vvEPA
          United States
          Environmental Protection
          Agency
           industrial Environmental Research  EPA^-BCMWa


                  Park NC 27711    6 . 2>
          Research and Development
Treatability Studies of
Pesticide Manufacturing
Waste waters: Carbaryl

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                  RESEARCH REPORTING SERIES

  gories were   tabfe^t                    SeneS' Jhese nine bro^ en-
                                 rthc
  vironmental technology  eton  5 ?«J7   ?     3   application of en-
  planned to foster technology transfer  °fHtrad'tlOnal 9rouPin9 was consciously
  The nine series are:      9V       3nd * maxtmum inte--face in related fields
     1. Environmental Health Effects Research
     2. Environmental Protection Technology
     3. Ecological Research
     4. Environmental Monitoring
     5. Socioeconomic Environmental Studies
     6.  Scientific and Technical Assessment Reports (STAR)
    7.  Interagency Energy-Environment Research and Development
    8.  "Special" Reports
    9. Miscellaneous Reports


=rrn^~^
o. PoNution sources ^^J^SS^ *""
                     EPA REVIEW NOTICE



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                                     EPA-600/2-80-077a

                                                April 1980
    TreatabilitV Studies of Pesticide
Manufacturing  Wastewaters-.  Carbaryl
                             by

                   Edward Monnig. M'«Jael Murphy.
                    Ruth Zweidinger, and Linda Little

                      Research Triangle Institute
                         P.O. Box12l94
                Research Triangle Park, North Carolina 27709


                       Contract No. 68-02-3688
                          Task No. 109
                      Program Element No. 1BB610



                   EPA Project Officer. David C. Sanchez
                     Research Triangle Park,
          Prepared for

u S ENVIRONMENTAL PROTECTION AGENCY
   Slice of Research and Development
       Washington, DC 20460
    US Environmental Protection
    Region V, Library
    230 South Dearborn Sir
    Chicago, Illinois  60604
                                          n

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U,S- Environmental Protection Agency

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                                  ABSTRACT
     !„ February 1979 Research Triangle Institute (RTI)  was requested by
the industrial Environmental Research Laboratory, Research Triangle Park
(IERX-RTP) of the U. S.  Environmental Protection Agency (EPA) to conduct
Moratory and pilot studies of the treatability of pesticides manu ,c-
turing wastewaters.  The project is designed to investigate  the su.tabi-
U«, !f  individual pesticide manufacturing vastewaters  for discharge  to
biological treatment systems,  whether publicly o»ned  treatment works
 (POTW) or on-site  systems.
     The approach  taken with each  pesticide manufacturing vaste»ater
 prioritised that is,  less costly,  more available methods of treatment
 are investigated first.  Tie preferred method  of treatment „ assume  to
    b logic 1 treatment.  If the pesticide is  Judged suitable to hiolog,-
 Cl treatment, a Judgement based on chemical and toiicoKgical evaluate
 of the vaste before and after treatment, additional options were not
               tbe results of the bench scale experimental work involved
 in this study, both carbaryl manufacturing .abater  *- -^™
 part in nine parts municipal waste»ater, and carbaryl itself, when
  rrr,rrr
  of t ese p Lameters include combined hydrolysis  and biodegradation of
           and -apbthol,  volatilation of toluene and biodegradat.on of
         ir
   from the biological units treating carbaryl manufacturing wastewater
                                    ii

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 Because tne technoloov  r\f r,,-«-	                                  "

31, 1979.                                           3S ""Pted as of May
                                     ill

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                               TABLE OF CONTENTS

                                                                      Page
Section                                                                . .
-                                                             •  •  •  •
          Abstract

   1      INTRODUCTION ...................... '     ^

   2      CONCLUSION AND RECOMMENDATIONS  ........ .......


   3      CARBARYL  .  ....................  '.'.'.'.    3
            Chemical  Information  ...............     _    5

            Manufacture ......... . ............. .    5
            Current Waste Disposal  Practice.  .  . . ........   ^    5

            Ecological Effects  .........  .....  '....'.    6
            Environmental Fate  .................        7
            Health Effects  .....................

    4      TREATABILITY  STUDIES  ......  -  •  •  •  ;  ; '  ......
             Characterization of Wastewater  from Carbaryl    .....     g

               Manufacture ....................         9
             Biological  Treatability Studies.  .  .  -  -  - -  ......
             Effect of Biologically Treated  Carbaryl Waste-             ^
               water on Algae, Fish and Daphnia ........ •  •  •    Jg

             Conclusions ..................

 REFERENCES ......... .................


 AP™nalytical Procedure for Determination  of Carbaryl^and^  ^ ^   ^

      a-Naphthol   .....................


 AP™nalytical Procedures  for Routine  Wastewater  Characterization .   23



 APPTrocedures  for  Conducting Activated Sludge  Treatability     ^   ^

       Tests ...... ....................

  APPENDIX D                                                  .....   26
       Procedures  for Algal  Assay Tests ..........

  APPENDIX E                                                   .  ...    28
       Procedures for Fish Bioassay Tests ........   • •


  AMIS2hod for Carbaryl Analysis as Reported by Hathaway .....    30


              for the Analysis of Carbaryl as Developed by ......    ^

       Union Carbide .....................
                                       iv

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                                LIST OF FIGURES




                                        f°r  Carbaryl

                                                  Activaed
  3       Influent  and Effluent COD Values 'for ' Control ..........  10
             Activated Sludge Units .          Control
          Pesticide Reduction in Activated "sludge Units  Fed  .......  "
             Municipal Sewage Spiked to 10 mg/1 with Carbarvl
C 1       Diagram of Swisher Bench  Scale ActfvateTsiudge JnxV ! ! .'  .'  .'  25

                                LIST OF TABLES
Table

   1       Ecological Effects  Testing of Carbaryl

            Sample". Cha"'te"Zati0n °f th£ Composiiei Carbaryl .....   '

  3       Toluene Concen^ations'in Va^iou^ FracUon^ of .........   9
            Carbaryl  Wastewater

  5      sss s  fig c                 '
            and-                        Wastewatr
            and
                            Treated
                    .                     «-ufacturing

8      Effect
               on Fish Survival  of carbaryi Manufacturing  .......   1?
  9      Effect    rerAiXed 10%  With Municipal Wastewatef  .              17
         Effect on Fish Survival  of Carbaryl Manufacturing  .......    ?

