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:2007-04-24:(1976—),,,.E-mail:tanxuejun@mail.tongji.edu.cnSBR谭学军1,2,唐 利1,周 琪1(1.,200092;2.,200092):、、,(SBR).:SBR(COD),COD;2,3,5(2,3,5-triphenyl-tetrazoliumChloride,TTC)[2-(p-iodophenyl)-3-(p-nitrophenyl)-5-phenyl-tetrazoliumChloride,INT](ETS)(OUR),TTCINTETS,OUR;pH,(DO),(ORP)SBR;SBR(MLVSS)(MLSS),MLVSSMLSS.:;;;;;:X703.1 :A :0253-374X(2008)08-1094-07PerformanceofOperationofSequencingBathReactorSystemforLowTemperatureSewageTreatmentTANXuejun1,2,TANGLi1,ZHOUQi1(1.SchoolofEnvironmentalScienceandEngineering,TongjiUniversity,Shanghai20092,China;2.ShanghaiMunicipalEngineeringDesignGeneralInstitute,Shanghai200092,China)Abstract:PerformanceoflowtemperatureSequencingBatchReactor(SBR)systemwasstudiedviatheinvestigationofpollutantsremoval,parameterscontrol,biologicalactivityandsludgecharacteristics.TheresultsshowthatChemicalOxygenDemand(COD)removalinlowtemperatureSBRsystemisdi-videdintotwostages,andnitrificationreactionoccursoninthesecondstage.2,3,5-triphenyl-tetra-zoliumChlorideTTCand2-(p-iodophenyl)-3-(p-nitrophenyl)-5-phenyl-tetrazoliumChloride(INT)-ElectronTransportSystem(ETS)activityandOxygenUptakeRate(OUR)ofactivatesludgechangedperiodicallyinthelowtemperatureSBRsystem.ThevariationofTTCandINT-ETSactivitycanprovidesuitableinformationabouttheprocessofthewholeSBRsystem,andOURcanreflectthebiochemicalreactionoftheaerobicstage.pHvaluesprovideagoodindicationoftheongoingbiologicalreactionsforthewholeprocess,DissolvedOxygen(DO)onlyfitsforaerobicprocessandOxidationReductionPotential(ORP)isunsuitableforlowtemperatureSBRprocesscontrol.MixedLiquidVolatileSuspendedSolid(MLVSS)/MiredLiquidSuspendedSolid(MLSS)oflowtemperatureSBR36820088()JOURNALOFTONGJIUNIVERSITY(NATURALSCIENCE)Vol.36No.8 Aug.2008systemriseswiththeincreaseofoperationcycle,andwhensystemremainsstable,MLVSS/MLSSoflowtemperaturesystemishigherthanthatofnormaltemperaturesystem.Keywords:wastewatertreatment;sequencingbatchreactor(SBR);lowtemperature;performanceofoperation;biologicalactivity;controlparameters (sequencingbatchreactor,SBR),,.SBR、,、、、,[1],SBR、,,SBR,SBR,.SBR,.,、、,.,(dissolvedoxygen,DO)、(oxidationre-ductionpotential,ORP)pH、,SBR[2-3],SBR.SBR.,(electrontransportsystem,ETS)(oxygenuptakerate,OUR),ETS,OUR(O2)[4-5].2,3,5(2,3,5-triphenyl-tetrazoliumchlo-ride,TTC)[2-(p-iodophenyl)-3-(p-nitrophenyl)-5-phenyl-tetrazoliumchloride,INT]ETS,ETSTTCETSINTETS[6-8].,SBRTTCINTETSOUR,SBR.