRIFICATION,  BIOLOGICAL
FUNCTION:

PARAMETERS
AFFECTED:
EFFECTIVENESS:


APPLICATION
LIMITS:
DESIGN BASIS:
TREATABILITY
FACTOR:
Conversion of NH3-N and Organic-N  to  N02-N  and  N03-N
NFL-N
Organic-N (TKN)
BOD,
                    TOC
NH^-N + Organic-N removal  to  2  mg/1
Soluble BOD, removal to  5 mg/1
pH
Temperature
BOD,
BOD^/TKN
TDS5

Total Nitrogen
7.5-9.0
 50-100°F
125 mg/1
3.0
10,000 mg/1
 2,000 mg/1
Basin configuration = complete mix
Nitrification rate  = 0.3 Ib NH--N +  TKN
          removed/Ib MLVSS/day I 30°C and  pH  8.5
MLVSS = 2000 mg/1
                    HT =
                         VN
                         qN
                    where:
                         HT = hydraulic detention time (days)
                         N   = influent NH.-N  +  Organic-N  (mg/1)
                         N° = effluent NH^-N  +  Organic^  (mg/1)
                         qw = nitrification rate (day  "  )
                         Xlj1 = MLVSS (mg/1)
                    Aeration Tank D.O.   2.0  mg/1
Temperature correction
                                      45

                                     J-48

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                  NITRIFICATION, BIOLOGICAL  (Continued)


COST PARAMETERS:    Basin volume
COST CURVE SCALE
FACTOR:             Aeration time
RESIDUES:           Excess sludge:
                      Ib dry solids produced/lb NH--N + Organic-N  removed =  0.5
                      Ib dry solids produced/lb BOD,, removed =  0.3

MAJOR               Aeration basin:
EQUIPMENT:               Two provided, each @ 50 percent capacity, with
                         one 10'-deep influent  splitter box
                      Construction:
                           550,000  gal. - all concrete
                          _550,000  gal. - earthen basin with membrane liner

                          (The number of baffles is estimated on the
                          basis of  complete mixing.)
                    Aerators:   See  AERATION, BIOLOGICAL PROCESSES
                    Clarifiers:  See CLARIFICATION
                    Sludge recycle  pumps:
                         Three centrifugal pumps (including spare) each
                         @ 33.3 percent of plant design flow
                    Monitoring and  control devices
                         Sludge wasting control
                         Sludge recycle control
                         DO monitor
                         pH monitor and control system
                         Defoamer storage and feed
                         Temperature monitor
                                     46

                                     J-49

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                        DEN ITR IF I CATION,  BIOLOGICAL

     The anaerobic denitrification unit process  is  used for  the conversion
of nitrates and nitrites to  free  nitrogen,  following  a nitrification  unit
process or an extended-aeration unit process.  The  pollution parameters
affected are nitrates (N03)  and nitrites  (NO-).
     The design parameters are  based on Ib  NO.-N  +  NOp-N per Ib MLVSS
per day, with a correction factor for temperature.  The cost parameters
are based on flow, with cost-curve scale  factors  for  reaction time.
     Effluents from nitrifying  units are  exceptionally free  of BOD.   For
this reason, denitrification is a very slow process  unless  a readily  oxi-
dizable source of carbonaceous  material is  added.  For the purpose of
design, methanol is used as  the source of carbon  because it  is more completely
oxidized and produces less sludge for disposal,  and  is more  cost effective
than other source of carbon.  The effluent  from  the  denitrification unit
is flash-aerated prior to clarification,  to oxidize the excess methanol
and to strip entrapped nitrogen gas from  the sludge  in order to improve
its settling characteristics.
     See attached specification pages for a more  detailed description
of the design basis.
                                    47
                                   J-50

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                    DENITRIFI CATION, BIOLOGICAL
FUNCTION:

PARAMETERS
AFFECTED:

EFFECTIVENESS:
APPLICATION
LIMITS:
DESIGN BASIS:
TREATABILITY
FACTOR:

COST PARAMETER:

COST CURVE SCALE
FACTOR:
Conversion of NO..-N and NO^-N to free nitrogen
NO--N
NO^-N

NO--N removal to
NO^-N removal to
pH
Temperature
NO,-N + N09-N
TDS       i
                    1.0 mg/1
                    1.0 mg/1

                    6.0 - 8.0
                     10 - 38°C (50 - 100°F)
                     500 mg/1
                     10,000 mg/1

Basin configuration - complete mix
Denitrification rate - 0.16 Ib NO, + NO?-N  removed/lb
     MLVSS/day @ 30° and pH 7.0  J     *
Dissolved Oxygen   0.1 mg/1
MLVSS = 2000 mg/1
     D_-D.
                 HT = hydraulic detention time (days)
                    HT =

                         9DxX1
                                      D  = influent NO,  + N00-N
                                       o              32
                  D] = effluent N03 + N02-N (mg/1)

                  gp = denitrification rate (day" 1\

                  X1 = MLVSS (mg/1)

Methanol requirements = 4 Ibs methanol/lb NO,-N + N09-N
                                            O       L-

Temperature correction

Flow rate


Reaction time
                                      48

                                      J-51

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                 DENITRIFICATION, BIOLOGICAL  (Continued)
RESIDUES:


MAJOR
EQUIPMENT:
Excess sludge
     Ibs dry solids produced/lb NO.+NOp-N removed = 0.7

Reaction Basins (uncovered):   Two provided,  each @ 50 percent
     of capacity,  with concrete influent splitter box.
Construction:
     550,000 - all concrete
    _550,000 - earthen basin with membrane liner;
               concrete mixer-abrasion pads
Mixers:  0.5 HP/1000 cu ft (0.067 HP/1000 gal)
Clarifiers:  See CLARIFICATION
Sludge Recycle Pumps:
     Three centrifugal pumps (including spare) each
     @ 33.3 percent of plant design flow.
Monitoring and Control Devices:
     Sludge wasting control
     Sludge recycle control
     pH monitoring and control system
     Temperature monitor
Methanol Feed System:
     Methanol storage tank (if usage is over 350 Ib
          per day), carbon steel surrounded  by a
          concrete dike
     Methanol feed pumps (metering type)
Aerated Stabilization Chamber, concrete:
     Detention time (0.5 hr)
     Aerators:  (0.1 HP/1000 gallons)
Acid storage tank  (carbon steel) and feed pumps
                                       49

                                      J-52

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                                 OZONATION

     The ozonation treatment process is used for the removal  of cyanide
and/or phenol, but only on individual process-unit streams or in plants
with low wastewater flow.
     The two principal features of the design basis for the ozonation
process are:  7 Ib 0.,/lb cyanide and/or phenol for the ozone-generating
equipment;  and 30 minutes retention time for the contactor chambers.
     The concentration of ozone (03) is 1.0-2.0 percent (by weight),  or
about 20 grams/cubic meter.   Efficiency of usage is assumed to be 70  percent.
     Waste air/ozone from the contactors will be returned to the compressor
section, with 33 percent discharged to the atmosphere as a purge stream.
     Equipment considerations limit the capacity of the ozonation unit
to 2.0 MGD.  PI ate-type ozonators are used.
                                     50
                                   J-53

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                                 OZONATION
FUNCTION:

PARAMETERS
AFFECTED:
EFFECTIVENESS:


APPLICATION
LIMITS:

DESIGN BASIS:
TREATABILITY
FACTOR:
Removal of cyanide and phenol

Cyan i de
Phenol
Other organics

Cyanide removal - to less than or equal to 1 mg/1
Phenol removal - total


None

Ozone dosage = 7 lb,0, per lb (CN + phenol),
     20 6M 03/meterJ J
Contact time - 30 minutes
None
COST PARAMETER:     Ozone usage rate (Ib/day) and Flow
COST CURVE SCALE
FACTOR:

RESIDUES:

MAJOR
EQUIPMENT:
Concentration of pollutants

None

Ozone generator (air-fed) with compressor, cooler,
     water knockout drum, and dryer.
Closed contact chamber (2-Stage), with venting system
                                      51

                                     J-54

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                            CHEMICAL OXIDATION

     Chemical oxidation is used in removal  of cyanide and other organic
and inorganic materials.   This unit process is needed when the pollutant
involved is not amenable to other types of  treatment, for either technological
or economic reasons.  Cyanide removal  by alkaline chlorination is used
on individual-process waste streams when the cyanide concentration is
too high for effective removal in a biological treatment system.  To minimize
the risk of formation of chlorinated organics, chlorine is used only when
no feasible alternative is available.
     Other available chemical  oxidants include permanganates and hydrogen
peroxide, which can be used as required for removal  of specific organic
and inorganic pollutants.   However, for the purposes of preparing the
cost estimate for this unit process, it was assumed  that chlorine would
be used.  Oxidation by ozone,  which would be generated on-site, performs
the same function as oxidation by purchased oxidants, but the costs  generally
are more capital-intensive.  (Ozonation is  included  in this Treatment
Catalog as a separate unit process).
     The choice among the various types of  oxidation systems is essentially
an economics decision.
                                      52
                                     J-55

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                            CHEMICAL OXIDATION
FUNCTION:


PARAMETERS
AFFECTED:

EFFECTIVENESS:


APPLICATION
LIMITS:

DESIGN BASIS:
TREATABILITY
FACTOR:

COST PARAMETER:

RESIDUES:

MAJOR
EQUIPMENT:
Removal of cyanide and/or other organic and inorganic
materi al s.
Specific organic or inorganic pollutants.

Specific for each oxidant/pollutant combination.
Total cyanide destruction by chlorine.


