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451320177GuangzhouChemicalIndustryVol.45No.13Jul.2017112121212114500012450001。UASB、EGSB、IC、、。。X703.3A1001－9677201713－0032－03ResearchProgressonHigh－rateAnaerobicReactorYANGShan1MAXiao－jian12CHENJun－ying12FANGShu－qi12BAIJing12CAILi－fang11SchoolofChemicalEngineeringandEnergyZhengzhouUniversityHenanZhengzhou4500012EngineeringLaboratoryofHenanProvinceforBio.RefineryTechnologyandEquipmentHenanZhengzhou450001ChinaAbstractForsolvingtheincreasinglyseriousenvironmentalandenergyissuesbiologicalenergycandrawmoreandmoreattention.Anaerobicdigestiontechnologyasthemostprevalentmethodofsewagesludgestabilizationandrecyclationhasabroaddevelopmentprospect.ThedevelopmentofanaerobicreactorssuchasUASBEGSBICreactionmechanismoperatingrulesadvantagesanddisadvantagesaswellasapplicationstatusofdomesticandforeignscholarsstudyingonthemwerediscussed.Thedirectioninanaerobicreactorsdevelopmentwasintroduced.Moreovertheproblemsneededforfurtherstudywerepointedout.Keywordsanaerobicreactorsdevelopmenttypicalreactorsresearchprospects1990－。1953－。。11990－2003100m32003460m320111050m3。2。3、。。。Bryant4Zeikus5。。11881100。。1.118966。1904Imhoff7。19146。2050Schroepfer8。4513331.22060。1969Young239。1974LettingaUASB10。11。1.3。2080。22.1UpflowAnaerobicSludgeBlanketUASBUASB12。1972－1978LettingaUASB10。UASB、131。。。。。。。1UASBFig.1SchematicdiagramofUASBreactorShigeki14UASB1325℃HRT4.7h6CODCOD80%70%。15COD7.2kgCOD/m3·d80%CH46.2L/d。2.2expandedgranularsludgeblanketEGSBEGSBUASB。2080WageningenEGSB。COD16。EGSB2、、、17。。。2EGSBFig.2SchematicdiagramofEGSBreactorKato1830℃EGSBCOD100200mg/L12kgCOD/m3·dHRT4hCOD80%。19EGSB20℃、HRT18h184dEGSB10kgCOD/m3·dCOD85%1kgCOD0.58m3。2.3internalcyclicreactorICUASB2080PAQUES20。IC2UASB。、、213。。。。3420177。。。。。3ICFig.3SchematicdiagramofICreactorPengyiCui22IC。SCOD3500mg/L18kgCOD/m3·d68%SCOD6600mg/L16kgCOD/m3·d60%。23ICOLR。1.0m/hOLR2.5018.94kgCOD/m3·dCOD85%4.49L/L·d。COD60%81%。3。。12fluent。3。4。5。6。、。1.J．201024133－133.2.J．2007222174－176.3.—D．2007.4LafitteTSForsterCF.Dualanaerobicco－digestionofsewagesludgeandconfectionerywasteJ．BioresourceTechnology200071177－82.5.J．2008s1215－219.6.J．200324482－86.7HAANDELAVKATOMT.AnaerobicReactorDesignConceptsfortheTreatmentofDomesticWastewaterJ．ReviewsinEnvironmentalScienceandBio/Technology20065121－38.8SCHROEPFERGJANDERSONJJ.TheanaerobiccontactprocessasappliedtopackinghousewastesJ．Sewage＆IndustrialWastes1955274460－486.9YOUNGJCMCCARTYPL.TheanaerobicfilterforwastetreatmentJ．Journal－WaterPollutionControlFederation1969415SupplR160+.10LETTINGAGHAANDELAC.AnaerobicdigestionforenergyproductionandenvironmentalprotectionJ．RenewableEnergySourcesforFuels＆Electricity1993817－839.11.J．200422212－17.12.UASBJ．2008325655－660.13.UASBD．2008.14UEMURASHARADAH.TreatmentofsewagebyauasbreactorundermoderatetolowtemperatureconditionsJ．BioresourceTechnology2000723275－282.15.UASBJ．201483851－856.16.EGSBJ．200512330－32.17.EGSBD．2007.18KATOMTFIELDJALETTINGAG.TheanaerobictreatmentoflowstrengthwastewatersinuasbandegsbreactorsJ．WaterScience＆Technology1997366375－382.19.EGSB20℃J．2008294990－995.20.icD．2005.21.ICJ．200022339－41.22CUIPYZHOUXFZHANGYL.ThefeasibilitystudyofcottonpulpwastewatertreatmentwithicanaerobicreactorJ．ProcediaEnvironmentalSciences2011111686－692.23LUOGLIJLIYetal.PerformancekineticsbehaviorsandmicrobialcommunityofinternalcirculationanaerobicreactortreatingwastewaterwithhighorganicloadingrateRoleofexternalhydrauliccirculationJ．BioresourceTechnology2016222470－477.