           IS^SifS-ffi  with Municipal w— « -
 10      Effect on Daphnia  Survival of Ammonia  Stripping of .......   1?
           Effluent Samples  from Carbaryl Test Units
                                                    .........   lo

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                                  SECTION I
                                INTRODUCTION
     In February 1979 Research Triangle Institute (RTI)  was requested by the
Industrial Environmental Research Laboratory, Research Triangle Park (IERL-
RTP) of the U.S. Environmental Protection Agency (EPA) to conduct laboratory
and pilot studies of the treatability of pesticides manufacturing waste-
waters.  The project is designed to investigate the suitability of individual
pesticide manufacturing wastewaters for discharge to biological treatment
systems, whether publicly owned treatment works (POTW) or on-site systems.
     The approach taken with each pesticide manufacturing wastewater is
prioritized, that is, less costly, more available methods of
treatment are  investigated first.  The preferred method of treatment is
assumed to  be  biological treatment.   If  the  pesticide is judged suitable to
biological  treatment, a judgment based on chemical  and  toxicological evalua-
tion of the waste before and  after treatment,  additional options  are not
investigated.
      If pesticide manufacturing wastewater disrupts biological treatment
 systems, the possibility  of pretreating  the waste  prior to biological  treat-
 ment is investigated.   Pretreatment  options may include pH adjustments,
 filtration, flocculation,  oxidation  and  others depending on the nature of
 the waste and its chemical composition.
      If pretreatment does not make the waste compatible with activated
 sludge systems, adsorption techniques may be investigated.  These may in-
 clude both  carbon and resin systems.  The necessity for physical-chemical
 treatment  of wastewaters will again be evaluated as with the biological
 treatment  system.
      This  report details a study of  the  treatability of a wastestream  re-
 sulting from  the manufacture of carbaryl, a product of the Union Carbide
 Corporation manufactured at their Institute, West  Virginia plant.

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                                    SECTION 2
                         CONCLUSION AND RECOMMENDATIONS
       Based  on  the  results  of  the  bench  scale experimental work  involved  in
  thxs  study,  both carbaryl  manufacturing wastewater, when mixed  one part  in
  nine  parts  municipal wastewater,  and carbaryl itself, when spiked at 10 mg/L
  xn municipal wastewater, appear suitable for biological treatment by accli-
  mated systems  if additional provision is made for removing ammonia in the
  effluents from these biological treatment systems.  Other parameters investi-
  gated in this study including carbaryl, a-naphthol, and toluene concentrations
  and the chemical oxygen demand (COD) all showed large reductions (90% or
  greater).  The mechanisms of reduction of these parameters include combined
 hydrolysis and biodegradation of carbaryl and a-naphthol,  volatilization of
 toluene and biodegradation of species  contributing to COD.
      A large increase in ammonia concentration  was noted in the  effluent
 from  the biological treatment  units  relative to  their influent.   This ammonia
 concentration made  the  toxicological evaluation  of the effectiveness of
 treatment problematic by rendering the effluent  more  toxic than  the influent
 Ammonia  stripping lessened  this  toxicity.  Because the technology of nitrogen
 control  has  been extensively developed,  these treatment  options  were not
 pursued  further.
     The  carbaryl manufacturing wastestream  investigated in this study is
 presently mixed with other manufacturing wastestreams  and treated in a
 manufacturer-operated aerated lagoon with approximately a 3-day  retention
 time.   Based on the study detailed below, this treatment process should
provide an adequate treatment of the carbaryl manufacturing wastestream
provided there is no interference from the components of other wastestreams
and provided nitrification of ammonia occurs.

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                                  SECTION  3

                                  CARBARYL
CHEMICAL INFORMATION
CAS No.:  63-25-2
Category:

Synonyms:
 Structure:
           carbamate

           Arylam, Atoxan, Caprolin, Carbaryl (DOT), Carbatox,
           Carbatox-60, Carbatox-75, Capolin, Compound 7744,
           Crag  sevin, Denapon, Dicarbam, ENT 23, 969, Gamonil,
           Germain's, Hexavin, Karbaryl, Karbatox, Karbosep,
           Septene,  Sevidol,  SDK, Tricarnam, and others.
            (Fairchild, 1977).

                     0-CO-NH-CH
 Properties:

 M.W.      201.24
  1971).
PH
7.0
8.0
9.0
10.0
Carbaryl
half-life
10.5 days
1.8 days
2.5 hours
15 min.

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Cl,
     NaOH
1
Hyd
PI
J
( H2° Naphthalene 0
I 1 1
rogen tt ^ Tetralin Tet
ant 2 Unit Ur
	
-
CO H. ' ,
J
.ralol
lit

Ve
t
nt
\

*1 Condenser |

v-
r
INaphthol
Unit

Phosgene
Unit


V
>

2 	 , Lt

\
' >
f
— 9
oformate
nit

	 » Carharyl
Unit

rcnt* 	 Dust >
°nt* Collector < Pack
)
Proc

Jging
r
hict



H2°

->Vent-
— NaCl-
^
NaCl




	 »
*
2



>
Secoi
Wa
Trea
P1;

Flare
N t
Heavy Re
From Pro
Solvent
Son
idary
ste
tment
int-
                                                                                             •* Incinerator
                  FiRure  1.   Production and  Waste  Schematic for Carbaryl (Sittig, 1977)

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Application:
Wide spectrun, insecticide for control of insects on cotton, vegetables,
fruits, rice, sugarcanes and ornamentals; used in agriculture, homes, anx-
mals, forests.  Registered, 1959.
MANUFACTURE
     Figure  1 presents a generalized production and waste  schematic  for
carbaryl manufacture.
CURRENT WASTE DISPOSAL PRACTICE
      Carbaryl manufacturing wastewater is  presently  combined with the  efflu-
 ent of other manufacturing processes at the Institute,  West Virginia plant
 and treated in  a system of aerated lagoons.  This system consists of 3
 aerated treatment basins run in parallel.   Retention time of the entxre
 system is reported to be approximately three days (plant engineer, personal
 communication).
      The major  carbaryl-containlng wastestream is a  continuous decantatxon
 stream generated during a solvent recovery step in the carbaryl production
 unit   This stream was sampled for this study.  Other carbaryl inputs  to the
 waste  treatment systems include wash down from packing and cleaning procedures
 which  is intermittent in nature and was not sampled.
       Carbaryl  has  apparently been detected in a  sample of the effluent  from
  Union Carbide's waste  treatment units at  the  Institute plant.  Carbaryl
  concentration  in a sample taken on 4/11/78 was found to be 260 Mg/L (Hatha-

  Way' Tpossible interference in some methods of analysis for carbaryl should
  be noted.  Routine in-plant analyses by Union Carbide personnel of products
  vastestreams known to be free of carbaryl have shown a compound which elutes
  at a  similar retention time as carbaryl under the conditions for carbaryl
  analysis.  This compound has not been identified, though  it  resists hydrolys.s
  at high PH which  is not  characteristic of  carbaryl.   The  method  of analysis
  for  carbaryl used by Union  Carbide and the method used by Hathaway (1979)
  are  described  in  Appendices F  and  G.
  ECOLOGICAL EFFECTS
        Table 1  surcmarizes  the published ecological effects data for carbaryl.