TSS 50 mg/1 maximum

Contact time
     First stage         10 minutes
     Second stage        30 minutes
Chemical requirements (CN destruction)
     15 parts chlorine per part CN~
     17 parts NaOH* per part CN"
     pH  8-9.5


None

Basin volume

Oxidized impurities that form TSS

Two-stage, concrete reaction vessel
pH control system
ORP control system
Oxidation-chemical feed system (for chlorine: chlorine
     vaporizer, chlorinator, and circulation pumps).
          A chemically equivalent amount of lime can be substituted for
          the 17 parts NaOH.
                                     53

                                     J-56

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                        ACTIVATED CARBON ADSORPTION

     The activated carbon process is used to remove dissolved organic
material.  Pollution parameters affected are COD,  TOC,  TOD,  and specific
soluble organic material adsorbable by carbon.  In most cases,  activated
carbon is used as an individual-stream pretreatment process;  however,
in other cases, activated carbon treatment is used as a final treatment
process following biological treatment.
     Activated carbon adsorption rate coefficients are determined as accu-
rately as possible from actual treatment plant data in industry when available.
Where such data are unavailable, pilot or laboratory-scale data are used.
Values chosen represent the adsorption rate most typical of  the wastes
in question for a variety of types of carbon.  No attempt is made to opti-
mize a particular brand of carbon to the particular wastes in question.
     The time required to reach the "breakthrough point" is  one of the
most important design factors in fixed-bed adsorption processes.   The
approach taken to model the activated carbon adsorption process was to
apply a method for predicting breakthrough times to yield:  size, perfor-
mance, cost, and operation data for the required carbon system.
     Non-equilibrium fixed-bed column dynamics is suggested  as  the most
applicable adsorption method for controlling water pollutants.   Non-equi-
librium theories take into account the nature of driving forces which
control the transport phenomena of solutes from solution.  Equilibrium
theories assume the resistance to mass transfer to be negligible.
     Three models were presented which deal  with the theoretical  treatment
of non-equilibrium column dynamics:   1) pore diffusion; 2) homogeneous
solid diffusion; and 3) kinetic reaction (or bilinear adsorption).  All
three models are based on the fundamental concept of a material balance
for the adsorbate in the liquid phase and on the solid adsorbent.' '
     The model selected for analysis was the lumped parameter model (also
                                    54
                                   J-57

-------
called the Glueckauf Model).   This model  combines  the diffusional  -resistances
described by the pore diffusion model  and homogeneous solid diffusion
model into a single parameter.
     The approach taken to model the activated carbon adsorption process
was the application of a method for predicting the breakthrough time of
a pollutant from the known breakthrough time of a  similar pollutant/ '
A breakthrough curve for benzene was selected as the reference case from
which all other breaktrough times were predicted for those pollutants
treatable by carbon.
     Various pretreatment unit processes, such as  filtration or clarification
for suspended solids removal, frequently are required prior to the use
of activated carbon.  These processes  are not included here, but they
are detailed in other sections of this catalogue.
     On-site carbon regeneration is considered only when carbon usage
exceeds 1,000 Ib carbon/day (see ACTIVATED CARBON  REGENERATION).  When
carbon usage is below 1,000 Ib/day, disposal is by landfill or outside
contract regeneration.

                        ACTIVATED CARBON ADSORPTION
FUNCTION:
PARAMETERS
AFFECTED:
EFFECTIVENESS:
APPLICATION
LIMITS:
DESIGN BASIS:
Removal of dissolved organics.

COD, TOC, specific organic materials.
Removal of pollutant is subject to the adsorption
limits for the compounds present.
Suspended solids:   25 mg/1
Free oil:          10 mg/1
Langmuir adsorption isotherm theory for multicomponent
     mixtures.  Design is based on the breakthrough time
     of the critical pollutant.  The reference case is the
     breaktrough curve for benzene.
Backwash @ 20 gpm/ft  for 15 minutes/cycle.
On-site carbon regeneration only for plant using more
     than 1,000 Ib carbon/day.   See ACTIVATED CARBON
                                    55
                                   J-58

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                         REGENERATION.
TREATABILITY        Isotherm constants
FACTOR:                  Q = Langmuir constant  related  to slope
                         B = Langmuir constant  related  to intercept  and  slope
                    Final attainable value
COST PARAMETER:     Total bed volume
COST CURVE SCALE
FACTOR:             None
RESIDUES:           Spent carbon
                         If  1,000 Ib/day, see  ACTIVATED  CARBON REGENERATION.
                         If  1,000 Ib/day, disposal  by  landfill or contract
                         hauler.
                    Backwash effluent.
                    Drainage and transport water.
                                      56

                                     J-59

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                 ACTIVATED CARBON ADSORPTION  (Continued)


MAJOR               Moderate-Flow Unit  (  0.4 MGD)
EQUIPMENT:               Adsorbers
                         Fixed-bed,  pressurized, downflow contactors;
                         minimum  of  two in  series, plus  a spare  (all  lined
                         carbon  steel).
                         Minimum  depth:   Diameter  ratio  =  1:1
                    Regenerated-carbon  storage  tank,  lined carbon  steel
                    Spent-carbon  holding  tank,  rubber-lined carbon steel
                    Effluent  holding tank,  carbon  steel
                    Backwash  pumps
                    Backwash  storage tank,  carbon  steel,  (with agitator)
                    Backwash  return  pumps
                    Spent-carbon  slurry pumps
                    Surface-spray pumps
                    If on-site carbon regeneration is involved
                    (1,000  Ib/day carbon),  see  ACTIVATED CARBON
                    REGENERATION.
                    High-Flow Unit ( 0.4  MGD)
                    Feed pumps
                    Adsorbers, lined carbon steel
                         Pulsed-bed, fluidized,  upflow contactors;  minimum
                         of two contactors, plus a spare.
                         Minimum depth:  Diameter  ratio  = 1:1.
                    Regenerated-carbon  storage  tank
                    Spent-carbon storage  tank
                    Spent-carbon slurry pumps
                    Regenerated-carbon  loading  pumps
                                     57

                                    J-60

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                       ACTIVATED CARBON REGENERATION

     The activated carbon regeneration process is used only when the carbon usage
exceeds 1,000 Ib/day.   The parameter affected is the adsorption capacity of the carbon
and there is a 10 percent carbon loss per cycle during regeneration.  The carbon is
regenerated on a column-by-column basis when the effluent quality reaches the limiting
effluent requirement.
     The design parameters are based on a mul tipie-hearth furnace with a carbon
loading of 40 lb/day/square foot, plus 20 percent for down time.  The cost parameters
are based on the effective hearth area required.
     Activated carbon  regeneration by multiple-hearth furnace is the only regeneration
process used in the model.  Other regeneration processes  (such as solvent washing
and acid or caustic washing)  were investigated, but were  considered less desirable.
See the attached design data page for a more detailed description of the design basis.
                                      58
                                     J-61

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                       ACTIVATED CARBON  REGENERATION
FUNCTION:


PARAMETERS
AFFECTED:

EFFECTIVENESS:

APPLICATION
LIMITS:

DESIGN BASIS:
TREATABILITY
FACTOR:

COST PARAMETER:

COST CURVE SCALE
FACTOR:
RESIDUES:

MAJOR
EQUIPMENT:
                                                                         area
Remove and thermally oxidize adsorbed organics from
spent activated carbon,  for reuse of the carbon.

Restoration of carbon adsorption capacity
Complete combustion of off-gases

None
Multiple-hearth furnace with afterburner on top hearth
Carbon loading:  40 Ib/day per ft  of hearth surface a
Temperature:  1700°F to 1800?°F
Surface area required:  design plus 20 percent for down time
Regeneration fuel:   8,000 Btu/lb of carbon
Carbon loss:  10 percent per cycle

None
Total hearth area

(No. of Furnaces)0'8
Clean off-gas and ash, representing the carbon losses
Regeneration furnace  (multiple-hearth) w/stacks and
     afterburner
Quench chamber
Venturi scrubber
Separator
Venturi recirculation tank and pumps
Caustic storage and feed system, carbon steel
Combustion  and shaft  cooling air blowers
Fuel-oil storage and feed system, carbon steel
Carbon transfer pumps
Feed slurry tank
Dewatering  screw conveyor
Asphalt slab, surrounded by a concrete wall, for storage
     of a 14-day supply of carbon during furnace downtime.
                                    59

                                    J-62

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                                ION  EXCHANGE

     The ion exchange process is used to remove dissolved contaminants
that are not amenable to other forms of treatment.  Pollution parameters
affected are cyanide, ammonia, and specific soluble heavy metals.  In
almost every case, ion exchange is used as a pretreatment process on a
single product/ process waste stream.
     The design parameters are based on the ion exchange resin capacity
(Ib/cubic foot of resin) for cyanide, ammonia, and specific metals.   The
values chosen represent the resin capacity most typical of the wastes
in question for the type of resin being used.  No attempt is made to optimize
a particular brand of resin to the particular waste in question;  thus,
values are chosen of a variety of types of resin.  Other design parameters
include hydraulic loading and regeneration rates.  The cost parameters
are based on the working-bed volume required to achieve the desired effluent
quality.
     Various pretreatment unit processes are required preliminaries  to
the use of ion exchange, e.g., filtration or clarification for suspended
solids removal.  These processes are not included here, but they are detailed
in other sections of this catalogue.
     Ion exchange resins are regenerated, by rinsing with clean water
and concentrated brine solutions, after the bed capacity is exhausted.
The type of treatment system to be used on the regeneration wastes depends
on the particular contaminants removed by the ion exchange.
     See the attached design data page for a more detailed description
of the design basis for ion exchange.
                                     60
                                     J-63

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                               ION EXCHANGE
FUNCTION:           Removal  of  dissolved  contaminants

PARAMETERS          Cyanide
AFFECTED:           Ammonia
                    Metals
                    Total  Dissolved  Solids  (TDS)

EFFECTIVENESS:      Removal  subject  to  ion-exchange rates for
                    compounds present

APPLICATION         Suspended solids -  25 mg/1
LIMITS:             Oil  -  10 mg/1

DESIGN BASIS:       Hydraulic 1oading:
                         1.5 gpm/f±J
                         10  gpm/fr
                         (12 bed volumes/hr)
                    Regeneration rate:             ,
                         6 bed  volumes  @  0.5  gpm/ft    (4 bed volumes/hr)
                    Ion exchange capacity:
                         2 Ib cyanide/cubic ft  of  resin
                         1 Ib ammonia/cubic ft  of  resin
                         4 Ib Zn,  Ni, Cu/cubic  ft  of  resin
                         3 Ib Cr/cubic  ft of  resin
                                     61

