李 方 杨 波 田 晴 陈季华(,200051) 针对纺织染整企业各股废水的特点,提出混凝沉淀+生化处理的工艺路线,并考虑在工艺系统中实现污泥减量。工程运行结果表明,出水水质优于《纺织染整工业水污染物排放标准》(GB4287-92)中一级排放标准,实现部分污水回用,而且系统污泥减量效果良好。 纺织 染整 综合废水 污泥减量 、、、、。,,。1 、1.1 设计水量Q=15000m3d,、、。1.2 设计水质分析,,41。1 COD(mg·L-1)BOD5(mg·L-1)pHSS(mg·L-1)NH3-N(mg·L-1)(m3·d-1)10003501286~720010300030001200646~6.52002040025004005129~114001090006002002568~111200520004001506.5~7.54004060015005004008.5~1135015150001.2.1 、,Ⅰ、Ⅱ、Ⅲ,CODBOD5,COD3.2mgL。90%,3000mgL,BOD51500mgL[1]。COD,,[2]。1.2.2 、。CODpH,PVA[3]。COD2000mgL,。COD200~400mgL,,pH11。,9000m3d,pH,COD、,pH,。1.2.3 ,、、、、,COD600mgL。。,《》(GB4287-92)。2 1。77 200810265DOI:10.13205/j.hjgc.2008.05.0231 ,,pH,,PVA、、。,PVA、、、,,,BC。,,。(),0.5mgL,,。,。,,,[4-5]。,,。,,。,,。3 ,。。2。2 ()42m×32m×5.3m1HF-800,210m×6m1200-WLB360-7.4-15,332m×12m×5.3m142m×32m×5.5m2TA42m×32m×5.3m1TA42m×20m×5.3m2JAS-200,4,,HA-65=24m,h=5.5m2BXH-24,25m×5m×3.3m16m×6m112m×8m1=24m,h=5.5m2BXH-24,215m×10m×5.5m2JTS-80,1;=10m,h=5.5m219m×9.5m1CDYC150020m×8m110m×10m1200WLB360-7.4-15,318m×8m()178 2008102654 (1),、(),C∶N∶P=100∶5∶1(,C∶N∶P),;7d,。30d,、,3000mgL,。4d,,《》(GB4287-92),3。3 mgL(pH、)CODBOD5SSNH3-NpH90154076~730 ,、,,。(2),。:①“++”,,;②,、PVA,。5 (1),“++”,。(2)“++”,,。[1] ,,..:,1990:135-167[2] ,..,2001,19(6):7-9[3] .PVA.(),2002,28(1):101-104[4] ,,,.-A1A2O.,2006,27(3):478-482[5] ,,,.-A1A2O.,2007,28(6):1280-1284 201620 2999E-mail lifang@dhu.edu.cn2008-02-132008《》《》()1982,,,。、。:、、、、、、、、、。,、、、、、。《》,CN53-1205x,ISSN1673-9655,25,96,60,。 :650034::23::《》 :53001615637050309169():0871-4142389E-mail:ynhjkx@yies.org.cn。79 200810265APPLICATIONOFMBRTECHNOLOGYINTREATMENTOFPCB'sWASTEWATERWuShiwen(68)…………………………………………………………………………………………………………………………………Abstract ThepracticalapplicationofMBRtechnologyintreatmentofPCB'swastewaterwasintroduced.TheoperationresultsshowthattheMBRsystemisstablewithqualityeffluentunderthefollowingconditions:theinfluentCODof1500mgL,Cu2+of1.5mgL,MLSSof6000~8000mgLandDOof2~4mgL,withthesystemtemperatureof20~40℃,residencetimeof10handaerationquantityof40~43m3min.TheaverageremovalrateofCODisover87%andthatofCu2+isabout70%.Keywords MBRtechnology PCB COD Cu2+ treatmentofwastewaterENGINEERINGPRACTICEANDSTUDIESONSLAUGHERWASTEWATERTREATMENTGuoTing YangPing WangHonglei(70)………………………………………………………………………………………Abstract Theslaugherwastewaterwastreatedwithhydrolyticacidification-CASStechnology.TheoperationalresultsprovethattheCASStechnologyhasgoodeffectiveness.VariousfoulingindexesoftheeffluentmeetthefirstclassofDischargeStandardofWaterPollutantsofMeatPackingIndustry(GB13457-92).Keywords slaugherhousewastewatertreatment hydrolyticacidification CASSPRETREATMENTOFREFUSELEACHATEBYCOOPERATIONFUNCTIONOFHIGHMAGNET-ICPOWDERTangYanchao ChengYue FuMingliang(72)……………………………………………………………Abstract Thecooperationfunctionofhighmagneticpowder(Fe3O4)andabio-coagulantAl2(SO4)3werestudiedinthispaper.TheresultindicatedthattheflocculationeffectfromcomplexuseofFe3O4andAl2(SO4)3wasbetterthanuseofAl2(SO4)3only.WhendosageofAl2(SO4)3is2.0gL,Fe3O4is1.6gL,stirringrateis150rpm,pHis3.0,sedimentationtimeis5min,theCODremovalrateofleachateis70%.Thesedimentationvelocityofcolloidalparticleispickedupevidentlyinflocculation.Keywords highmagneticpowder cooperationfunction leachate flocculationRESEARCHONMAINFACTORSOFINFLUENCINGBIOLOGICALP-PEMOVALINEBPRSYS-TEMCaiTianming CaiShu NingQiangetal(74)…………………………………………………………………………Abstract Takingenhancedbiologicalphosphrousremoval(EBPR)systemastheobjectofstudy,itwasresearchedtheeffectsofinfluent'sacetateconcentration&pHandresidenttimeofsludgeonitsphosphorusremoval(PR).TestresultsshowedthatPRratewasincreasedgradual-lywiththeincreaseofacetateconcentrationwhenaceticacidwaslessthan30%beforekeepinganaerobicconditionfor45min;afterkeepinganaerobicconditionfor2h,theconcentrationofaceticacidhaslesseffectonPR.ThesuitablepHwas6.0~7.0foranaerobicPR,aerobicobso-rptionofphosphorusandCODdegradation.WhenpHwaslargerthan8.0thesystemwouldloseEBPRcapacityandPRwasonly39.7%.Iftheagewas4dtheconcentrationofPintheeffluentwaslowerandthesystemwouldhavethebestrunningeffect.Keywords EBPR acetateconcentration pH sludgeageDESIGNOFCOMPOSITIVEWASTEWATERTREATMENTPLANTOFALARGETEXTILECOR-PORATIONLiFang YangBo TianQinetal(77)………………………………………………………………………Abstract Accordingtothecharacteristicsofthecompositivewastewaterinalargetextilecorporation,theprocessofcoagulatingsedimenta-tionandbiologicaltreatmentwasadoptedinthisproject.Thesludgereductiontechniquewastakenintoaccountinthisdesign.ThepracticeshowedthattheeffluentqualitymettherequirementofGradeⅠof“NationalTextileWastewaterDischargeStandard”(GB4287-92)andpartofbio-filtereffluentwasreclaimed.Theexcellentbiologicalsludgereductionwasobtainedduringtherun.Keywords textile dyingandfinishing compositivewastewater sludgereductionAUNIVERSALEXPONENTIALFORMULAOFAIRQUALITYASSESSMENTBASEDONARTIFI-CIALFISHSWARMALGORITHMLiZuoyong WangJiayang WuMin(80)……………………………………Abstract Bysettingupbenchmarksforairqualityindices,auniversalexponentialformulawithpowerfunctionformulti-indicesofairpol-lutantisputforthforevaluatingairquality.Artifi