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         TABLE 1.  ECOLOGICAL EFFECTS TESTING OF CARBARYL
Species          Duration       Result (LC  a)
                                                                 Reference
Stone fly.
Pteronarcys
californica

Daphnia pulex


Brown trout

Gammarus lacustris


Fathead minnow

Bluegill

Daphnia magna


Gobio gobio


Red crawfish

Fathead minnow
Fathead minnow
— 	 	 — 	 , — _
48 hr

48 hr

48 hr

48 hr

96 hr

96 hr

48 hr

96 hr

48 hr

96 hr
Life cycle
	 	 ou

1.3 mg/L

6.4 mg/L

1500 mg/L

22 mg/L

12 mg/L

5.3 mg/L

0.1 mg/L

1.0 mg/L

3.0 mg/L

9.0 mg/L
0.21 to 0.68 mg/]

' • 	 — 	 	 — —
Bond and Straub,
1973
Bond and Straub,
1973
Bond and Straub,
1973
Bond and Straub,
1973
Surber and Taft,
1962
Surber and Taft,
1962
Ilisescu and
Stefanescu, 1974
Ilisescu and
Stefanescu, 1974
Muncy and Oliver,
1963
Carlson, 1971
- Carlson. 1Q71
 3LC50-Concentration to kill 50% of a test population in the specified time

ENVIRONMENTAL FATE

     Half life of carbaryl in soil is dependent on numerous variables.
Bollag and Lui (1972) state that a generally accepted half life of carbaryl
in the soil is one week though others have shown stability in soil from 25
to 60 days before appreciable decay (Caro, Freeman and Turner,  1974).
Bollag and Lui isolated fungi which were able to alter carbaryl by sidechain
and ring hydroxylation.  or-Naphthol was  shown to be more readily degraded by

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the marine fungi and bacteria studied than carbaryl (SiKKa,  «iyazaki  and
      ts           to separate the relative contribution .f chemical and
biological hydrolysis to the degradation of carbary!.  Paris et .1 .  O975),
report that bacterial removal or carbaryl was dependent upon the rate of
chemica! hydrous of carbary!.  These authors also report that no sorpion
of carbaryl to microorganism was found in their studies, though  thers have,
reported  rapid sorption to  saline sediments  (Karinen et .1., 1967).

HEALTH EFFECTS
      An  extensive review  of the toxicological  literature  on carbaryl  is
 contained in the vo!ume:   Dr^n^WaterjniJieaUh (NRC, 1977).  Ih. NHC
 report classified the toxicity of carbaryl as  moderate (1^ for  male rats
 500 mg/kg; no effect for man at 0.13 mg/kg for 6 «eeks).   Carbaryl  vas not
 fold to"e either mutagenic, teratogenic, or carcinogenic after extens.ve
 testing.  The Mrak Commission IMC, 1977)  concluded that  c.rbaryl was one
 of but three pesticides Judged "not positive for carcinogenicity  by appropriate
 tests in more than one species of test animals".  The  SEC report  also concludes,
 "In general, metabolism of carbaryl and the appearance of metabolites in water
 syste«s would create no significant hazard in addition to that of carbaryl
 itself".

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                                     SECTION 4

                               TREATABILITY STUDIES
CHARACTER™* or WASTEWATER FROM CARBARYL
                                               MANUFACTURE
  tive dys.
  t^e days during a normal winter operation perlod.  „„ rate
  t»  ays of sa»pling.  Plant personnel estiMted the flou             "
  -P Ung to be approximately 6-7 gpm and flow rate oo day 2 to be approxi-

               "   PeS
             .
         values according  to plant personnel
           s
 run on this composited sample.

 as anaT
                                                                      ^ -ate
                  -ult  was  noted in the deter«ination of tot.l  dissolved
        HW).   The .etnod  for  the determination  of  TDS retires  vacuim
 f,l.r.t1M  of  the saBple through  . 0:«  „ filter (Millipore HA).  After
 fUtration  of  the carbaryl waste  and  subsequent  drying at  105= an oily
 rescue „. noted in the filtered sample  that resisted  further dessication.
 Thls rescue »as not noted during the dessication of the who!e unfiitered
 sample   This ,rtlf.ct may arise ^ „ lnteraction ^^           «*

 h  was estrea. ,„„ the filter itse!f.  The implication of these results on
the conduct of the algal  assay will be discussed below.

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                    t,
 TABLE 2.  WASTEWATER
         =====
          Parameter  (units)
OF THE COMPOSITED CARBARYL SAMPLE
                     Value
   pH
   Cl"  (mg/L)
   Alkalinity  (mg/L as CaC03 to pH 4:5)
   Total kjeldhal nitrogen (mg/L as N)
   NH,-N (mg/L as N)
      4
    NO  + N03 (mg/L as N)
    COD  (mg/L)
    Total solids  (mg/L)
    Total dissolved solids,  (mg/L)
    Settleable  solids (mg/L)
    Carbaryl (mg/10
    Toluene (mg/L)
                       8.2
                       120
                       385
                       1100
                        158
                        5.2
                       4100
                        100
                          75
                       Trace
                        4.3
                         160
BIOLOGICAL TREATABILITY STUDIES
                                                 °!  (v/v) with municipal
 diluted settled ..nicipal »aste«ater

 units vas maintained at a
 Mixed liquor volatile Su£pended .olids OU-VS ,                           o_




  MLVSS quantity a the test «t.  »                      ^ ,wrMiBately
  value of 3100 mg/1 on day 14.  F/M ratios at
  ... d,/1 »ased on influent COD values
                         "-


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700
                                ©
®-
                                                                                          ®
                                                        ®
                                                                                G> Influent COD




                                                                                •  Unit#1 Effluent COD
                                                                        	A  Unit #2 Effluent COD
               Figure 2.  Influent and Rrfluent COD ValuPs  for T^,  A^,..__ ,	

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500
          Influent COD
          Unit #1 Effluent COD
*.	-*  Unit #2 Effluent COD
                   Mgurc 3.  ,n.l«nt an, «fl«ent COD Value,  for Control Actlv-fd  Slud.e  UnHs.

