AO法处理水产品加工废水李亚峰

A/O110168A/O500t/dCOD、BOD594.7%、98.1%86.4%GB8978—1996《》、、。A/OTHETREATMENTOFWASTEWATERFROMPROCESSINGAQUATICPRODUCTSWITHANA/OPROCESSLiYafengXieXinliSchoolofMunicipalandEnvironmentalEngineeringofShenyangJianzhuUniversityShenyang110168ChinaAbstractAnA/Oprocesswasusedtotreatthewastewaterfromprocessingaquaticproducts.Thetreatmentcapacitywas500t/d.Duringtheoperationoftwoyearstheeffectofthisprocessperformedstably.TheresultshowsthattheremovalratesofCODBOD5andNH3-Nare94.7%98.1%and86.4%separately.Thequalityofeffluentcanmeetthefirst-orderof“IntegratedWastewaterDischargeStandard”GB8978—1996.Theprocessfeatureslowoperationcostgoodtreatmenteffectandconvenientmanagement.KeywordswastewaterfromprocessingaquaticproductsA/Oprocesstreatmentengineering0。、、。、、、1。1500tGB8978—1996《》2。1。1ρCOD/mg·L－1ρBOD5/mg·L－1ρSS/mg·L－1ρNH3-N/mg·L－1pH1000～1300600～800400～50050～806～913008005008091002070156～922.1。A/O3。1。、、。BOD、COD。。。0120112291DOI:10.13205/j.hjgc.2011.01.0041。。pH。。。。。2.2111.2m×0.6m×0.8mB600D31。217.0m×0.6m×0.8m、。318.2m×5.4m×5.2mCT51.5－652Q=25m3/hH=10mN=1.5kWUPVC35m2。418.0m×4.5m×5.0mWJ0.75－4－2102N=0.75kW。5110.0m×8.0m×5.0m2KBB－215200GRB－1252Q=11.72m3/min=49.0kPaN=15kW。612.0m×2.0m×5.0mCT53.7－802Q=45m3/hH=15mN=3.7kW。715.5m×4.5m×5.0mSCZ－7501、。812.25m×1.0m×5.0mCP50.75－502Q=10m3/hH=10mN=0.75kW。913.25m×2.25m×5.5mG25－11Q=2.6m3/hH=60mN=1.5kWXAYJ12/630－U1N=1.5kW。103。UPVC33N=0.37kW16CQ－83N=0.18kW。1119.0m×6.0m。、、。32007112010362。2mg/LpHCODBOD5SSpH1201.8689.8425.86163.513.340.88.37.5797.498.190.486.42A/O25112011229121SivaramanC.AnasuyagangulysrikanthmutnuribiodegradationofhydrocarbonsinthepresenceofcyclodextrinsJ.WordJMicrobiolbiotechnol2009226227-232.22GaronDSageLSeigle-MurandiF.EffectsoffungalbioaugmentationandeyclodextrinamendmentonfluorenedegradationinsoilslurryJ.Biodegradation20041511-8.23BardiLMartiniCOpsiFetal.Cyclodextrin-enhancedinsitubioremediationofpolyaromatichydrocarbons-contaminatedsoilsandplantuptakeJ.InclPhenomMacrocyclChem200757439-444.24.J.200425298-103.25LagemanR.ElectroreclamationapplicationsintheNetherlandsJ.EnvironSciTechnol199327132648-2650.26KrantiMaturi.KrishnaRReddy.Cosolvent-enhanceddesorptionandtransportofheavymetalsandorganiccontaminantsinsoilsduringelectrokineticremediationJ.WaterAirSoilPollut2008189199-211.27KoSOSehlautmanMACart′awayER.Cyclodextrin-enhancedelectrokineticremovalofphenanthrenefromamodelclaysoilJ.EnvironSciTechno120003481535-1541.28BrusseauMLWangXHuQ.Enhancedtransportoflow-polarityorganiccompoundsthroughsoilbycyclodextrinJ.EnvironSciTechnol1994285952-958.29.J.2009272105-109.30ShibanaiINagatomoSGoseiJ.USPatent5492947BarriermaterialcomprisingathermoplasticandacompatiblecyclodextrinderivativeJ.PatternStorm19883442-9.31PatonGI.ReidBJ.Applicationofaluminescence-basedbiosensorforassessingnaphthalenebiodegradationinsoilsfromamanufacturedgasplantJ.EnvironmentalPollution20091571643-1648.32HuaGuoxiongJohnBroderickKirkTSempleetal.Rapidquantificationofpolycyclicaromatichydrocarbonsinhydroxypropyl-b-cyclodextrinHPCDsoilextractsbysynchronousfluorescencespectroscopyJ.EnvironmentalPollution2007148176-181.33WangGWuFZhangXetal.Enhancedphotocata-lyticdegradationofbisphenolFbyβ-cyclodextrininaqueousTiO2dispersionJ.FresenEnvironBullut200615161-67.34AnandanSYoonM.Photocata1yticdegradationofnileredusingTiO2-β-cyclodextri[e-mail]2010－04－07櫅櫅櫅櫅櫅櫅櫅櫅櫅櫅櫅櫅櫅櫅櫅櫅櫅櫅櫅櫅櫅櫅櫅櫅櫅櫅櫅櫅櫅櫅櫅櫅櫅櫅櫅櫅櫅櫅櫅櫅櫅櫅櫅櫅櫅櫅櫅櫅櫅櫅11GB8978—1996。44.1365m224.5830.8910.5566.02。4.248.05kW26.35kW0.5/kW·h316.20.63/t。NaOH0.06kg/m330kg2/kgPAM0.0002kg/m30.1kg40/kg640.13。1250.05/t。5A/OCOD、BOD594.7%、98.1%86.4%GB8978—1996、。1.J.200523515-17.2GB8978—[e-mail]2010－08－025220112291