                                     J-64

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TREATABILITY
FACTOR:             None

COST PARAMETERS:    Working bed volume and  flow
COST CURVE:         Number of beds

RESIDUES:           Spent regenerant
                         Cyanide -  15% NaCl solution  (precipitation with FeClJ
                         Ammonia -  15% NaCl,CaCl9, CaO mixed solution
                                   (see AMMONIA STRIPPING)
                         Zn,Ni,Co - 5% H?SO.  solution  (precipitation with lime)
                         Cr       -  10% NaOR  solution  (chromic acid recovery)
                    Backwash effluent

MAJOR               Exchangers, Fiber-Reinforced Plastic  (FRP)
EQUIPMENT:               Fixed-bed  pressurized  downflow contactors,
                              minimum  of two  in series.
                         Minimum depth/diameter ratio = 1:1
                    Regenerant make-up tank,  FRP
                    Spent regenerant collection and treatment tanks, FRP
                    Ion-exchange resin
                    Regeneration and sludge pumps
                    Regenerant treatment and  make-up tank agitators
                                     62

                                     J-65

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                   SLUDGE/RESIDUE HANDLING AND DISPOSAL
                                  GENERAL

     Aerobic digestion, gravity thickening,  vacuum filtration,  pressure
filtration, landfill, and incineration are the Treatment Catalog unit
processes for handling and disposal  of sludges and other residues generated
by biological and physical-chemical  unit processes.   A specific sludge/residue
may require only one of these specific unit  processes, or it may require
treatment by a sequence of several unit processes.
     Aerobic digestion is used to stabilize  waste activated sludges,  gravity
thickening to concentrate chemical and biological sludges,  and  vacuum
or pressure filtration for the dewatering of chemical  and biological  sludges.
Ultimate disposal of sludges is either by landfill alone or by  incineration
followed by landfill.  Federal  and state regulations,  land  availability,
sludge type, and other factors affect the decision on whether to landfill
directly or to incinerate a processed sludge.   Therefore, the option  to
examine both landfill and incineration of a sludge/residue  is available
for most of the treatment trains that will be encountered.
     For each particular sludge or sludge combination from  a biological
or physical-chemical unit process, there is  an assigned treatment train(s)
for processing that sludge/residue.   The treatment trains to be used  on
all sludges/residues are summarized on the attached table,  which presents
the sludge/residue type on the left and the  treatment train options on
the right side for that particular sludge/residue.  When the quantity
of a sludge/residue is small, the treatment  train concept is not used,
for economic reasons; instead, a private contractor is utilized to handle
the sludge/residue.
     In this sludge-handling section of the Treatment Catalog,  the unit
pro-cesses used in the sludge/residue treatment trains are  examined on
an individual basis. For each of the six sludge unit processes  mentioned,
                                      63
                                      0-66

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there is a narrative and a design data sheet(s) detailing its  applicability,
operation, design basis, association with other sludge unit processes,
and other information necessary to model  the unit process under  consideration
      i. T
accurately.
                                      64
                                      J-67

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                            TABLE 1.  SLUDGE TREATMENT SUMMARY
Disposal
Sludge/Residue Options*
Process Primary Sludge
(Primary Clarifier)
Incinerator Scrubber Sludge
Oil/Oily Solids
Floatable Chemical Solids
Waste Activated Sludge (WAS)
Chemical Sludges from Floc-
cul ation/Clarif ication and
Neutralization
Chemical plus Biological
Sludge (WAS)**
Process Primary Sludge
plus (WAS)
Extraction/Distillation
Resi dues
Inci nerator Ash
Non-Organic Filter
Backwash from Tertiary
Sand F il ter
Throw- away Activated
Carbon
L
I
O.C
L
I
O.C
L
I
O.C
L
I
O.C
L
I
O.C
L
I
O.C
L
I
O.C
L
I
O.C
L
I
O.C
L
I
O.C
L
I
O.C
L
I
O.C
Aerobic
Digestion Vacuum/
Pressure
Gravity (Bio-Sludge Filtra- Incinera- Land-
Thickening Only) tion tion fill
X XX
Option Not Avail able
Option Avail able
Option Not Avail able
X
Option Available
X X
X X
Option Available
XXX X
X XX
Option Available
X XX
Option Not Available
Ojjti on Avail able
XXX X
X XXX
Option Available
XXX X
X XX
Opti on Avail able
Opti on Not Avail able
X
Option Avai Table
X
Option Not Available
Opti on Avail able
X XX
Option Not Avail able
Opti on Avail able
XXX X
X XX
Option Avail able
X
Option Not Avail able
Option Avail able
* L = Landfills;  I = Incineration;  O.C. = Outside Contractor.

** For the Incineration option,  biological  and chemical  sludges  are thickened separately;
   the chemical sludge is landfilled,  and the bio-sludge is  incinerated.   For the Land-
   fill option, the two types of sludge are thickened separately,  the bio-sludge is
   digested, and then the sludges are combined in a conditioning unit before dewatering.
                                          65

                                          J-68

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                            GRAVITY THICKENING

     Gravity thickening is used to concentrate waste activated sludge,  chemical
sludges, primary sludges,  and certain combinations of these types  of  sludge.   Concentr
of these sludge solids in a gravity thickener results in cost savings in subsequent
sludge dewatering.
     The gravity thickener used in the model  is a mechanical  type  with  a picket
sludge-collection device used to promote thickening.   Thickened sludge  that  collects
on the bottom of the thickener is pumped to a dewatering device as required.   For
biological  sludge thickeners,  recycled final  effluent water is available to  suppress
odors associated with septic conditions.  The continuous supernatant  flow from sludge
thickening is pumped to the head end of the treatment plant.
     Determination of the thickener surface area, which dictates associated  costs,
                                           o
is based on solids surface loading in Ib/ft /day.  Typical  solids  loadings vary  depend
on the type of sludge being thickened, as indicated on the  attached design data  sheet.
For sludge combinations, a weighted average approach is used  to define  the solids
loading to the thickener.   Underflow solids concentration at  the thickener depends
on the type of sludge being concentrated, as  well as on the solids loading.   For sludg
combinations, a weighted average technique is used to determine thickener underflow
concen-trations.  For more details on the thickener,  see the  attached design  data
sheet.
                                      66
                                      0-69

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                            GRAVITY THICKENING
FUNCTION:

PARAMETER
AFFECTED:

EFFECTIVENESS/
DESIGN BASIS:
APPLICATION
LIMITS:

TREATABILITY
FACTOR:

COST PARAMETER:

COST CURVE SCALE
FACTOR:

RESIDUES:
MAJOR
EQUIPMENT:
Increase the solids concentration

Concentration of suspended solids
Solids, underflow concentration:
                    Type of Sludge
                    Primary
                    Waste Activated
                    Lime
                    Alum
                    Iron
                    Combined
                    Overflow quality:
                   Solids  Loading
                    (lb/ft/z/day)

                         20
                          5
                         40
                         24
                         15
                            Weighted Average
                   500 ppm TSS
                                                           Underflow Cone.
  9
2.5
 15
  3
  6
None

None

Surface area


None
Scum
Thickened sludge at various solids concentrations,
     depending on the type of sludge.
Supernatant liquor - 500 mg/1 suspended solids

Thickener tank, carbon steel: 15-ft liquid depth
     Thickener mechanism with skimmer  (center feed,
     peripheral overflow), carbon steel
Underflow sludge pumps (positive-displacement type)
                                    67

                                   J-70

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                             AEROBIC DIGESTION

     Aerobic digestion is used to reduce the volatile suspended solids
(VSS) content of a waste activated sludge (WAS) if the sludge is to be
dewatered and hauled directly to a landfill  for final disposition.   When
the WAS is to be incinerated, aerobic digestion is not used,  because a
digested sludge has a lowered percentage of  VSS,  making it less efficient
as an incinerator fuel.  Aerobic digestion is preceded by gravity thickeners
in all sludge-handling systems.
     The aerobic digester utilized in the model has a basin similar to
that of an activated sludge system.   The digester basin is 12 feet  deep
with a three-foot freeboard.  Basin size determines the materials of construction
and also the number of aerators required for proper digestion of the activated
sludge.  Aerobic digester basins are not covered or heated.
     Digested sludge from this unit process  is pumped to a dewatering
unit.  The dewatering unit is not normally operated continuously (24 hr/day),
but the feed rate to the digester is relatively constant.  Therefore,
the water level will vary somewhat,  and fixed-mounted surface aerators
cannot be used.  Floating, low-speed, surface-turbine aerators are provided.
     Waste activated sludge going to the digester has a solids concentration
of 2.5 percent, of which 80 percent is volatile.   In the digester,  the
volatile material in the sludge will be reduced by 4 percent  per day at
20°C, to a maximum reduction of 70 percent.   A temperature correction
factor is included on the specification sheet for operating temperatures
different from the normal of 20°C.   For further information on the  aerobic
digester, refer to the attached design data  sheet.
                                     68
                                    0-71

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                             AEROBIC DIGESTION
FUNCTION:
PARAMETER
AFFECTED:

EFFECTIVENESS:
APPLICATION
LIMITS:

DESIGN BASIS:
TREATABILITY
FACTOR:
COST PARAMETER:

COST CURVE SCALE
FACTOR:

RESIDUES:

MAJOR
EQUIPMENT:
Reduction of volatile suspended solids (VSS)  in waste
     activated sludge (WAS).
Stabilization of WAS.
VSS

VSS Reduction = 4 percent/day @ 20°C,  to a maximum
     of 70 percent

pH of basin: 6.0-9.0
Basin temperature: 55-100 F

VSS/TSS = 0.8
Influent solids concentration =2.5 percent
Hydraulic retention time = 15 days under normal  conditions.
     Can be varied for temperature and VSS reduction con-
     siderations.
Aerators: 0.1 HP/1,000 gallons

Temperature correction;,  percent reduction @ T = (% Reduction
     @ 20°C) (1.06)'^°'
     where T = calculation temperature ( C)

Sludge - flow rate (gpd)


