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2015（2）%%%%：20150313：（1982—），，，，,，。：UASB、EGSB、IC，。3，。、，。：UASB；EGSB；IC；；：X703.3：：1005－7676（2015）02－0014－03FANGMingzhong,HEHui,LINJiacheng,ZHONGLiangming（ZhejiangBlueEnvironmentalTechnologyCorporation,Wenzhou325027,Zhejiang,China）UASB,EGSBandICanaerobicreactoriswidelyappliedinwastewatertreatment,mainlyduetoitshighconcentrationofbiomass,aswellashighshockloadingtolerance.Whiletheprogressiverelationshipbetweenthethreetypesofanaerobicreactors,alsoshowsthecorrelationbetweenthedesignofreactorandstableoperationaswellasthephysicalparameters.Thelongstart-upperiods,aswellasinhibitionafterstableoperationaredescribed,showingtheprogressoftheanaerobicreactornowadays.UASB;EGSB;IC;start-upperiods;inhibitionUASB、EGSB、IC，，，（，325027）、、1896，，[1]。，，4～5kgCOD/(m3·d)[2]。，Lettinga1974—1988（UpflowAna-erobicSludgeBed，UASB），，[3]。，、、、、pH，。UASB，，，、、，COD、、，[4]。UASB5，，DOI：10.16056/j.1005-7676.2015.02.01459··2015（2）%%%%；，，；1，，，，，SRT，HRT，，，[5]。UASB、，，，，、，（ExpandedGranul-arSludgeBed，EGSB）、（InsideCycling，IC）、（AnaerobicBaff-ledReactor，ABR）、（AnaerobicSequencingBatchReactor，ASBR）、（AnaerobicMembraneBiosystem，AMBS）[6]。EGSB、，，；，；，。，，EGSB，，。IC21。1，，，2，，。、、UASB、EGSB、IC，，、、、、、，、，。Cavaleiro[7]，，，，。，，，、，。Escudie'[8]、、、。Ghangrekar[9]，，VSS/SS，COD。VSS/SS，，，。VSS/SS0.6～0.85。Mahmoud[10]，，，，，；，，，，；。。，、、，、、、。Benjamin[11]，，，，。Liu[12]，，200mg/L。Harada[13]，，。2，60··2015（2）%%%%、、。Colleran[14]，，100～800mg/L、50～400mg/L。Jin[15]，。Cabirol[16]，、、、，，、，1000～2500mg/L。Wong[17]，：＞＞＞。Ahring[18]，，，、、，、。。23。，[19]。，。，，，，。，。[1]臖,.UASB[J].,2004,34(2):261-268.[2]SchroepferGL.Theanaerobiccontactprocessasappliedtopackinghousewastes[J].SewageandIndWastes,1995,27(4):460-480.[3].[M].:,2005:98-99.[4],.UASBUASB[J].,2007,14(4):62-67.[5].UASB&IC[D].:,2007:73.[6].UASB[J].,2010,17(5):17-23.[7]CavaleiroAnaJ,SalvadorAndreiaF,AlvesJoanaI.Continuo-ushighrateanaerobictreatmentofoleicacidbasedwastewat-erispossibleafterastepfeedingstart-up[J].EnvironSciTec-hnol,2009,43(8):2931-2936.[8]Escudie'R,CressonR,DelgenèsJP.Controlofstart-upandoperationofanaerobicbiofilmreactors:Anoverviewof15yearsofresearch[J].WaterResearch,2011,45(1):1-10.[9]GhangrekarMM,AsolekarSR,JoshiSG.CharacteristicsofsludgedevelopedunderdifferentloadingconditionsduringUASBreactorstart-upandgranulation[J].WaterResearch,2005,39(6):1123-1133.[10]MahmoudN,ZeemanG,GijzenH,etal.Solidsremovalinupflowanaerobicreactors,areview[J].BioresourceTechno-logy,2003,90(1):1-9.[11]BenjaminMM,WoodsSL,FergusonJF.Anaerobictoxicityandbiodegradabilityofpulpmillwasteconstituents[J].Wat-erResearch,1984,18(11):601-607.[12]LiuT,SungS.Ammoniainhibitiononthermophilicaceticla-sticmethanogens[J].WaterSciTechnol,2002,45(10):113-120.[13]HaradaH,UemuraS,MonomoiK.Interactionsbetweensulphate-reducingbacteriaandmethane-producingbacteriainUASBreactorsfedwithlowstrengthwastescontainingdifferentlevelsofsulphate[J].WaterResearch,1994,28(2)：355-367.[14]ColleranE,PenderS,PhipottU,etal.Full-scaleandlabor-atory-scaleanaerobictreatmentofcitricacidproductionwas-tewater[J].Biodegradation,1998,9(3/4):233-245.[15]JinP,BhattacharyaSK,WilliamaCJ,etal.Effectsofsulf-ideadditiononcopperinhibitioninmethanogenicsystems[J].WaterResearch,1998,32(4):977-988.[16]CabirolN,Barraga'nEJ,Dura'nA,etal.Effectofaluminumandsulphateonanaerobicdigestionofsludgefromwaste-waterenhancedprimarytreatment[J].WaterSciTechnol,2003,48(6):235-240.[17]WongMH,CheungYH.Gasproductionanddigestioneffic-iencyofsewagesludgecontainingelevatedtoxicmetals[J].BioresourTechnol,1995,54(3):261-268.[18]AhringBK,WestermannP.Sensitivityofthermophilicmet-ha-nogenicbacteriatoheavymetals[J].CurrMicrobiol,1985,12(5):273-276.[19]ChenY,ChengJJ,CreamerKS.Inhibitionofanaerobicdig-estionprocess:Areview[J].BioresourceTechnology,2008,99(10):4044-4064.61··