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      the test un,ts.  on day 12  lt had been noted ^
   >n both test unit reactors had dropped belw 1         Air        *  >    s
   units was doubled on day „ £r- 2W) ^                           the test
       flow, coupled with the gradual increase  in
   -rease ln COD renoval.                                          d    tlc
                         .              on COD rcduction
   -fluent .verain  595 rag/L and fttlmt
       Analysi, for carbaryl an  a.naphthol revealed
    e c  taryl nanufacturing Msteuater  cMposite ^     had        e  1   „
        was  determined to be 0.06 mg/L instead of  th
                                Illg/-L lnstead of  the expected 0.10 me/L
       Straight iajection of aqueous effluent  sables by the method presented
        : r;;tre:eaied  n° carbaryi °r — — - «- -«•«» •  -
                    "
   h or    a                           '          - °  •«*« -itb -thylene
  chloride  nd concentration of the extract likewise revealed no carbaryl „

            "  "1"6"1                                     "-overy of
        s        th: possibu roie °                      «"   "»^>
      ,  sludge samples from the test units and control units were extracted
 Pw:: rhyieM chioride -d -^ *- -^ - »-— -  -    1
 proble     „ encountered  Bith an ^^^ EMpies duri^ ^ ^
 step.   FUtration through  glass »ool followed  by fiUration through phase-
   p.ra.ngfiHer paper aneviatea some  of these problems.   Hoover, recovery
 •f carbaryl spiked at  levels of 2 ,ne/L in municipal sludge  was only 3»
     Because of  incomplete resolution of  other compounds  in  sludge with
        ei0n
                                                                  ogr
              used, an absolute determination of carbaryl ievels was not
possible.   Carbaryl concentration was no greater than 0.01 mg/L in sludge in
the t«t units.  Given the influent and effluent levels of c.rbaryl>  tnis
concentration  in the sludges wouid not represent any sorptive accumulation.
"-Naphthol was not detected in  any of the sanples
                                    12

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     To test the possible role of air stripping in the removal  of  volatile
organic an air stripping control (ASC) unit .as run.   Composite carbaryl
.aste.ater was nixed 10% in deionized vater (DIW) and pumped through an
activated sludge unit vhich contained only DIW.  An eight hour retention
time and an air flo. of 400 .I/I. .as maintained in the ASC umt.  COD
measurements .ere taken of the influent and effluent to the ASC units over a
t.o day period.  No difference .as measured in the influent or effluent
values  (420 mg/L for both  influent and effluent).  This value corresponds to
that expected  of a  10% diiution  of the composite  carbaryl waste
     Toluene  analyses  .ere performed on both  the  influent and effluent  of
 the  biological treatment units and air stripping  controls by the  purge  and
 trap method (Bellar and  lichtenberg, 1974;  Bellar, Uchtenberg  and  Eicb.1-
 berger  1976).  Analysis of data provided in Table 3  sho.s  that only m.nrmal
 handling of carbaryl .aste .iU  cause a substantial  reduction in toluene
 concentration.  The routine handling retired to dilute sables and the
 subsequent exposure of samples to the open air during the pumplng of in    nt
 over a 24 hour period is sufficient to reduce toluene concentrate by 85
 95 percent.   Additional reduction in toluene concentration occured after
 passage through a  S.isher unit.  It .ill be  noted that this reduction  »
 toluene concentration does not  effect the  COD determination.  The  d.chro.ate
 digestion involved in COD measurement provides  only  minimal oxidate  of
 aromatic  compounds.
       To more adequately test the biodegradation of  carbaryl, a  .erxe.  of
  tests were run on municipa!  »aste.ater spiked at a  concentration of 10 mg/L
  .ith technica! grade carbaryl.   Three activated sludge units  (test units)
  .ere fed settled municipal .aste.ater diluted .ith carbaryl saturate  de-
  ionized .ater to give a final emulated carbaryl concentrate o   00m
  compared .ith a carbaryl concentration of 4.3 mg/L in the composited  carbary!
  .aste.ater sample.  Three activated sludge  units (control units  .ere  e
  .ith municipal .aste.ater diluted  .ith a  corresponding amount of  unsp.ked
  DIW.  He. influent .as mixed every 48 hours.
        Immediately upon  mixing of test unit influent  an .Uquot »•««*'»
   for  carbary! .naXysi..   Ali,uots .ere  filtered through .  0.45M  MilUpore  HA
   filter.   Anaayses of influent  over the period of the study  sho.ed that
   carbary! !e,els  averaged 7.3 «g/L.  Analyses of influent  after its 48 hour
                                         13

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          Biological treatment units (10% carbaryl
          waste in municipal waste)
               Influent
               Effluent
          Air stripping control units (10% carbaryl
          waste in deionized water)
               Influent
               Effluent
2.5
0.001
   shelf  life"  showed  that  carbaryl  levels averaged 7.0 mg/L.  The difference
 between the 10 mg/L  spiked  levels  and the 7.3 mg/L analyzed levels probably
 represents sorbtion  of carbaryl to influent solids and its loss during the
 filtration of samples prior to analysis by HPLC.
      MLVSS levels were maintained between 1740 and 2300 mg/L.   0 85g/L of
 NaHC03 was added to  influent samples to maintain the PH in the units from
 7-3 to 7.65.   Residence time in the units was 8 hours.   Dissolved oxygen was
      Figure 4 presents data on percentage reduction in carbaryl  concen-
 tration over time in the test units.   From day 7  on reduction  was  complete
 except for a period  around day 15  when aeration difficulties were  experi-
 enced in one unit.   During the same period the COD  reduction in  the  test
 units averaged  83%,  with the  influent  averaging 227 mg/L and the effluent
 averaging 39 mg/L (range 24 to 60).  The  COD reduction  in test units was 84%
 with  the  influent averaging 230 and the effluent  averaging 37  (range 28 to
 48).
      As these data indicate, carbaryl  is  readily  degraded in activated
 sludge systems after a short acclimation period.
EFFECT OF BIOLOGICALLY TREATED CARBARYL WASTEWATER ON ALGAE,  FISH AND DAPHNIA
     Algal assays were conducted in accord with the procedures  outlined in
                                      14

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Figure 4.  Pesticide Reduction in Activated Sludge Units Fed
      Municipal Sewage Spiked to 10 n,g/l with Carbaryl