Hydraulic retention time

Digested biological solids

Digester basin (12' SWD + 3'  Freeboard)
      300,000 gal:, steel tank, above ground
     _300,000 gal: earthen basin,  with plastic membrane
       1 iner
Floating, 1ow-speed mechanical aerators
Sludge-transfer pumps (progressive-cavity,
       vari able-speed)
                                     69

                                     J-72

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                             VACUUM FILTRATION

     Vacuum filtration, pressure filtration, and centrifugation all  are accepted sludc
dewatering techniques.  The choice is usually based on technical  effectiveness,  and
depends on the type of sludge to be dewatered.  Vacuum filtration is discussed here;
pressure filtration is covered in a separate section of this Catalog.
     The rotary vacuum filter is used in the model to dewater chemical  sludges,
biological sludges, and their various combinations.  The sludges  are fed to the  vacuurr
filter at various solids concentrations from the sludge thickener.   Lime and ferric
chloride are used to condition all biological sludges for dewatering;  conditioning
is also required for some chemical sludges.  The quantities of conditioners required
are defined as a certain weight percentage of the sludge being dewatered.   (See  the
attached design data sheet for the lime and ferric chloride requirements for different
sludges.)  The resulting sludge cake from the vacuum filter is either sent to a  centre
landfill or incinerated.  Filtrate from the vacuum filtration operation is pumped
to the head end of the plant.
     Filter surface area is the basis for determination of the associated costs  of
a vacuum filtration system.  Factors which affect filter surface  areas  are filter
yield and operation time.  Filter yield, defined as pounds of dry sludge filtered per
hour per square foot of surface area, varies depending on the type  and  quantity  of
sludge being filtered.  Filter yields for both chemical and biological  sludges are pre
on the attached design data sheet.  In the case of combined sludges, weighted averages
determine filter yields.  Performance of the designed vacuum filter  is  dependent
on the type of sludge.  Cake moistures for different sludges are  also presented  on
the attached design data sheet.  In combination sludge cases, weighted  average techniq
again are used to determine sludge cake moisture.
                                      70
                                      J-73

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                             VACUUM  FILTRATION


FUNCTION:           Dewatering of  sludge
PARAMETERS
AFFECTED:           Sludge Moisture  Content
EFFECTIVENESS/
DESIGN BASIS:       Chemical  requirements, filter yields, expected cake solids:
                                       P r.                      Expected
               Sludge Type     Lime     reu 3.     Filter Yield   Cake Solids
                                %        _%	      Ib/hr/sq ft       %
               Biological        15      4            2               12
               Primary          8      1.5          8               25
               D.A.F. Chemical   8      1.5          8               25
                 Float
               Sulfide          20        -           1.2             20
               Incinerator      8      1.5          8               25
                 Scrubber  Sludge
               Iron             20        -           1.2             20
               Alum             20        -           0.8             20
               Lime                                 10               40
               Combined                Weighted Average
                    Filtrate  Quality:  1,000 ppm TSS  (maximum)
                                      71

                                     J-74

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TREATABILITY
FACTOR:             None

COST PARAMETER:     Filter media surface area

RESIDUES:           Filtrate (return to head end of  plant)
                    Filter cake - see effectiveness/design  basis
MAJOR               Vacuum filters (two)
EQUIPMENT:          Sludge conditioning unit
                         Mix chamber with mixers,  carbon  steel
                         Fed- storage and feed unit,  rubber-lined  carbon
                             •'steel
                         Lime storage and feed system,  carbon  steel
                    Filtrate return  system (receivers  and pumps), carbon
                         steel
                    Cake-conveying units, carbon steel
                    Cake storage units, carbon steel
                         Hopper
                         Bin activator
                    Vacuum pumps (two) including silencers
                    Facilities for equipment shelter
                    Building sump and pumps
                                    72

                                   J-75

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                            PRESSURE FILTRATION

     Pressure filtration (filter press)  is available as  an alternative to vacuum filtr
It is applicable to all  types of sludges and is used whenever the  required solids cone
for the dewatered sludge is higher than  the maximum achievable by  vacuum filtration.
     The application of  pressure filtration encountered  most frequently is the dewater
of waste activated (biological)  sludge prior to incineration.   Filter  presses  are used
in this situation because they can produce a dewatered sludge with a solids concentrat
of 35 percent or more, which is  high enough for self-sustained combustion (no  auxiliar
fuel required).   Filter  presses  can also be used to dewater chemical  or primary sludge
that are to be disposed  of in a  landfill;  their advantage is a greater reduction in si
volume, which could be  an important factor if the landfill is small  relative to demand
or if the haul distance  to the landfill  is significant.
     The pressure filtration system is sized on the basis of 8 hours  per day,  5 days
per week operation.  A minimum of two filters is provided, which permits the design
sludge load to be processed by the remaining filter (or  filters) over  a longer period
of time (e.g., 16 hours  per day  for a 2-filter system) when one filter is out  of servi
                                     73
                                    0-76

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FUNCTION:

PARAMETER
AFFECTED:

EFFECTIVENESS/
DESIGN BASIS:
             PRESSURE FILTRATION


     Dewatering of sludge


     Sludge moisture content

     Chemical requirements,  filter yields,  expected  cake  solids:


                        FeCl,
                                Lime
     Sludge       Expected
Loading?    Cake Solids
  lb/ft-/cycle
Sludge Type

Biological
Process primary
  D.A.F. Chemical
  float
Sulfide
Incinerator
  Scrubber Sludge
Iron
Alum
Lime
     *Three cycles per 8-hour shift

Diatomaceous-earth Requirement:   approx.  8  lb/100  sq ft  of  filter  area
8
5
5
30
5
_
-
-
15
10
10
-
10
30
30
-
1.5
2.2
2.2
2.2
2.2
1.6
1.6
3.6
35
45
45
40
45
40
40
50
                                      74

                                     J-77

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TREATABILITY
FACTOR:             None
COST PARAMETER:      Filter  plate area

RESIDUES:           Filtrate -  to clarification
                    Cake -  to incineration  or  landfill
MAJOR               Feed pumps
EQUIPMENT:          Contact tank, carbon steel
                    Surge tanks, carbon steel
                    Ferric chloride tank, rubber-lined  carbon  steel
                    Ferric chloride pumps
                    Filters, carbon steel/cast iron
                    Cake conveyors, carbon  steel
                    Filtrate tank, carbon steel
                    Precoat blower
                    Bag breaker
                    Precoat storage bin, carbon  steel
                    Precoat feeder
                    Precoat slurry tank
                    Precoat pumps
                                      75

                                     J-78

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                                  LANDFILL

     Landfill is the method of ultimate disposal for ash and dewatered sludge in
the treatment model.  Depending on existing legislation and the particulars of a
given situation, an individual company may either landfill  on unused land on plant
property, purchase land on a suitable site away from plant  property, or utilize a
public or privately-owned landfill.  For the purposes of the model, it is assumed that
a company will construct and operate a controlled landfill  on a suitable site on its
own property, away from the production area.  The location, design, construction,
and operation of the controlled industrial landfill are such as to minimize degradatio
of air and water quality in the immediate area of the landfill.
     In the initial design of a controlled landfill, area requirements are of prime
concern.  The landfill is designed to handle all dewatered  sludges/residues produced
in a 20-year period; but operation is based on 2-year cells.  Loading rates to the
landfill vary depending on the type of sludge being landfilled, and on the dewatering
method used (vacuum or pressure filtration).  The attached  design data sheets present
all landfill loadings and other design parameters.
     The area and loading requirements presented are based  on a mixture of sludge
and soil to a final solids concentration of 80 percent.  The landfill area designated
for each landfill cell is adequately diked and has easy access for earthmoving and
dumping equipment;  to account for this extra area requirement, the basic cell area
requirement for sludge and soil is increased by 25 percent.  While one cell is being
utilized, the next 2-year cell is being constructed, thus providing flexibility in oper
The landfill cell area is lined with a plastic membrane liner to contain leachate flow
A 2-foot layer of sand drainage material  is placed above this liner on the landfill
bottom.  Any leachate that develops percolates through the  landfill sludge layer,
hits the drainage material and then drains down the slightly-sloped landfill bottom
toward a central leachate collection basin.   Besides collecting leachate, this basin
also collects rainwater.  Central-col lection-basin water is treated by a package physic
chemical treatment system.  Leachate monitoring wells are strategically placed
around the landfill to determine whether there is any leachate contamination of
groundwater.  In addition, an underdrain system is provided to intercept any leachate
that leaks through the liner and prevent it from reaching the groundwater.
                                      76
                                     J-79

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                                 LANDFILL
FUNCTION:

APPLICATION
LIMITS:

DESIGN BASIS:
TREATABILITY
FACTOR:
Ultimate disposal  of sludge

None
Loading rate based on adding sludge and soil  to 80  percent
sol ids:
                    Sludge

                    WAS
                    Primary
                    Lime
                    FeCl.,
                    Alum"3
                    Sulfide
                    Fly Ash
               Sludge Solids Loading
               Vacuum       Pressure
               F i 1 ter        F i 1 ter
          (Dry tons/
           Acre-ft)
          From Process
                 27
                 71
                170
                 49
                 49
                 49
103
169
270
124
122
122
                                            318
                    Operating time:  20 years  with 2-year  cells
                    Final  area requirement:  1.25  x sludge area  requirement
                    Landfill  depth:  10 ft.
None
COST PARAMETER:     Land area requirements based -on sludge  application rate.

