MBBR法处理桃浦工业区废水的中试研究李 锋 向 阳 周增炎 采用MBBR法处理桃浦工业区废水,同原有的SBR法相比无论在有机物的去除效果上还是对有机物的耐冲击负荷上都更优越。试验结果表明,当HRT为6~15h时,MBBR法对COD的平均去除率大于75%。 MBBR法 工业废水处理 悬浮填料0 ,、、。,75%。。SBR,4m3/d,80%。COD800mg/L,200mg/L。,,;SBR,,。MBBR。1 MBBR(MovingBedBiofilmReac-tor,MBBR)80。,,。。,(160~450m2/m3),,、,,、。MBBR,,,;,,(),、、、,,,。,,,。,、、、;,,、。2 MBBR2.1 :※※MBBR※※。。,,MBBR,。4m3。,。pH,,。1 MBBRMBBR1,3m×1.25m×1.5m,4.2m3;4;, Vol.27 No.4 200147 DOI:10.13789/j.cnki.wwe1964.2001.04.015;,50%;,,。,,50mm,350m2/m3。2.2 COD:;BOD:;DO:YSI;:105℃。2.3 2.3.1 MBBRCODMBBR。,10~35℃,:COD200~800mg/L,BOD/COD0.4,SS50~200mg/L,pH6~9,NH3-N20~50mg/L。,,pH1.9;COD,1400mg/L;,。MBBR,HRT5~8h。20004(COD),HRT15h3,HRT20h2,HRT17h2,HRT12h。SBR:HRT16h,MLSS3~5g/L。2 MBBRCOD3 SBRCOD 2200047MBBRCOD,3SBRCOD,4COD4 SBRMBBRCOD。2,34,MBBRCOD75%,SBR60%;COD800mg/L,200mg/L,。2.3.2 1,COD800mg/L,(0.42~1.16kgCOD/(kgMLSS·d)),COD75%,COD200mg/L。,HRTCOD。COD,COD。COD200~300mg/L,,COD70%。,DO。MBBR48 Vol.27 No.4 20011 ⅠⅡⅢⅣHRT/h/℃COD/mg/LCOD/mg/LNs/kgCOD/(kgMLSS·d)/gMLSS/LDO/mg/LηCOD/%2.141.893.0 57.8 1.071.205.8 18.7 0.141.087.0 2.2 0.140.567.2 1.2 1.161.18 79.9 1228860173Ns/kgCOD/(kgMLSS·d)/gMLSS/LDO/mg/LηCOD/%0.822.740.7 48.4 0.422.545.5 23.2 0.101.718.6 3.7 0.081.549.0 2.8 0.422.13 78.1 1511721158Ns/kgCOD/(kgMLSS·d)/gMLSS/LDO/mg/LηCOD/%1.052.622.7 55.3 1.060.907.3 19.3 0.140.358.1 1.0 0.270.268.2 1.4 0.931.03 77.0 1720876202Ns/kgCOD/(kgMLSS·d)/gMLSS/LDO/mg/LηCOD/%0.722.531.6 51.4 0.940.906.3 24.0 0.267.0 0 0.140.567.3 2.2 0.631.06 76.0 2021734176Ns/kgCOD/(kgMLSS·d)/gMLSS/LDO/mg/LηCOD/%0.491.843.5 26.9 0.372.145.1 24.0 0.271.076.0 8.6 0.100.566.8 1.7 0.361.40 61.212*22417162Ns/kgCOD/(kgMLSS·d)/gMLSS/LDO/mg/LηCOD/%0.841.373.3 64.6 0.120.997.6 6.7 0.908.4 0.647.9 0.320.98 70.9 12**3022365 :*;**。,,HRT。3 (1)MBBR,SBR。MBBR75%。,COD800mg/L,200mg/L;,COD;(2)MBBRSBR,COD;(3)MBBRHRT。,,HRT6~15h,。:200092 :(021)65985308 191-3152806 :2000-9-22·广告·JWX、、,,,,,,,,。一握恒龙手,永远是朋友。总经理周建达祝全国用户在新世纪里身体健康,心想事成! :27 :214211: :(0510)7805562 7807579 :(0510)7881310 :13806158562 Vol.27 No.4 200149 WATER&WASTEWATERENGINEERINGVol.27No.4April2001OptimizationoftheOperationParametersonMBRandMembraneFoulingControlZhengXiangetal(41…………………)Abstract:Inthispaper,optimizationofoperationparametersonmembranebioreactor(MBR)isinvestigatedandmembranefoulingcountermeasuresarediscussed.Theresultsshowthatthelow-pressureoperationcanreduceenergyconsumptionandretainhighflux;membranefoulingiscrucialfactorforenergyconsumption;constant-fluxoperationcanalleviatemembranefouling;backwashingiseffectivecountermeasuretoretainconstantflux.PilotPlantStudyonMovingBedBio-filmReactorTreatingIndustrialWastewaterLiFengetal(47…………………………)Abstract:Thepilotplantoperationofmovingbedbio-filmreactor(MBBR)issuccessfultotreatindustrialwaste-waterfromTaopuindustrialzone.ComparedwithSBR,MBBRismoreefficienttoremoveorganicmatterandtobuffertheorganicshockloading.Theresultofpilot-plantexperimentshowsthatCODcanberemovedmorethan75%byusingMBBRwhenHRTis6hto15h,andCODineffluentcansatisfythedischargedemand.ApplicationofAABCProcessinTextileWastewaterTreatmentLiuHong(50…………………………………………………)Abstract:Anaerobicaerobicbio-carbon(AABC)processwasdevelopedtotreatprintinganddyeingwastewater15yearsago.Nowithasbeenappliedsuccessfullyintextile,printinganddyeingofcotton,silk,wool,syntheticfiberandgarmentindustries.Alsoithasbeenadoptedtotreatdomesticwastewater.Inthispaper,theapplicationofAABCpro-cessintextileandgarmentindustriesispresentedwithpracticalexamples.DesignandOperationofDetergentWastewaterLiangYanzhouetal(52………………………………………………………)Abstract:TheanionsurfactantsLASindetergentwastewaterisbadlydegradableorganiccompounds,buritcanberemovedeffectivelyfromwaterbycoagulation-sedimentation,hydrolysis-acidificationandcontactoxidationprocess.Theeffluentofthisprocessisstableandquitegoodtomeettherequirementofdischargestandard.50%and98%ofLASareremovedincoagulation-sedimentationandcontactoxidationprocessrespectively.ButtheLASremovalinhydrolysis-acidificationunitisstilllow.BriefonDesignandApplicationofanIntegralTrenchforVariousPipelinesinResidentialQuarterHuangXintian(58……)Abstract:Theintensivedispositionofvariouspipelinesinanintegralpipetrenchisbeneficialeconomicallyandtechnically,becausethisnotonlysolvestheproblemsinengineeringconflictandinterferenceofhorizontalandverticallayoutsofthepipelines,butalsocreatesafavorableconditionfortheoperationandmaintenanceofthepipeline.Onthebasisofapracticalexampleofalivingquarterwithhighriseresidentialbuildings,thedesignexperiencesofintegralpipetrencharepresentedinthispaper.WaterSystemDesignofWanBangCityGardenApartmentsZhanghongetal(70……………………………………………)Abstract:Somenewpracticesinindoorwatersystemdesignforresidentialbuildingsarepresentedinthispaper.Variousitemsareincludedsuchastheselectionofpipelinematerials,watersupplypatternsandlavatorydrainagepat-terns,theadoptionofreadingcachetbasedremotewatermeteranddesignoffirehydrantsystemfor9to12-storyresi-dentialbuildings.StandardizationofUpward-flowAnaerobicSludgeBlanket(UASB)ReactorWangKaijunetal(85…………………………)Abstract:Int