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  EPA manual:   The  Selenastrum  Capricornutuni  Printz  Algal Assay  Bottle J^st
  and described in  Appendix D.  Samples were  vacuum-filter  sterilized through
  a  0.45  (J  filter.
      Table 4  presents the results of an algal assay on the untreated carbaryl
  manufacturing wastewater.  The data on algal growth in test flasks are
  presented in  terms of percent of the growth in the control flasks on day 14
  of  the  test.   As  can be seen in Table 4 the algal EC^ (concentration effective
  in  reducing growth to 50% of controls) for carbaryl wastewater lies between
  0.01 and 0.1 mL per liter.
      When mixed 10% with municipal wastewater, the toxicity to algae de-
  creased remarkably.  As shown in Table 5 the EC5Q for influent to the AS
 units was approximately 1000 mL/L.   On the other hand the effluent from the
 AS units showed an increased toxicity over the influent.   As  shown in Table 6,
 the EC5Q for the effluent samples was between 100 and 320 mL/L.
      A similar pattern was exhibited by  the  fish bioassay using fathead
 minnows.  The bioassay procedure  is  described in Appendix  E.   As  shown  in
 Table 7, the  LC5Q  (concentration  lethal  to 50% of the  test population)  of
 carbaryl wastewater was  approximately 100  mL/L.   Table 8  shows  the LC    of
 the influent  to the test units was between 320  and  1000 mL/L.   The LC    of
 the effluent  from  the  AS units as shown  in Table  9  was between  100 and°320
 mL/L (Table 9).
      It  was hypothesized that  the conversion  of  organic nitrogen  to ammonia
 by  biologically mediated processes in the  treatment units  caused  an increase
 in  the toxicity of the effluent from the AS unit.  The ammonia  levels in-
 creased  from 30 mg/L in  the influent to 110 mg/L  in the effluent.
      To  test the biological significance of this  ammonia concentration an
 additional bioassay was  conducted comparing ammonia stripped samples with
 unmanipulated  samples.   To strip the test unit effluent of ammonia, the
 sample pH was  raised from 7.2 to 14.   Samples were aerated for 2 hours and
 pH readjusted  to 7.  Due to sample volume limitations  this bioassay was
 conducted with Daphnia pulex.  The results of this bioassay are presented in
Table 10.  As  can be seen, the toxicity of the ammonia stripped effluent was
 less than that of the unmanipulated sample effluent or the influent.   It
 could, of course, be argued that  the  stripping process may have removed some
other volatile, toxic  component of the effluent.   However,  these samples
                                      16

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    TABLE 4.   EFFECT ON ALGAL GROWTH OF CARBARYL MANUFACTURING WASTEWATER
Carbaryl wastewater (mL/L)
Growth (% of control on day 14)
         TABLE 5.  EFFECT ON ALGAL GROWH OF CARBARYL MANUFACTURING
               WASTEWATER MIXED 10% WITH MUNICIPAL WASTEWATER
Carbaryl wastewater  (mL/L)
Growth  (%  of  control on day  14)
     TAB!* 6.   EFFECT ON ALGAL GROWH OF'  CARBARYL MANUFACmiNG WASTEWATER
         MIXED in Mli miSpALWASTEWATER AND BIOLOGICALLY TREATED
 Carbaryl wastewater (mL/L)
 Growth (% of control on day 14)
    TABLE 7.  EFFECT ON FISH SURVIVAL OF CARBARYL MANUFACTURING WASTEWATER
 Carbaryl wastewater (mL/L)
 Fish surviving 96 hr (%)
    TABLE 8.  EFFECT ON FISH SURVIVAL OF CARBARV1 MANUFACTOJNG WASTEWATER
                     MIXED  10% WITH MUNICIPAL WASTEWATER
  Carbaryl  wastewater, mL/L
  Fish surviving 96  hr (%)
     TABLE 9.   EFFECT ON FISH SURVIVIAL OF CARBARYL t^FACTURING WASTEWATER
WASTEWATER ASD BIOLOGICALLY TREATED
  Carbaryl wastewater, mL/L
  Fish surviving 96 hr (%)
  ~"   = —    ""-	
  aTest population, 10 fish per concentration.
                                         17

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                               -_	^           tinuent        Influent
                           f^^tr^edunmanipulated    uiunanipul.ted
                                               "	—•	_	
  Survival of Daphnia at
  had previously  been  subjected to , hours of air stripping under neutral p«
  cond^ons during p.sssge through  an AS  unit.  This aeration would  elininate

   :::CL   L" crunds which d°not sh°-a —«"<->< ->—hiP
  characteristic of ammonia.
  CONCLUSIONS

      Based on the initial examination involved in this study, carbaryl
  manufacturing w.t«.t« and  carbary! appear suitab!e for biological  treat-
 ment by acclimated systems  if addition provision is made for ammonia
  reduction.   The  production  of a^onia in the digestion of this »aste  could
 prov.de toxicity problems if  some  form of a^onia removal is  not employed or
 »f  he effluent  is  not diluted substantially.   Because this technology is
 well established, extensive study in this area  Uas not undertaken   The
 reader is directed  to the EPA Technology Transfer Manual:  Process Design
 Manual  for Nitrof.n Control for further  information on these" systems
      The execution and interpretation of various  bioassays conducted on
 multi-component wastestreams,  particularly those  containing volatile compounds
 should  recognize certain sources  of uncertainty.  A primary concern  is the
 ma.ntenance of sample integrity through  the manipulations »hich are  a  part
 of many bioassay procedures.
     The filter sterilization  step  required by algal assays can be a particu-
 larly important,  especially  if done under a vacuum.   The loss  of volatile
 components  in the sample  during vacuum filtration is  an obvious result   In
•dditxon, the filter itself might provide active sites for the  chemical
formation of  compounds not found in the  unfiltered sample.  This possibility
                                    18

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was noted in conjunction with the discussion of the determination of dissolved
solids in carbaryl wastewater.
     The sorption of toxic components to particulate portions of samples and
their subsequent removal in the filtration step also provides a source of
interference.  This process could account for the reduction in toxicity to
algae of carbaryl wastewater mixed 10% in municipal wastewater.  This reduc-
tion in toxicity is greater than that expected by a simple 1:9 dilution.
     While  the fish or  daphnia bioassays require much less sample manipu-
lation than the algal assay,  the maintenance of sample integrity can  still
be a problem.  The  loss of volatile  compounds  over  the 96 hour test period
will  occur  as  the  samples are exposed to open  air.   It might be  argued  that
 this  loss  represents  an environmental reality;  the  volatile  components  of  a
 waste will  become less  available over time.  However,  as with  many  of the
 factors involved in biological testing,  the problem remains  one  of  adequate
 laboratory accounting of environmental  processes.
                                         19

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                             REFERENCES
                      t
2
3

      Sci. Technolo:926-3o  1976
                                    -w  "  \  Eichelber*e-  Determination
                                    "    " ^ G"  Ch*™^Ora.  Environ.
            ; 236:177°ld78S;
                                                «f Carbaryl by Soil Fungi.
             '  Voi
      Ohi   1973?
                                                        °f
                                       Treatment> CRC Press, Cleveland,
     Survival
     prolelas)   J
     promeiasj.  j.
                           °f i°n«-Tera ExP°su" to Carbaryl (Savin) on
                           ^"r^ °f the Fathead Minno«
                       Res.  Bd.  Canada.  29:583-587, 1971.
11 '
                   c

           i E' J' Ced°-  Agricultural Chemicals and Pesticides-  A
                 MOS\Re8if ry,?f IOX1C E""" °f CheMcal sSst.*
                 blication Ko. 77-180, National Institute for Occuna
  tional Safety and Health, Cincinnati, Ohio, 1977.               P
                                   20

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12.  Hathaway, J. L.   Compliance Evaluation and Wastewater Characterization:
     Union Carbide, Institute,  West Virginia,  EPA-303/2-79-014A,  U.S.  Environ-
     mental Protection Agency,  Denver,  Colorado, 1979.