COST CURVE SCALE
FACTOR:
RESIDUES:


MAJOR
EQUIPMENT:
None

Leachate
Runoff
Membrane-lined earthern landfill cells,  2-yr capacity each
Bulldozer
Leachate monitoring wells around landfill
Wide-tire dump truck(s)
Leachate collection basin, earthern basin,  membrane-lined
Leachate collection sump (concrete),  with transfer pump.
Package treatment plant feed pumps in concrete sump.
Package treatment plant
Leachate-monitoring underdrain system
                                      77

                                     J-80

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                                INCINERATION

     Incineration is available as a volume-reduction method for organic
primary sludges and waste activated sludges,  and as  a final  disposal  method
for oils and the liquid residues from extraction/distillation.   Two types
of incinerators (the multiple-hearth and vertical  liquid waste  type)  are
used in the model, depending on the particular type  of waste to be incinerated.
If biological sludge, oil, or liquid residue  quantities  are below a defined
limit, the residue is handled by contractor disposal rather than by incinera-
tion.
     The multiple-hearth incinerator is used  to burn liquid residues  from
extraction/distillation and biological  sludges with  or without  waste  oils.
Gases produced by residue combustion pass through  a  venturi scrubber  for
particulate removal.  If removal of contaminants in  a vapor phase is  also
required, the off gases will then be passed through  a packed-tower alkaline
scrubber.  Hearth area requirements are based on a loading of 8 Ib/hr/sq ft.
     Depending on the calorific value of the  wastes  being burned in the
incinerator, auxiliary fuels may be necess.ary to support combustion.
The attached design data sheet presents typical fuel values of  typical
wastes and of No. 2 fuel oil, which is  the auxiliary fuel to be used  when
necessary to assist combustion.  Storage and  feeding facilities for No. 2
fuel oil are provided even if the heat  value  of the  wastes is high enough
to sustain combustion, because auxiliary fuel is considered necessary
for incinerator start-up.
     When liquid wastes (oils, extraction/distillation residues) are  burned
without being mixed with biological sludges,  a liquid waste incinerator
is used.  Waste gases are cleaned with  a venturi scrubber, followed by  a
packed-tower alkaline scrubber, which is considered  mandatory for liquid
waste incineration.  The combustion chamber volume is based on  a heat
release value Of 40,000 Btu/hr/cu ft.
                                      78
                                     J-81

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     No spare units  are  provided for inci neration^and scrubbing facilities.
In lieu of  duplicate units,  a  storage vessel that has the capacity to
hold two weeks'  feed (average  rate) to the incinerator is provided.
     Separate design data sheets are presented for Sludge Incineration
(Liquid Optional)  and for Liquid Incineration.
                                    79
                                   J-82

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                 SLUDGE  INCINERATION  (with LIQUID OPTIONAL)
FUNCTION:

PARAMETERS
AFFECTED:

EFFECTIVENESS:
APPLICATION
LIMITS:

DESIGN BASIS:
TREATABILITY
FACTOR:

COST PARAMETER(S)

COST CURVE SCALE
FACTOR:

RESIDUES:
Volume reduction

Sludge volume

Type of Waste
Organic primary sludge
Waste activated sludge
Grease, scum, oily wastes
 Ash Remaining
After Combustion
      35%
      35%
       5%
Sludge must be dewatered before inci nceration

LjQ:iy,4.u av%Qa _ Total 1b of waste/hr
Hearth area -  8.0 ib/nr/Sq ft	

Total heat release = (Ib waste/hr) x (avg Btu/lb)
                    + (Ib aux fuel/hr)  x (Btu/lb)
Typical fuel values of wastes
                            Fuel Value
Type of Waste            Btu/lb dry solids
Organic primary sludge          6,500
Grease, scum, oily wastes      16,000 (pure fraction only)
Waste Activated Sludge          8,000 (volatiles only)

Typical fuel value of No. 2 fuel oil =  18,000 Btu/lb
       (a 7.25 Ib/gal
Typical fuel requirements of water = 2,000 Btu/lb
Operating time:   24 hrs/day; 5 days/week

Sludge moisture content
Lb/hr of wet sludge


None
Ash (see EFFECTIVENESS for percent)
(See LANDFILL)
Venturi scrubber slurry
Spent packed-tower scrubber liquor (if  liquid wastes
     are present)
                                      80

                                     J-83

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          SLUDGE INCINERATION (with LIQUID OPTIONAL)   (Continued)


MAJOR               Multiple-hearth incinerator,  including  cooling-air
EQUIPMENT:               fan for center shaft  and combustion-air  blowers
                         (supplied as  vendor package).
                    Sludge handling system (storage  vessel,  bin vibrator,
                         conveyors, controls),  carbon  steel.
                    Gas-scrubbing unit (Venturi  type).
                    Exhaust blower
                    Separator,  carbon  steel.
                    Venturi recycle pumps.
                    Venturi recycle tank
                    Ash-handling system (conveyors,  storage vessel,  vibrator)
                    Packed tower (optional).
                    Caustic storage and feed system, carbon steel.
                    Liquid waste or auxiliary  fuel  system
                         (storage vessel,  pumps,  controls).
                    Gas-quenching system,  carbon  steel.
                    Vent stack.
                    Afterburner.
                    Feed storage tank  and  bin  vibrator,  carbon steel.
                    Asphalt slab, surrounded by concrete wall, for  storing
                         a 14-day supply of sludge  when  the incinerator
                         is not in operation.
                                     81

                                    J-84

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        LIQUID INCINERATION (OILS, EXTRACTION/DISTILLATION RESIDUE)
FUNCTION:

PARAMETERS
AFFECTED:

EFFECTIVENESS:

APPLICATION
LIMITS:

DESIGN BASIS:
Ultimate disposal

All organics

Total combustion; negligible residue
NONE
Total heat release =
                   +

Minimum incinerator
     volume
 (Ib waste/hr) x (avg Btu/lb)
 (Ib aux. fuel/hr)  x (Btu/lb)

_ Total heat released (Btu/hr)
      40,000 Btu/cu ft/hr
                    Typical fuel values of wastes:
                    Type of Haste
                      Oils
                      Phenolics
                      Paraffins
                      Aromatics
                      Cyclics
                      01ef i ns
                    Fuel Value (Btu/lb)

                         16,000
                         14,000
                         19,000
                         17,500
                         18,700
                         19,500
                    Operating time:  24 hr/day;  5 days/week
                                      82

                                    J-85

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TREATABILITY
FACTOR:             Moisture content  of the  waste

COST PARAMETER:     Required heat release

COST CURVE SCALE
FACTOR:             None

RESIDUE:            Venturi  ash scrubber slurry
                    Spent packed-tower scrubber liquor.

MAJOR               Incinerator
EQUIPMENT:          Waste injector assembly
                    Combustion air blower
                    Liquid waste storage and feed system,  stainless steel
                    Fuel-oil storage  & feed  system,  carbon steel
                    Venturi  scrubber  unit
                    Cyclone separator
                    Venturi  recycle tank, with agitator
                    Venturi  recycle pumps
                    Packed tower
                    Packed tower recirculation tank  with agitator
                    Gas quenching system
                    Vent stack, carbon steel
                    Gas-emission monitoring  equipment
                                     83

                                    J-86

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                             AMMONIA STRIPPING

     Ammonia stripping removes  ammonia from pre-limed wastewaters  by  using
direct-contact steam as the heat input.   Two stripping towers  are  used,  each  with
an independent collection system.   Each tower has  the same wastewater flow  rate,
with 200 gallons per minute specified as the upper limit  for flow  to  a column.
     Pre-liming is necessary to facilitate the removal of ammonia,  and a pH  of
10.5 or higher is specified for the system.   Ammonia removal is  99  percent  of the
influent rate, and the attainable effluent limit  is set at 50  ppm  of  ammonia.
     The ammonia is collected overhead and sent to a spary absorber,  where  it is
reacted with dilute sulfuric acid to produce ammonium sulfate, which  is recovered
as a crystalline powder.
                                     84
                                    J-87

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                             AMMONIA STRIPPING
FUNCTION:


PARAMETERS
AFFECTED:

EFFECTIVENESS
APPLICATION
LIMITS:


DESIGN BASIS:
TREATABILITY
FACTOR:

COST PARAMETER:

COST CURVE SCALE
FACTOR:

RESIDUES:

MAJOR
EQUIPMENT:
Removal of ammonia from wastewater by direct injection
of steam into a distillation column.

Ammonia concentration

99 percent removal of ammonia, or 50  ppm of ammonia in
the effluent.
TSS:   50 mg/1
pH:    10.5
NH3-N: 500 mg/1

Flow = average of the average and high values
Stripping steam rate:  1.4 Ib/gal of  feed
Bottoms temperature:   232 F
24 actual trays at 24" spacing
25 weight percent ammonia vapor leaving dephlegmator
Sulfuric acid (10%)  rate = two times  the stoichiometric
     requirement
60-foot high column
400 gallon per minute maximum flow per column


None
Flow per stripping column

For two or more operating columns Ipjus a spare),
multiply by: (number of columns/2)
Ammonium sulfate recovered as product

Sieve-tray stripping columns, carbon  steel
Bottoms cooler
                                     85

                                    J-88

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Bottoms flash tanks
Dephlegmators
Accumulators
Spray absorption tower
Crystal!izer
Centrifuge
Rotary drum dryer
Slurry tanks
Sulfuric  acid feed tank
                86

               J-89

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                              STEAM STRIPPING

     Steam stripping causes the separation of water-immiscible (or slightly water-
miscible) materials from a wastewater stream by means  of direct-contact steam
as the heat input.  For the purpose of this design calculation,  the concentration of
the organic pollutant in the influent wastewater stream is assumed to be at or below
the solubility of the pollutant at ambient conditions.
     The influent stream is preheated by the effluent  stream in  a counter-current
heat exchanger.  It enters the stripping column near the top, and cascades down
over a number of trays.  Steam, which is added at the  bottom of  the column, causes
the organics to vaporize, and the water/organic azeotrope exits  at the top.  The
vapors are condensed, and the water and organic phases  separate  in a decanter.
The organic phase is either recovered or incinerated.   The water phase, which is
saturated with the organic contaminants, is recycled to the top  of the column.
     It is possible that the organics removed will be  highly toxic.  Therefore, the
removal efficiency of this unit process must be constant and the operation must
be uninterrupted.  Accordingly, each steam stripper will be provided with a spare
unit at 100 percent of design capacity.  This should insure that maintenance problems
will not adversely affect the degree of treatment provided.
                                      87
                                    J-90

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                              STEAM STRIPPING
FUNCTION:


PARAMETERS
AFFECTED:

EFFECTIVENESS:

APPLICATION
LIMITS:

DESIGN BASIS:
TREATABILITY
FACTOR:
COST PARAMETER:

COST CURVE SCALE
FACTOR:
Separation of
wastewater
              specific dissolved organics  from
Concentration of organics, temperature
Removal to achievable outlet concentration, usually 50  g/1
TSS:
Oil:
        50 mg/1
       100 mg/1
Design flow = 120 percent of the average flow
Maximum number of trays = 22
Maximum column diameter = 6 ft
Tray spacing = 2.5 ft
Organic concentration:  No higher than its solubility
     at ambient conditions
Pollutant molecular weight
Overall column efficiency
Pollutant latent heat of vaporization
Achievable effluent concentration (each pollutant)
Steam requirement (each pollutant)
Vapor- liquid equilibrium ratio.
Activity coefficient (deviation from ideal -
     solution behavior)
Diameter of the column
Number of columns
     For two or more
     spare), multiply
Number of trays
                     operating columns (plus a
                      by:  (number of columns/2)
                                                                    ,.
                                     88

                                    J-91

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RESIDUES:           Distillate is  decanted;  water  phase  is  returned to
                    column;  organic  phase is recovered or incinerated.

