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 ------- 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 ------- 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 ------- U,S- Environmental Protection Agency ------- 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 ------- Because tne technoloov r\f r,,-«- " 31, 1979. 3S ""Pted as of May ill ------- 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 ------- 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 ------- 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. ------- 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. ------- 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. ------- 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) ------- 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. ------- 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 ------- 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". ------- 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. ------- 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 "- ------- 700 © ®- ® ® G> Influent COD • Unit#1 Effluent COD A Unit #2 Effluent COD Figure 2. Influent and Rrfluent COD ValuPs for T^, A^,..__ , ------- 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. ------- 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 ------- 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 ------- 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 ------- Figure 4. Pesticide Reduction in Activated Sludge Units Fed Municipal Sewage Spiked to 10 n,g/l with Carbaryl ------- 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 ------- 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 ------- -_ ^ 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 ------- 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 ------- 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 ------- 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 ------- 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 ------- 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 ------- 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.). ------- ro INFLUENT FEED RESERVOIR EFFLUENT COLLECTION AIR Figure C-l. Diagram of activated sludge pilot unit. ------- 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 ------- 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 ------- 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 ------- 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 ------- 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 ------- 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 ------- 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. 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