13.  Ilisescu, A., and L.  Stefanescu.   Cercetari Privind Biodegradabilitatea
     si Toxicitatea unor Impuritati Existente  in Apele  Uzate Evacuate  de
     Industria Petrochimica (Research on the Biodegradability and Toxicity
     of Pollutants in Wastewaters Discharged by the Petrochemical Industry).
     Stud. Epurarea Apelor 16:76-98, 1974.

14.  Karinen, J. F.,  J. G. Lamberton, N. E. Stewart, and L. C. Terriere.
     Persistence of Carbaryl in the Marine  Estuarine Environment.  Chemical
     and Biological Stability in Aquarium Systems, J. Agric. Food Chem.,
     15(1):148-156, 1967.

15.  Matsumura, F.  Biological Effects of Toxic Pesticidal Contaminants  and
     Terminal Residues, pp. 525-548, in F.  Matsumura, G. M. Boush, and
     T. Misato, eds.   Environmental Toxicology of Pesticides.  Academic
     Press, N. Y., 1972.

16.  Miller, W. E., J. C.  Greene and T. Shiroyama.  The Selenastrum Capri-
     cornutum Printz Algal Assay Bottle Test,  EPA-600/9-78-018, U.S. Environ-
     mental Protection Agency, Corvallis, Oregon, 1978.

17.  Muncy, R. J.  and A. D. Oliver.  Toxicity of Ten Insecticides to Red
     Crawfish, Procambarus clarki  (Girard).  Trans. Amer. Fish. Soc.  92(4):
     428-431, 1963.

18.  National Research Council.  Drinking Water and Health.  National Academy
     of Sciences,  Washington, D. C., 1977.

19.  Paris, D. F., D. L. Lewis, J. T. Barnett,  Jr., and G. L. Baughman.
     Microbial Degradation and Accumulation of  Pesticides  in Aquatic Systems,
     EPA-660/3-75-007, U. S. Environmental Protection Agency, Corvallis,
     Oregon,  1975.

20.  Sikka, H.  C., S. Miyazaki, and R.  S. Lynch.  Degradation of Carbaryl
     and  1-Naphthol by Marine Microorganisms.   Bull. Envir. Contam. Toxicol.,
     13(6):666-672, 1975.

21.  Sittig,  M.   Pesticides Process Encyclopedia.   Noyes  Data Corporation,
     Park Ridge,  N. J., 1977, 524  pp.

22.  Sparacino,  C. M.  and J. W. Hines.  High  Performance  Liquid  Chromato-
     graphy  of  Carbamate  Pesticides.  J. of Chrom.  Sci.,  14:549-556,  1976.

23.  Surber,  E.  W. and R. A. Taft.  Water  Quality Criteria for Freshwater
     Fishes.  Proc. 16th  Annual  Conf.,  S.  E.  Assoc.  Game  and  Fish Comm.,
     Oct. 17,  1962.

24.  Swisher, R.  D.   Surfactant  Biodegradation.   Marcel Dekker,  Inc.  N. Y.,
     1970.
                                       21

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                                  APPENDIX A
       ANALYTICAL PROCEDURE FOR DETERMINATION OF CARBARYL AND a-NAPHTHOL

      The procedure for the analysis of carbaryl and a-naphthol was adapted
 from Sparacino and Hines (1976) and involves the separation and quantitation
 of compounds by high-performance liquid chromatography (HPLC)  with a reverse
 phase column and an ultraviolet absorption detection system.
      A modular liquid chromatographic  system was used for analyses.   The
 basic system consisted of  the  following components:   2 M6000 pumps  with an
 M660 solvent programmer and  a  U6K injector (Waters  Assoc.); Model  SF 770
 variable wavelength detector (Schoeffel Inst.).   A  reverse phase column,
 packed in our laboratory,  was  employed.  The  column  was packed  with  Partisil
 10  bonded with octadecyl trichlorosilane in  the  conventional manner.  The
 mobile phase consisted  of  acetonitrile  mixed  40% in  distilled water.  A
 wavelength of 222 nm was used  for  the detection  of both carbaryl and a-naphthol.
 Flow  rate of mobile phase was  2 mL/min.  Sample  injection size was either  10 ML
 or  100  ML.   Samples were directly  analyzed by HPLC.  Separate calibration  curves
 were  run  for  each injection size.  Detection limit of the system at these
 conditions was 0.5 nanograms carbaryl and  1.0 nanograms of a-naphthol.  Standard
 deviation of  carbaryl determination at 0.25 mg/L was 5.6% and at 1.0 mg/L was 7.5<
     All samples were filtered  through a 0.45 p Millipore HA filter prior to
analysis.
                                    22

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                                 APPENDIX B
        ANALYTICAL PROCEDURES FOR ROUTINE WASTEWATER CHARACTERIZATION

     Routine wastewater analyses were conducted according to Standard Methods
for the Examination of Water and Wastewater, 14th Edition, (APHA, AWWA,
WPCF, 1976).
pH-
     pH was determined electrometrically by Method 424.
Chloride—
     Chloride was measured by the mercuric nitrate method (Method 408 B)
Acidity—
     Acidity, as CaCO~, was determined by Method 402.
Alkalinity—
     Alkalinity, as CaCO«, was determined by Method 403.
Nitrogen Forms—
     Total Kjeldahl nitrogen was determined after digestion, according to
Method 421.  Ammonia  (NH.-N) was determined by an acidimetric method as
described in Sections 418 A and 418 D.  Nitrite and nitrate nitrogen (N02~N,
NO--N) were determined by the Devarda's alloy method  (419 F).
COD—
     Chemical oxygen  demand  (COD) was determined by Method 508.
Residues—
     Suspended  solids  (SS) were determined  by Method  208  D.  Total solids
 (TS) were determined  by Method  208 A.  Total dissolved solids  (TDS)  were
determined  by Method  208 A.   Settleable  solids were determined by Method
208 F.
                                       23