MAJOR               Feed tank, carbon steel
EQUIPMENT           Distillation columns  with sieve  trays,  carbon  steel
                    Feed preheater,  carbon steel
                    Condensers,  carbon steel
                    Accumulator/decanter, carbon  steel
                    Organic-phase  pumps
                    Water-phase recycle pumps
                    Column feed pumps
                    Bottoms pumps
                                       89

                                      J-92

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                            SOLVENT EXTRACTION

     This unit process is used for removal of dissolved phenol ics or other
organics from a contaminated stream in cases where distillation is inapplicable
or too costly, such as with some azeotropic mixtures or with mixtures
that have components whose boiling points are very close.   Extraction
is capable of 99.5 percent removal or reduction to an effluent  concentration
of 10 mg/1.
     The optimum solvent for extraction is selected upon consideration
of several properties, including; solubility, density (difference between
solvent and water), interfacial tension, selectivity, distribution coefficient,
chemical inertness, viscosity, flammability, pH, ease of solvent recovery,
and cost.

                            SOLVENT EXTRACTION
FUNCTION:

PARAMETERS
AFFECTED:
EFFECTIVENESS:

APPLICATION
LIMITS:
DESIGN BASIS:

TREATABILITY
FACTOR:
Removal of dissolved phenol ics or other organics into
a water-immiscible solvent stream.

Organic or phenolic concentration.
99.5 percent removal or 10 ppm of the pollutant and
residual solvent in the effluent.
Temperature:  50 to 150°F
pH:   6.0 to 9.0
TSS:  25 mg/1
Solute concentration must be less than the solubility
     of the solute in water.
Boiling point of the organic must be less than 230 C.
Removal to 99.5 percent or 10 ppm organic.
120 percent of flow
Contact time = 20 minutes
Distribution coefficient
Solubility of the pollutant in water
Latent heat of the pollutant
                                      90
                                     J-93

-------
                    Pollutant specific heat
COST PARAMETER:     Flow

COST CURVE SCALE
FACTOR:             Percent removal  efficiency

RESIDUES:           The phenolic or  other organic compound is recovered
                         from the solvent by distillation in a solvent-
                         recovery system.

MAJOR               Extraction column with extract reflux, carbon steel
EQUIPMENT:          Recovered-sol vent pump
                    Solvent storage  tank
                    Solvent feed pump
                    Pre-heater (solvent and/or water stream), stainless steel
                    Spent solvent pump
                    Spent solvent filter
                    Solvent-recovery distillation column
                    Reboiler
                    Condenser
                    Effluent transfer pump
                    Accumul ator
                    Pump for removal of recovered pollutant
                                      91

                                      J-94

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                COOLING TOWER/HEAT EXCHANGER/STEAM INJECTOR

     Cooling towers or heat exchangers may be required to lower the temperature
of a wastewater stream for either or both of two reasons.  First,  if a biological  syst
is used, its temperature may not exceed 105°F; therefore, the influent stream must
be cooled prior to treatment.   Second, water quality criteria of the receiving stream
may place a maximum temperature limitation on the plant's wastewater discharge;
in this case, the treated effluent wastewater must be cooled.
     Heat exchangers are used for small flows, and cooling towers  for larger ones.
Thus, cooling towers are specified whenever the required surface area of  a heat
exchanger would exceed 5,000 sq ft.  Area requirements are based on she11-and-tube,
countercurrent heat exchangers.  Because the tubes can be individually valved off
for maintenance purposes, no spare exchanger is provided.   Cooling towers are
the mechanical-draft type, which use fans to improve the rate of heat transfer.
The water is cascaded down the tower through splash bars, causing continuous shearing
that results in maximum contact with the rising air, whose upward flow is  induced
by a fan at the top of the tower.  The tower generally lowers the  water temperature
to within 3 to 5°F of the wet-bulb temperature of the incoming air.  Multiple towers
(or cells) are provided whenever practicable.
     In the winter, it may be necessary to heat a waste stream prior to biological
treatment.  This is done by direct injection of steam.  An energy balance  is used
to determine the stean requirements.  Because the cost of generating the steam
is much greater than the cost of the equipment needed to add it, no capital  cost
curve (and no design data sheet) is included for this feature of the unit  process;
operating costs are calculated, based on pounds of steam per day.
                                     92
                                    J-95

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                              COOLING TOWERS
FUNCTION:
PARAMETERS
AFFECTED:

EFFECTIVENESS:

APPLICATION
LIMIT:

DESIGN BASIS:
TREATABILITY
FACTOR:

COST PARAMETER:

COST CURVE SCALE
FACTORS:
MAJOR
EQUIPMENT:
To cool a wastewater stream to the operating temperature
of a subsequent unit process, or to meet receiving stream
temperature requirements


Wastewater temperature

Approach to within 3-5°F of wet-bulb temperature of air

Desired temperature cannot be lower than 5°F above
the wet-bulb temperature of air

Design flow = 110 percent of the average flow
Wet-bulb temperature = 78 F


None

Flow rate

Change in wastewater temperature
Difference between effluent wastewater temperature
     and the wet-bulb temperature of the air

Cooling tower cells, wood
Top-mounted fans, steel
Hot and cold wells, concrete
Vertical feed pumps, steel
Chlorine storage and feed system, steel
                                    93

                                    J-96

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                               HEAT  EXCHANGER
FUNCTION:


PARAMETERS
AFFECTED:

EFFECTIVENESS:


APPLICATION
LIMITS:


DESIGN BASIS:
TREATABILITY
FACTOR:

COST PARAMETER:

COST CURVE SCALE
FACTOR:

MAJOR
EQUIPMENT:
Cooling of a wastewater stream in an exchanger, using
cowater as the heat-transfer medium.


Wastewater temperature

Cooling normally to within 5°F of the inlet cooling water
temperature

Desired temperature cannot be lower than 5°F above
     the inlet cooling water temperature.
Maximum heat transfer Area = 5,000 sq ft
Countercurrent flow
Overall heat transfer coefficient U = 100
Change in cooling water temperature is half the
     change in the wastewater temperature


None
Heat transfer area
None
Concrete wet well with carbon steel feed pumps
Shell-and-tube heat exchanger, carbon steel
                                     94

                                    J-97

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                            DEEP-WELL DISPOSAL

     Deep wells are used as a means  of ultimate disposal  of  liquid wastes.   This
unit process, however,  is not permitted  in all  areas  of  the  country,  and  is  used only
when in compliance with state and local  regulations.
     All wastewater outside a pH range of  6.5 to 8.0  must be neutralized  prior to
injection, and the maximum allowable suspended solids concerntration  is 10 mg/1.
However, the neutralization and filtration facilities needed to meet  these  limits
are not included as part of this unit process.
     All estimates are based on a well depth of 3,500 feet.   Flow rates vary from
0.02 to 1.5 MGD, and a constant discharge  pressure of 500 psi  is assumed.
                            DEEP-WELL DISPOSAL
FUNCTION:
PARAMETERS
AFFECTED:
EFFECTIVENESS:
APPLICATION
LIMITS:
TREATABILITY
FACTOR:
COST PARAMETER:
SCALE FACTOR:
RESIDUES:
MAJOR
EQUIPMENT:
Ultimate disposal of liquid waste

None
Total disposal
Where permitted by law
Where subsurface geology is suitable
Suspended solids  10 mg/1
pH 6.5-8.0

None
Flow rate
None
None
Injection pumps, carbon steel
Deep-well, 3,500 ft
                                     95
                                    J-98

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                               LIME  HANDLING

     Lime (or caustic)  addition is  required  in  connection with several unit processes,
including neutralization,  coagulation,  vacuum filtration, pressure filtration, and
sludge incineration.   If the lime requirement exceeds 8,000 Ib/day of hydrated lime,
quick lime is used instead.   If less than  500 Ib/day are needed, lime is replaced by
caustic.
     Both quick lime and hydrated lime  are supplied by truck and unloaded by blowers
to storage silos.   Automatic feeding equipment  is  used to slurry the lime to a 10 perc
concentration.  Slakers are  provided when  quick lime is involved.  Spares are providec
for all feeding equipment  such as pumps,  volumetric feeders, and slakers.  Only one
lime storage silo (or one  liquid caustic  storage tank) is provided, since neither of
these should have to be taken out of serivce.
     The lime slurry is stored in agitated pits,  from which it is pumped to the other
unit processes.  The slurry  pipeline is operated as a loop, past all "user" unit proce
and then back to the slurry  storage  pits.  The  slurry feed pumps run continuously,
even when there is no demand for lime.  This  is necessary to provide a constant moveme
in the line to prevent clogging.  It also  provides sufficient pressure in the line to
satisfy the demand immediately.
     If caustic is used, the system  consists  of a liquid caustic storage tank and feec
pumps.
                               LIME  HANDLING

FUNCTION:           Provide lime slurry (or caustic) to  other  unit
                    processes.
PARAMETERS
AFFECTED:           None
EFFECTIVENESS:      Not applicable
APPLICATION          500 Ibs/day:   Caustic
LIMITS:              500-8,000  Ibs/day:   Hydrated Lime
                     8,000 Ibs/day:   Quick Lime
DESIGN BASIS:       Lime silo capacity sized  for two weeks storage, or
                                    96
                                   J-99