(5±1)℃SBR,SBR、、.SBR,SBR,.1 1.1 ,,pH.1.2 SBR,70cm,30cm,40L.,;;;DO,ORPpHDO,ORPpH.1.3 1.3.1 ,.,(25±1)℃,,10h,2,.2,CODcr40040mg·L-1,COD90%,0mg·L-1,30%,,.1.3.2 ,(25±1)℃.,,1095 8,:SBR (25±1)℃(5±1)℃,.1,10,2431,SBR、、;,SBR.SBR,、,400,456mg·L-1,6500mg·L-1.,COD,“”,TTCETS,INTETS,OUR,DO,ORP,pH.1.4 1.4.1 TTCETS10mL0.8mL、0.5mL0.36%Na2SO30.3mL0.4%TTC.30min,1mL37%,.4000r·min-15min,,5mL,,10min.4000r·min-15min,.485nm.(105±1)℃1h.TTCETS:UT=D485V/KTWt(1):UTTTCETS,mg·g-1·h-1;D485485nm;V,mL;KTTTC;W,g;t,h.1.4.2 INTETS10mL0.3mL、1.5mLTrisHCl1mL0.2%INT.30min,1mL37%.4000r·min-15min,,5mL,,10min.4000r·min-15min,485nm,(105±1)℃1h.INTETS:UI=D485V/KIWt(2):UIINTETS,mg·g-1·h-1;KIINT.1.4.3 OUR250mLOUR,,,,,0.1mg·L-1.OUR,.,.ρ(DO)—tOUR,:UO=Δρ(DO)/Xt(3):UO,mg·g-1·h-1;Δρ(DO),mg·L-1;X,g·L-1;t,h.1.4.4 CODcr(5B1COD);NO-3—N();NO-2—N(N(1));NH4+—N();(MLSS)(MLVSS)();DO(WTWOxilevel2);ORPpH(HANNApH211).2 2.1 1.COD,SBRCOD,(COD,COD),.1,10,2431COD20,40,6060min.COD,COD,(),().,COD.:,,,,[8].1096 ()36 ,COD,,COD.COD,COD(1/10~1/5),COD90%.,,SBRCOD.1 SBRCOD、、((5±1)℃)Fig.1 TheprofilesofCOD,ammonia,nitrateandnitriteinSBRprocessat(5±1)℃ ,(190min,10、2431120min),COD,COD.,COD,,COD.COD,COD,.,COD,,.,SBR,30%,.SBR,1h.2.2 TTCINTETSOURSBRTTCINTETSOUR2.,TTCETSCOD;,TTCETS,;COD,TTCETS.TTCETSCOD,TTCETS.COD,COD,TTCETSCOD.,160120min,10,243190180min.TTCETS,,,.SBRINTETSTTC1097 8,:SBR ETS,.SBR,、,TTCINTETS.,TTCINTETSSBR.2 SBRTTCINTETSOUR((5±1)℃)Fig.2 TheprofilesofTTCandINTETSactivityandOURofactivatedsludgeinSBRprocessat(5±)℃ OURCOD,COD(120min,1040min,24,3160min),OUR,;,,OUR;COD,OUR,.,OUR.,OURCOD,CODOURCOD.TTCINTETSOUR.2.3 DO,ORPpHSBRDO,ORPpH3.DO,,DO,COD;COD,DO,;,DO(COD,);COD,DO,.DOSBRCOD.COD,ORP;COD,;COD,ORP,.,24ORP“”,.,,ORPSBR.,pHCOD,COD,.,pH,COD,pH,1098 ()36 .,pH,,.DO,ORPpH,SBRDO,ORPpH.,pH,DO,ORPSBR.3 SBRDO,ORPpH((5±1)℃)Fig.3 TheprofilesofDO,ORPandpHinSBRprocessat(5±1)℃2.4 MLVSSMLSS,,[9].SBRMLVSSMLSS,,4.,SBRMLVSSMLSS0.827~0.845,0.839;SBRMLVSSMLSS.1,MLVSSMLSS;10,MLVSSMLSS,0.840;2431,MLVSSMLSS,,0.8660.867,.,SBR,SBR,.4 SBRMLVSSMLSS((5±1)℃)Fig.4 TheprofilesofMLVSS/MLSSinSBRprocessat(5±1)℃3 (1)SBRCOD,,.1099 8,:SBR COD.(2)SBRTTCINTETSOUR,TTCINTETS,OUR.(3)SBRDO,ORPpH,pH,DO,ORP.(4)SBR,MLVSSMLSS.:[1] ,,.SBRORPCOD[J].,2002,28(9):40. GAODawen,PENGYongzhen,WANGShuying.CorrelationofORPandCODinSBRprocesstreatingsoybeanprocessingwastewater[J].Water&WastewaterEngineering,2002,28(9):40.[2] PengYZ,GaoJF,WangSY,etal.UsingpHandORPasfuzzycontrolparametersofdenitrificationinSBRprocess[J].WaterScienceandTechnology,2002,46(4/5):131.[3] AkinBS,UgurluA.Monitoringandcontrolofbiologicalnutrientremovalinasequencingbatchreactor[J].ProcessBiochemistry,2005,10:2873.[4] OrhonD,OkutmanD.Respiromet
本文标题:低温SBR法污水处理系统运行特性谭学军
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