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                                    APPENDIX  C
           PROCEDURES FOR CONDUCTING ACTIVATED  SLUDGE  TREATABILITY  TESTS

      For biological  treatability  studies  the bench  scale,  complete-mix,  con-
 tinuous-feed,  activated  sludge unit designed by Swisher  (1970) was employed
 (Figure  C-l).   This  unit has  an aerator capacity of 0.3  L  and a settler
 capacity of  0.075  L.   The unit is made entirely of  glass,  avoiding the
 possibility  of contamination  by organics  leaching from the container.
 Continuous feed to the units  was  supplied through Teflon tubing by a peris-
 taltic pump  to give  the  nominal retention time of 8 hours.
      The units were  started with activated sludge from the Hope Valley
 Treatment Plant, Durham,  NC , which  treats municipal wastewater.  The units
 were  then fed  from a  reservoir of primary wastewater from the Chapel Hill
 Treatment Plant.   When a  steady-state condition was reached, as indicated
 by consistent  effluent quality in terms of COD and^mixed liquid suspended
 solids levels,  the feed to the test  units was spiked with pesticide waste-
 water.   Control units  were fed only  primary wastewater.
     The  pesticide spiked wastewaters were prepared by adding pesticide
 wastewater to  the primary municipal wastewater which had been allowed to
 settle for a 120 min to simulate primary settling.   Routine determinations
 were made of dissolved oxygen, pH, mixed liquor volatile suspended solids
 in the aerator and COD, and pesticides.   Dissolved oxygen was determined
with an  oxygen probe (Yellow Springs Instrument Co.).

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ro
                          INFLUENT
                      FEED
                   RESERVOIR
 EFFLUENT
COLLECTION
                                          AIR
                        Figure C-l.   Diagram of activated sludge pilot unit.

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                                  APPENDIX D
                       PROCEDURES FOR ALGAL ASSAY TESTS

      Algal bioassays were conducted according  to the  freshwater algal  assay
 procedure described in the report The Selenastrum Capricornutum Printz Algal
 Assay Bottle Test (Miller, Greene,  and Shiroyama,  1978).   The  test  alga was
 Selenastrum Capricornutum Printz,  obtained from  the National Eutrophication
 Research Program,  EPA,  Corvallis,  Oregon.   This  test  was designed to measure
 algal response  to changes in nutrient concentrations  and to determine  toxi-
 city  or  inhibition.
      Wastewaters  to be  tested were  filter  sterilized  through a  sterile
 prewashed membrane filter (Millipore  Filter, 0.45  [im  pore  size).  Serial
 dilutions were  then made  in sterile algal  media  to give the appropriate
 final concentration.  Sufficient  inoculum  was added to produce  an initial
 cell  concentration of 10   cells/mL.
      In  each  set  of experiments, algal  growth in the  presence of a series of
 concentrations  of  the wastewater added  to  the nutrient medium was compared
 to algal  growth in the nutrient medium  alone.  Growth was determined by
 direct counts of the algae during the  10-14 day incubation period.  Effect
 of the wastewater  on algal growth was determined in terms of the effect on
 the cell  yield.  Direct cell counts were performed by an automated procedure
 utilizing  a Fisher Scientific Model FO  16 particle counter.
      The  tests were conducted in water bath shakers at 24 ± 2° C and at approxi-
mately 80  oscillations per minute with constant white fluorescent lighting at
4300  lux.  Test containers were 250 mL Erlenmeyer Pyrex flasks containing 60 ml
of test medium and covered with an inverted Pyrex beaker.
     The method of expressing inhibitory or stimulatory effects was  that
recommended by Miller et al. (1978), i.e., as the percent growth inhibition
 (I) or stimulation (S), as compared to growth in a control  culture without
the test materials.  These authors suggest that,  in general practice,  the
results be based on the growth  at 14 days, i.e.,  as % I ^ or % S . at  a
given concentration of the effluent being tested.
                                        26

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     Decreased growth, compared to the control, is evidence of an inhibitory
effect.  The manner in which the test is conducted does not allow determina-
tion of whether this inhibition is temporary (algistatic) or permanent
(algicidal).  Such a determination would require further testing by subcultur-
ing into fresh medium free of the test material.
                                        27

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                                 APPENDIX E
                      PROCEDURE FOR FISH BIOASSAY TESTS

     The fish bioassay procedure chosen was the standard 96-hour static
bioassay (APHA, et al., 1976; Duke et al., 1977).  The static method has
been criticized as being rather simplistic, and more complex alternate
methods have been suggested.  However, the relative simplicity and economy
of the static method make it the method of choice in initial screening.  The
test fish was the fathead minnow, Pimephales promelas, selected from a list
of recommended species prepared by D. I. Mount of the National Water Quality
Laboratory (as reported in Cairns, 1969).  This species has been widely used
in fish bioassay studies and is adaptable to laboratory conditions.  Test
fish were obtained from Kurtz's Fish Hatchery, Elverson, PA.  New shipments
of fish were routinely exposed on arrival to the broad-spectrum antibiotic
tetracycline HC1 at a dose of about 13 mg per gallon of water for 24-48 hr.
This treatment helps prevent introduction into the stock tank of diseases
from fishery stock or from fish damaged in shipment.  On evidence of disease
in the stock tanks, the tetracycline treatment was repeated.  Fish were
maintained in 30-gal. glass aquaria equipped with aeration devices and
recirculating filtration.  The water was Durham tapwater which was passed
through a combined selective ion exchange and activated carbon system which
removes 99+% of the organics and ionics present in the water.  The water was
then reconstituted by the addition of 48 mg/L NaHCOg, 30 mg/L CaS04«2H20,
30 mg/L MgSO,, and 2 mg/L KC1.  The tanks were kept  in a room maintained at
24 ± 2° C, with a light cycle of 8-hr dark and 16-hr  light.
     Small-scale  laboratory bioassays were conducted  to determine  the  range
of concentration  to be tested in full-scale tests.   For these screening
tests  solutions were prepared as decimal  dilutions of the wastewater  (such
as 0.01, 0.1,  1.0 percent).  A test volume of  3  liters and  3  fish  per  con-
tainer was used.
                                      28