-------
                    for one week  storage  plus  minimum  bulk.delivery  load,
                    whichever  is  larger.
TREATABILITY
FACTOR:             None

COST PARAMETER:      Lbs/day of hydrated  lime

SCALE FACTOR:        None

RESIDUES:           None

MAJOR               Caustic:

EQUIPMENT:               Caustic  storage  tank,  carbon  steel
                         Caustic  feed  pumps, carbon  steel
                    Hydrated Lime:
                         Storage  silo, carbon  steel
                         Bag filter, carbon steel  housing
                         Bin vibrator, carbon  steel
                         Lime  feeder  (plus  warehouse spare), carbon  steel
                         Slurry tanks  with  agitators,  carbon steel
                         Feed  pumps, carbon steel
                    Quick Lime:
                         Storage  silo, carbon  steel
                         Bag filter, carbon steel  housing
                         Bin vibrator, carbon  steel
                         Lime  slakers  with  grit collectors, carbon steel
                         Lime  feeders, carbon  steel
                         Slurry tanks, carbon  steel
                                       97

                                     J-100

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           APPENDIX K



DESCRIPTION OF MODEL COMPONENTS AND USE

-------
                                APPENDIX K

                  DESCRIPTION OF MODEL COMPONENTS AND USE
    This Appendix describes the computer model developed for  EPA  by  Catalytic,
Inc. that can evaluate the costs and performance of various wastewater  and
sludge treatment technology trains in treating specific wastestreams generated
in the Organic Chemicals and Plastics/Synthetic Fibers  Industry.   The Model
has three distinct components:   (1) the permanent files which contain data on
the design criteria, costs, and performance of the treatment  trains, (2)  the
28 treatment technology program modules which model the design, performance,
and cost of each unit treatment process; and (3) the control  programs that
sequence the treatment units and estimate the overall costs.   Details of  each
of these three major components are discussed in this section.  The
relationships between the files and programs are depicted in  Figure  K-l,  and
the design assumptions incorporated into each treatment technology module are
stated in Appendix J, the Treatment Catalogue.
A.  PERMANENT FILES

    The Model programs draw data from eight separate permanent  files  in
executing the design and cost estimating routines.   These data  files  are
separate from the treatment technology modules and control programs  in order
to facilitate not only updating the cost and treatment performance information
but also overriding the default values built into the Model.  During  each
Model run the user may override the default values with new values.

    The eight data files, discussed in sequence below, are:

         •    Master Process File
         •    Parameter and Treatment Selection File
         •    Effluent Target File
         •    Unit Process Sequence Rules Files
         •    Plant Adder File
         •    Capital Costs File
         •    Operating Costs File
         •    Costs Allocation Rules File

    1.   Master Process File.  It was not practical to evaluate regulatory
         options for each of the thousands of OCPSF production  plants.  Using
         pollutant loadings obtained during the Verification  phase sampling
         program, responses to Section 308 questionnaires, and  engineering
         judgment, a Master Process File was developed.   For  176 major
         product/processes, this file estimates the flow and  loadings for
         conventional, nonconventional and priority pollutants, as well as
         rate constants for BOD 5 and COD.  The user may employ the Master
         Process File to simulate wastewaters from the Generalized Plant
                                   K-l

-------
     Configurations  (GPC's)  or  from  any combination  of  the  176
     product/processes.   Alternatively,  the  user  can specify other raw
     waste loads  and flows.

2.   Parameter and Treatment Selection File.   The Parameter and Treatment
     Selection File  contains pollutant-specific treatability information
     that  is  used to calculate  the treatment performance  of eight  of the
     treatment unit  processes for each pollutant  considered treatable by
     that  technology.  The  information tabulated  for each of the various
     technologies is:

     •    Activated  Carbon  Adsorption  -- control  constant,
          two sets of the Langmuir adsorption constants Q and b
          (one for influent  values below the control constant
          and another for influent values above the  control
          constant),  lowest  effluent concentration assumed  by
          the Model  to be achievable,  and Peclet  number.

     •    Activated  Sludge  -- reaction rate  constant and
          lowest  modeled effluent concentration.

     •    Chemical Oxidation -- applicable oxidizing
          chemical,  ratio of oxidizing chemical to pollutant,
          and lowest and highest predicted effluent
          concentrations assumed by  the Model to  be
          achievable.

     •    Chemical Precipitation --  water solubility of the
          pollutant,  applicable coagulating  chemical, and ratio
          of  coagulating chemical to pollutant.

     •    Ion Exchange -- type  of resin (e.g.,  cationic or
          anionic),  resin exchange capacity,  lowest  effluent
          concentration  assumed by the Model to be achievable,
          type of regeneration  chemical, and dose of
          regeneration chemical.

     •    Ozonation  -- ratio of ozone  to pollutant,  lowest
          and highest effluent  concentrations assumed by  the
          Model to be achievable.

     •    Solvent Extraction -- distribution coefficients for
          the solvents paraffin and  tricresyl phosphate;  water
          solubility, latent heat, and specific heat of the
          pollutant.

     •    Steam Stripping -- molecular weight (used  in
          calculating the molar reflux ratio),  column
          efficiency, latent heat of vaporization, lowest
          predicted  effluent concentration,  steam dosage,
          vapor/liquid equilibrium ratio, and activity
          coefficient.
                               K-2

-------
     The Parameter and Treatment Selection File also contains information
     on how each treatment unit process is typically used (e.g.,
     in-process, pretreatment of comingled streams, or end-of-pipe
     treatment).

3.   Effluent Target File.  The Effluent Target File (ETF) contains
     concentration limitations equivalent to the concentrations presented
     in EPA's Multi-Media Environmental Goals for Environmental
     Assessment (IERL, Research Triangle Park, N.C. 1977).  Override
     options allow the user to evaluate any desired set of target
     concentrations for conventional, nonconventional, and priority
     pollutants.  This override capability facilitates analyzing the
     sensitivity of treatment cost to target effluent concentration.

4.   Unit Process Sequence Rules File.  The Unit Process Sequence Rules
     File contains rules for arranging the unit treatment processes into
     sequences consistent with OCPSF industry wastewater engineering
     practice.  This file also contains the rules for inserting necessary
     ancillary unit processes into a treatment train (e.g.,  addition of
     nutrients where needed for activated sludge; filtration where
     necessary before activated carbon adsorption).

5.   Plant Adder File.  If commanded to do so by the user, this file adds
     wasteloads and flows from plant washdown, sanitary and utility waste
     disposal, spills, and other non-process sources of plant waste load.
     Only flow and conventional pollutants (e.g., suspended solids and
     BOD) data are contained in this file.  To simulate these non-process
     flows and loadings, the file increases the total flow by 50 percent
     of the estimated product/process flow calculated by the Master
     Process File; the file increases the loadings of the individual
     conventional pollutants by factors ranging from five to fifteen
     percent.

     Following user option decisions, the Model's programs design and
     assess performance of various treatment systems using data from the
     five files discussed above.  The data in the three remaining
     permanent files--the Capital Costs File, Operating Costs File, and
     Cost Allocation Rules File--are utilized solely for estimating
     treatment system costs.

6.   Capital Costs File.  The Capital Costs File contains the equations
     for capital cost curves for each unit process.  Each cost curve was
     developed by estimating the cost of the entire unit treatment
     process,  including required mechanical equipment, electrical
     equipment, tanks, piping, and system back-up equipment, for four
     different sizes of the treatment unit process.  Curves  relating cost
     to size were developed from these four estimates.  For  unit processes
     where equipment requirements for small systems were significantly
     different than for large systems, a second costing curve for small
     units was generated.  For those unit process costs described by one
     curve, precision at the small-system end of the curve was increased
     by defining the curve in small segments.  The Capital Costs File
                               K-3

-------
         reflects the CE Plant Cost Index from Chemical Engineering Magazine,
         July 1977, of  204.7 .   The user can update costs by specifying a new
         Chemical Engineering Index.  The July 1982 CE Plant Cost Index value
         was 314.2.

    7.   Operating Costs File.  The Operating Costs File contains two types
         of costs or file elements.  The first type is organized by unit
         process and includes the elements listed in TABLE K-l.   For each
         technology, the Operating Cost File contains the wastewater-flow
         dependent values for shifts per day and service water flow that are
         necessary to calculate the cost for each element.

         The second set of elements in the Operating Costs File are those
         items consumed during operation of each treatment technology and
         include chemicals, electrical energy and other utilities such as fuel
         oil; the unit costs for these items are listed in TABLE K-2.  For
         each run, each treatment technology program module calculates the
         quantity of each item consumed annually by operation of the treatment
         technology.  The annual cost of each item consumed is the product of
         the quantity consumed and the unit cost of the item.  The Model user
         may override any of these unit costs.

    8.   Cost Allocation Rules File.  This file stores the information
         necessary to allocate capital and operating costs back to each
         product/process in proportion to that product/process's contribution
         to the overall loading of those pollutants which necessitate
         treatment.

    In addition to the eight permanent files just discussed, during a run the
Model stores relevant portions of the permanent files and any data calculated
in temporary working files.


