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322009-08-221963-。E-mail:qin.lu.yao@163.com。ABR710021ABR,。ABR。ABRX794A1671-1602201003-0046-05TheResearchProgressofFactorsInfluencingSludgeGranulationandAcceleratingMethodsonABRDINGShao-Lan,QINNing(CollegeofResource&Environment,ShaanxiUniversityofScience&TechnoLogy,Xi’an,710021,China)Abstract:InthispaperitwasdescribedthatthesludgegranulationphenomenonanditsmechanismandthefactorsonABR.ThenseveralwaysforacceleratingsludgegranulationonABRweregiven.Keywords:ABR;granulation;factor;accelerating1。ABR。。2～3[1]。。2ABR2.1ABRStuckeyABRABR。[2-4]ABR、、ABR。BoopathyTilche[5]HABR32320102WESTLEATHERVol.32No.3Feb.2010463·ABR30d13。ABR、。Holt[6]5ABR1~4mm。ABR5、16L、11gVSS/LPCP-Na334、5。1、2、4、5。[7]ABR4.171kgCOD/m3·dABR0.15~5mm2、31、4。BarberBarber8ABR。ABR4、15L、15gVSS/L40d4。、、、。2.2ABR、Lettinga[8]。、[9]UASB“”、。1.6。2.3ABR2.3.1[10]。[11]。2.3.2N、P。N、、P。、、[12-13]。2.3.3。UASB。[14-15]。。。。、。。＜0.05gCOD·gVSS-1d-1TS＞60kgTS·m-3[17]。4732。。。2.3.4。UASB、53～55℃。30～48℃53～55℃。90%。LauandFang[16]UASB55℃65℃37℃CODCOD90%60%40%。。2.3.5。pHpH、。。pH＞8.2[16]。COD＞1∶3。ABRCaCO3500mg/L。McCartyCaCO320~5000mg/LCaCO31000mg/LpH。UASBCaCO3750mg/L。2.3.6ABR、。。。Kosaric[18]0.250.5m·h-11.01.5m·h-1。Guiot[19]4.3m·h-1。3ABR3.1、。MacarieGuyot[20]FeSO4UASB。[21]。Imai[22]WAP·483WAP750mg/LUASB。Tiwari[22]UASB、Reetha、ReethaReethaReetha。0.15、0.144、0.139、0.128mm。[23]。[24]UASB。KymeneSLK-2、、。Ca2+、Mg2+、Fe2+。。3.2Ca2+、Mg2+CO32-、SO42-。。[25]Fe2+、Zn2+、Co2+Ni2+UASB。Cu2+[26]。4ABRABR。。ABR。1ABR。2。3CaCO31000mg/LCaCO3500mg/L。[1].UASB[J].200018217-20.[2].ABR-[J].200329447-49.[3].[J].200218775-76.[4].ABR[J].200016842-44.[5]BoopathyR,Tilche1A.PelletizationofbiomassinahybridanaerobicbaffledreactorHABR)treatingacidifiedwaster1[J].BioresTech1992,40(2):101-107.[6]HoltCJ,MatthewRGS,TerzisE.AComparativeStudyUsingtheAnaerobicBaffledReactortoTreataPhenolicWastewater[C].Proceedingsofthe8thInternationalConferenceonAnaerobicDigestion.Sendi,Japan,1997,40-47.[7].[J].199915510-12.[8]GLettingag,JField,JVanLier,Zee－mang,HulshoffPol.Advancedanaerobicwastewatertreatmentinthenearfuture1[J].WatSciTech1997,35(10):5-12.[9].UASB[J].199612516-19.[10].[M].·ABR4932!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!1998.[11].UASB[J].200018217-20.[12].[M].2003.[13]SpeeceRE.[M]..2002.[14]UemuraS,HaradaH.Effectoftemperatureelevationfrom55Cto65ContheperformanceofathermophilicUASBreactorandcharacteristicsofmethanogenicgranularsludge[J].EnvironTechnol,1993,14(10):897-901.[15]FangHHP,LauIWC.Startupofthermophilic(55C)UASBreactorsusingdifferentmesophilicseedsludges[J].WatSciTech,1996,34(5～6):445-452.[16]LinKC,YangZX.TechnicalreviewontheUASBprocess.Intern[J].JEnvironStudies,1991,39(3):203-222.[17].UASB[J].200218813-15.[18]KosaricN,BlaszczykR,OrphanL,etal.Thecharacteristicsofgranulesfromupflowanaerobicsludgeblanketreactors[J].WatRes,1990,24(12):1473-1477[19]GuiotSR,PaussA,BourqueD,etal.Effectofupflowliquidvelocityongranulesizedistributioninanupflowanaerobicbedfilter(UBF)reactor[A].TilcheARozziA.Fifthinter2nationalsymposiumonanaerobicdigestion[C].Bologna:MonduzziEditore,1988.[20]ManojK.Tiwari,Saumyen,Guha,etal.EnhancedgranulationbynaturalionicpolymeradditivesinUASBreactortreatinglow-strengthwastewater[J].WaterResearch,2005,39(16):3801-3810.[21].UASB.1996312-15.[22]ImaiT,UkitaM,LiuJ,etal.Advancedstart-upofUASBreactorsbyad2ditionofwaterabsorbingpolymer[J].Water.Sci.Technol,1997,36(6):399.[23].UASB+AF.200117253-55.[24].UASB[J].1996312-14.[25].[J].199916324-25.[26].UASB[J].200218626-28.。。A.。。B.、。。。C.。D.。E.、。。F.1。2。3,,。4,。G。。。·50