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     Based on results of the screening assays,  a full-scale  test  range was
chosen, with the concentrations falling between the highest  concentration at
which all fish or most of the fish died.  In these tests,  the LC5Q was
determined by testing a series of concentrations based on  progressive bisec-
tion of intervals of the logarithmic scale, such as 1.0,  1.8, 3.2, 5.6,  and
10.0 percent, multiplied as necessary by any power of 10.  These  values  are
evenly spaced when plotted on a logarithmic scale.
     In each test series, control tests were conducted concurrently with the
experimental dilution water.  In the large scale tests, results were con-
sidered invalid if more than 10% mortality occurred among the control fish.
In the large scale tests, test containers were 10-gallon glass aquaria
containing 15 liters of test solution.  To test each experimental concen-
tration,  10 fish were used.  Fish were not fed for 48 hr prior to testing
nor during the tests.
     Use  of 10 or more test fish per toxicant concentration has been the
"usual practice" for short-term static  tests according to Standard Methods
(APHA  et  al., 1976).  As noted in this  document,  "a number of factors govern
the precision of the results of a bioassay and the arbitrary setting of the
number of test organisms will not assure a certain precision for  the results."
An example is cited  of tests with sewage effluent indicating that with  10
fish per  toxicant concentration, the 95% confidence interval was  within ±20%
of the means while when  20  fish were exposed it was within ± 14%  of  the mean
value.
     LC   values were  estimated by  interpolation  after plotting the  data on
semilogarithmic  coordinate  paper with  concentrations  plotted on the  loga-
rithmic  and  percentage  dead plotted on the  arithmetic scale, as described  in
Section  801F.1  (APHA et  al.,  1976).  This  method  of interpretation has  been
shown  to give values within the precision  of the  test.
                                        29

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                                 APPENDIX F
                  METHOD FOR CARBARYL ANALYSIS AS REPORTED
                             BY HATHAWAY (1979)

Methodology:  Carbaryl Analysis
     A liter of the sample was extracted serially with three 50 ml portions
of methylene chloride.  The extracts were combined and passed through Na2S04
into a 250 mL round bottom flask.  50 ml of ethyl acetate was added to the
flask and the solvents were concentrated to 10 mL in a rotary evaporator at
45° C.  The extract was passed through a cleanup column of 3 cm Florisil
topped with 1 cm of Na2S04.  The Carbaryl was eluted with 20 mL of ethyl
acetate.  The 30 mL of ethyl acetate was concentrated to 10 mL on a hot
plate under a gentle  stream of carbon filtered air.
     The extract was  analyzed on a Waters 204 Liquid Chromatograph with a
M Bondapak C18 column.  A methanol-1% acetic acid gradient was used over
25 minutes at a flow  rate of 2.0 mL/min.  The gradient was run from 0 to 80%
methanol.  The dual channel UV detector was operated at wave lengths of
254 run and 280 nm.
Quality Control:  A blank and a  spike were analyzed along with the samples.
The blank did not contain any interferences at the retention time of Carbaryl.
The spike was at a concentration of  250 pg/L  of  Carbaryl and the recovery
was 117%.
      The presence of  Carbaryl  in the samples  was established by the  coinci-
dence of retention time  and confirmed by  the  ratio of  the 254  to 280  response.
                                        30

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                                 APPENDIX G
                   METHOD FOR THE ANALYSIS OF CARBARYL AS
                         DEVELOPED BY UNION CARBIDE

     Samples were extracted serially with methylene chloride which was then
dried with Na2S04.  The extract was analyzed on a Varian 825 Liquid Chromato-
graph with a Micropak CN-10 column.  The mobile phase consisted of N-propanol
10% in iso-octane.  A single UV detector was operated at a wavelength of
25A run.
                                       31

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TECHNICAL REPORT DATA
(Please read Inunctions on the reverse before completing)
1. REPORT NO. 2.
EPA-600/2-80-077a
4. TITLE AND SUBTITLE
Treatability Studies of Pesticide Manufacturing
Wastewaters: Carbaryl
7.AUTH0R(s) Edward Monnig, Michael Murphy, Ruth
Zweidinger, and Linda Little
9. PERFORMING ORGANIZATION NAME AND ADDRESS
Research Triangle Institute
P.O. Box 12194
Research Triangle Park, North Carolina 27709
12. SPONSORING AGENCY NAME AND ADDRESS
EPA, Office of Research and Development
Industrial Environmental Research Laboratory
Research Triangle Park, NC 27711
3. RECIPIENT'S ACCESSION- NO.
5. REPORT DATE
April 1980
6. PERFORMING ORGANIZATION CODE
8. PERFORMING ORGANIZATION REPORT
10. PROGRAM ELEMENT NO.
1BB610
11. CONTRACT/GRANT NO.
68-02-3688, Task 109
13. TYPE OF REPORT AND PERIOD COVE
Task Final; 2/78-3/80
14. SPONSORING AGENCY CODE
EPA/600/13
15. SUPPLEMENTARY NOTES T.ERL-RTP project officer is David C. Sanchez, Mail Drop 62,
919/541-2547.
         The report gives results of a bench-scale, experimental treatability stud
of wastewaters from the manufacture of the pesticide carbaryl. Results indicate tt
both carbaryl manufacturing wastewater (mixed one part in nine parts municipal
wastewater) and carbaryl itself (spiked at 10 mg/L in municipal wastewater) appea
suitable for biological treatment by acclimated systems if additional provision is
made for removing ammonia in the effluents from these biological treatment sys-
tems.  Other parameters investigated in this study--including carbaryl, alpha-
naphthol,  and toluene concentrations and the chemical oxygen demand (COD)—all
showed large reductions (90% or greater).  The mechanisms of reduction of these
parameters include combined hydrolysis and biodegradation of carbaryl and alpha-
naphthol,  volatilization of toluene, and biodegradation of species  contributing  to O
A large increase in ammonia  concentration was noted in the effluent from the  bio-
logical units treating carbaryl manufacturing wastewater.  This ammonia concentr;
tion made the toxicological evaluation of the effectiveness of  treatment problemati
by rendering the effluent more toxic than the influent. Ammonia stripping lessenec
this toxicity. Because the technology of nitrogen control has  been extensively  deve
oped,  these treatment options were not pursued further.
17. KEY WORDS AND DOCUMENT ANALYSIS
a DESCRIPTORS
Pollution Nitrogen
Pesticides Naphthols
Industrial Processes
Waste Water Toluene
Waste Treatment Toxicity
Ammonia Oxygen Demand
18. DISTRIBUTION STATEMENT
Release to Public
b. IDENTIFIERS/OPEN ENDED TERMS
Pollution Control
Stationary Sources
Carbaryl
Treatability
Alpha-naphthol
Chemical Oxygen De-
mand
19. SECURITY CLASS (This Report)
Unclassified
20. SECURITY CLASS (This page)
Unclassified
C. COSATI
13B
06F
13H
07B
Field/Groi
07C
06T
06F
21. NO. OF PAGES
33
22. PRICE
EPA Form 2220-1 (9-73)

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