B.  TREATMENT TECHNOLOGY PROGRAM MODULES

    Design, performance, and cost information on the 31 specific technologies
has been programmed' into the Model.  This technology information differs from
the information in the Treatment Catalogue written by Catalytic in the
mid-1970's in that this version includes the following:  additional unit
processes; improved specifications for each technology; allowable influent
quality and pollutant removal rates that have been revised to reflect the new
data obtained through recent treatability studies and the Section 308
questionnaires; more accurately defined capital and operating cost data and
cost scale factors for each unit process; changes incorporating current
industry design practices, observed performance, cost information and other
comments from reviews by the Chemical Manufacturers Association.  The
individual treatment technology modules encoded into the computer Model are
discussed in Appendix J, The Treatment Catalogue.  The 31 technologies
include:  wastewater treatment technologies; processes, such as nutrient
addition to activated sludge, which are ancillary to the wastewater treatment
technologies; one wastewater disposal process (deep well injection); and
sludge treatment and disposal technologies.
                                   K-4

-------
                     TABLE K-l

COST FACTOR FOR EACH ELEMENT IN OPERATING COST FILE




   ELEMENT                       COST FACTOR
Direct Labor                Shifts per Day
Supervision                 Percent of Direct Labor
Overhead                    Percent of Direct Labor
Laboratory Labor            Percent of Direct Labor
Maintenance                 Percent of Capital Cost
Services                    Percent of Capital Cost
Insurance and Taxes         Percent of Capital Cost
Service Water               Thousand Gallons per Day
                      K-5

-------
                 TABLE K-2

            OPERATING COST FILE
                 UNIT COSTS
UNIT
    COST
Energy
Fuel
Steam
Lime
Acid
Ammonia
Phosphate
Sodium Sulfide
FeCl3

Alum
Polymer
Activated Carbon
Methanol
Waste Hauling
Residue Disposal
SoIvent-Undecane
Solvent-Tricresyl Phos
Caustic
Chlorine
P. Permanganate
H. Peroxide
NaCl
$0.02/kw-hr
 0.46/gal
 0.0045/lb
 0.0149/lb
 0.0215/lb
 0.0789/lb
 0.604/lb
 0.1375/lb
 0.045/lb

 0.0645/lb
 2.00/lb
 0.52/lb
 0.0696/lb
 0.0004/lb-mile
 0.018/lb
 0.0137/lb
 0.76/lb
 0.1575/lb
 0.0713/lb
 0.48/lb
 0.386/lb
 0.0199/lb
NOTE:  Costs are in July, 1977 dollars.
                  K-6

-------
    In addition to the design criteria, sludge generation quantities, and
costing data that are generated by the treatment technology programs, limits
on allowable influent concentrations and variability are defined within each
treatment technology program.  The variability (ratio of maximum to minimum
concentration) for each pollutant is determined by the values in the Master
Process File and is reduced appropriately when waste streams merge.  As an
example of checking the influent limits, if activated sludge treatment is
selected, the influent is checked for temperature, pH, and concentrations of
oil and grease, ammonia, TSS, TDS, formaldehyde, sulfide, phenol, and various
metals.  If the influent waste stream concentration of any of these pollutants
violates the concentration limits or variability prescribed as acceptable to
the selected treatment process, Model control programs insert one or more
appropriate treatment technologies upstream as pretreatment.  Only after all
parameters satisfy the limits for the treatment technology originally chosen
(activated sludge in this example) will the Model design that treatment
technology unit.  Appendix J discusses and lists the design assumptions and
influent quality requirements for each treatment technology.

    Using the design assumptions and, as needed, the pollutant-specific
information in the Parameter and Treatment Selection File, these technology
modules size the treatment facilities, calculate the quantities of sludge
generated by the treatment process, and specify the cost and scale variables
necessary for estimating the cost of treatment.  Seven of the modules (e.g.,
the activated sludge temperature modification program) merely calculate
numbers that are used by other modules and have no internal cost variables.
TABLE K-3 lists the cost and scale factors of all the modules except those
seven.
C.  MODEL LOGIC CONTROL PROGRAMS

    The overall model logic control programs were developed to allow maximum
flexibility in manipulating the data files and the treatment technology
program modules.  The ten major control programs, their primary functions,
their handling of the permanent files, and user (operator) options are
diagrammed in FIGURE K-l and are discussed next.  The Model is not
interactive; the user selects his override options, including raw wasteload
specifications, before the run begins.

    The control programs operate sequentially.  The Model may be operated in
either of two modes:  (1) Model Selection Run Mode, where the Model selects
the unit treatment processes, sequences and sizes a system that will treat the
raw waste load to meet the target limits and estimates the costs of the system
or (2) Specified Unit Process Train mode, where the user selects the major
unit treatment processes, and the Model adds necessary ancillary processes,
sequences and sizes them, and estimates the costs of the system.  For both
modes, PARAM, the first program in the control sequence, extracts data from
the Master Process File and the Parameter and Treatment Selection File
necessary to select the major and ancillary treatment units, as appropriate.
The two modes and their routes are described in more detail next.
                                   K-7

-------
                                  TABLE K-3

                 COST AND SCALE FACTORS FOR EACH UNIT PROCESS
UNIT PROCESS
COST FACTOR
SCALE FACTOR
Equalization
Neutralization
Oil Separation
Dissolved Air Flotation
Coagulation/Flocculation
Clarification
Dual Media Filtration
Activated Sludge
Aeration

Nutrient Addition

Nitrification
Denitrification
Ozonation

Activated Carbon
  Adsorption
Activated Carbon
  Regeneration
Gravity Thickening
Aerobic Digestion
Vacuum Filtration
Controlled Landfill
Solid and Liquid
  Incineration
Solvent Extraction
Ion Exchange
Flow Rate
Flow Rate
Flow Rate
Flow Rate
Flow Rate
Surface Area
Flow Rate
Flow Rate
Installed Horsepower
  per Aerator
Nitrogen/Phosphate
  Deficiency
Flow Rate
Flow Rate
Ozone Usage Rate and
  Flow Rate
Working Bed Volume

Total Hearth Area

Surface Area
Sludge Flow Rate
Filter Media Surface Area
Land Area Requirements
  from Sludge
  Application Rate
Sludge Moisture
  Content
Flow
Working Bed Volume
  and Flow
Flow Variability
Chemical Use Rate
Aeration Time
Number of Aerators
Aeration Time
Reaction Time
Number of Beds
Hydraulic Retention Time
Required Heat Release

% Removal Efficiency
Number of Beds
-- = No factor.
                                   K-8

-------
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    1.    Model Run Modes

         a.   Model Selection Run Mode

         If the Model Selection Run Mode has been input, SELECT develops a
skeletal treatment train by first assessing how much of each pollutant in each
product/process waste stream each in-process control technology can remove.
If removal is sufficient (the precise control percentage varies somewhat
depending on operator input), that technology will be considered by subsequent
programs in the total treatment design.  Selection of applicable end-of-pipe
unit processes is then performed similarly.

         After the potential treatment technologies for both segregated and
combined waste streams have been identified, they are organized by SEQUENCE
into the sequence which would typically be found in the industry.  The Unit
Process Sequence Rules File and information previously extracted from the
Parameter and Treatment Selection File contain the information required for
the sequencing of the technologies.  All flow junctions of segregated streams
are identified at this stage.  Any redundant treatment unit processes are
eliminated and appropriate ancillary processes (e.g., secondary clarification
after activated sludge) are inserted.

         b.   Specified Unit Process Train (SUPT) Mode

         In the SUPT mode, the user specifies the treatment train to be used,
activating the program HIDNSEQ.  Like the SEQUENCE program, HIDNSEQ inserts
appropriate ancillary technologies and tracks merge points (flow junctions) as
streams are comingled.  In addition, HIDNSEQ allows the operator to specify
key design parameters for any or all of the technologies included in the
overall design.

    2.    Subsequent Steps for Both Modes

         Once the skeletal treatment train has been developed in either the
Model Selection or SUPT mode, the control program RWLCALC calculates raw waste
loads for segregated and combined waste streams.   Where streams are combined,
RWLCALC calculates a dampened combined variability at the merge point from the
variability data for the individual streams.

         To this point in a run, the control programs have primarily combined
file data with user input directives to generate a generalized treatment train
that treats the specific pollutants in the waste streams.  The next program,
TRTCAT, coordinates the detailed design of the system through the use of the
treatment technology program modules and two auxiliary programs, RESEQUENCE
and COMPARE.

         TRTCAT starts the actual design by calling the appropriate treatment
technology module to design the most upstream unit process in the generalized
treatment train.  If the constituents in the stream(s) to be treated violate
the acceptable influent quality specifications for that technology, RESEQUENCE
inserts appropriate pretreatment.  Once the pollutant concentration and
variability meet the influent quality specifications for the unit process, the
treatment technology program sizes the unit and develops cost and scale
                                   K-ll

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    factors.  Additionally, the program calculates the pollutant reductions
    achieved by the unit process.  Using the waste load data for the treated
    stream, TRTCAT then designs the next downstream unit process.

             Iteration continues until all unit processes (and protective
    pretreatment, as needed) in the generalized tredtment train have been
    designed.  If, however, all effluent targets are met before all the unit
    processes specified have been designed, the COMPARE program stops adding
    further treatment, and TRTCAT transfers all design and cost data files to the
    COSTS program.  If the user has chosen to design and estimate costs for
    appropriate treatment sludge handling p*ocesses, the BYPROD program will be
    executed before COSTS.  BYPROD is analogous to a combination of the Parameter
    and Treatment Selection File and SELECT, SEQUENCE, and TRTCAT, except that it
    treats the wastewater treatment sludges rather than the wastewater.  The
    BYPRODUCT-SUPT program operates on sludges and is analogous to the SUPT mode
    for wastewater treatment.  Since BYPROD-SUPT was never used during the OCPSF
    study, it is not depicted in Figure VIII-1.

             COSTS is the control program for estimating the treatment systems
    costs.  It calculates individual unit process capital costs from their
    respective cost and scale factors combined with the Capital Costs File data.
    The method for calculating operating costs is contained in the Operating Costs
    File.  Because entire lime requirements for a treatment system cannot be
    determined until the total system is designed, the COSTS program itself
    designs a central lime handling facility and calculates its costs.  COSTS then
    calculates the miscellaneous costs, such as piping, and adds them into the
    overall capital cost of the facility.

             One final control program is an available option.  In OCPSF
    facilities, one product line may contribute disproportionately to treatment
    costs.  The ALLOC program can allocate both effluents loadings and costs back
    to the responsible product/processes.

             More complete documentation of this Model is in Appendix L of EPA's
    November 16, 1981, Contractors Engineering Report - Analysis of Organic
    Chemicals and Plastics,/Synthetic Fibers Industries.
U S. Environmental Protection Agency
Region 5, Library (PL-12J)
77 West Jackson Boulevard, IZtti rwoi
Chicago,  IL  60604-3590
                                        K-12

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