高效厌氧反应器流态研究综述张恺

421220146GuangzhouChemicalIndustryVol.42No.12Jun.2014*(东华大学环境科学与工程学院，上海201620)D/uLD/uL。X703.3A1001－96772014012－0006－03*2232012D3－08。1989－。1979－。ＲeviewofFlowPatternsofHigh－rateAnaerobicBioreactor*ZHANGKaiCHENXiao－guangMACheng－yuSchoolofEnvironmentScienceandEngineeringDonghuaUniversityShanghai201620ChinaAbstractThedevelopmentprocessofhigh－rateanaerobicbioreactorwasreviewedwhichshowedthattheupgradingofanaerobicbioreactorwasrelatedtotheimprovingofflowpattern.Thecurrentstudyofflowpatternofanaerobicbioreactorshowedthatbothnumericalsimulationandexperimentsimulationwereusedtostudytheanaerobicreactorflowpattern.SeveraltypicalanaerobicbioreactorflowpatterncharacteristicsweredescribedwhichindicatedthatdispersionnumberD/uLcanbeusedasanimportantflowpatterncharacteristicparametersofanaerobicbioreactorandthehigherthereactorloadwasthegreatertheD/uLvaluewasobtained.Keywordsanaerobicbioreactorflowpatterndispersingnumber、、1－2。3。、。。11.1。1860LouisMouras。。1974Lettinga4UpflowAnaerobicSludgeBlanketUASB。UASB、、。UASB、。ExpandedGranularSludgeBlanketEGSB5、InternalCyclicＲeactorIC6、AnaerobicBuffedＲeactorABＲ7、“”StagedMultiphaseAnaerobicＲeactorSMPA48。。1.2UASB。DeCarvalhoUASBUASBCSTＲ9Narayanan242127UASB10SinghalUASBUASBUASB6411。EGSBFuentesEGSBEGSBEGSB12。1.3UASBEGSB。Issiiκ－εUASB13。UASB14。MonodEGSBEGSB15－16。ABＲ17SPAC18－19。22.1UASBD/uLLm3/m3·dGm3/m3·dD/uL=0.0033L+0.045G+0.073。D/uLD/uL=0.088～0.09520。17ABＲ、ABＲABＲD/uL=0.07～0.1095HＲTABＲ。2.2EGSB。VupVup%=9.6305Vup－15.5669。D/uL=0.092～0.134EGSB21。SPAC。COD306kgCOD/m3/d15.3kg/m3/dCOD240kg/m3/d131kg/m3/d22。SPAC。SPAC23SPACD/uL＞0.2、D/uL=0.35～0.467D/uL≥0.2。D/uL=0D/uL=∞。。UASBD/uL＜0.1EGSBD/uL0.1SPACD/uL0.467。D/uL。31。UASBEGSB。2D/uLD/uL。D/uL0.1D/uL0.10.467。1CavinatoCFatoneFBolzonellaDetal．Thermophilicanaerobicco－digestionofcattlemanurewithagro－wastesandenergycropsComparisonofpilotandfullscaleexperiencesJ．Bioresour．Technol20101012545－550．2ＲodirguezDCBelmonteMPenuelaGetal．BehaviourofmolecularweightdistributionfortheliquidfractionofpigslurrytreatedbyanaerobicdigestionJ．Environ．Technol2011324419－425．3LeitaoＲCHaandelACZeemanGetal．TheeffectsofoperationalandenvironmentalvariationsonanaerobicwastewatertreatmentsystemsAreviewJ．Bioresour．Technol20069791105－1118．4LettingaGFieldJLierJetal．AdvancedanaerobicwastewatertreatmentinthenearfutureJ．WaterScienceandTechnology199735105－12．5ZoutbergGＲBeenP．TheBiobedEGSBExpandedGranularSludgeBedsystemcoversshortcomingsoftheupflowanaerobicsludgeblanketreactorinthechemicalindustryJ．WaterScienceandTechnology19973510183－187．6．J．1999023－6．7BarberWPStuckeyDC．TheuseoftheanaerobicbaffledreactorABＲforwastewatertreatmentareviewJ．WaterＲesearch19993371559－1578．8．SMPAJ．2004043－536．9DeCarvalhoKQSalgadoMTPassigFHetal．HydrodynamicevaluationofauasbreactorsubmittedtocyclicalflowratevariationJ．EngenhariaSanitariaEAmbiental2008132226－235．10NarayananCMNarayanV．MultiparametermodelsforperformanceanalysisofUASBreactorsJ．JournalofChemicalTechnologyandBiotechnology20088381170－1176．(下转第32页)3220146PdDPCδ－MnO2K－OMS－220。5DPC“100%”。1．M．1997860．2．－J．20032410760－764．3．M．2002137．4．J．20022225－29．5．J．20100435－37．6．J．200606528－532．7．TS－1J．200209423－427．8．MoO3J．200909853－8559．J．200324311－14．10HoYoungSongEunDuckPark．OxidativecarbonylationofphenoltodiphenylcarbonateoversupportedpalladiumcatalystsJ．JournalofMolecularCatalysisAChemical2000154243－250．11．J．200324311－14．12．P．CN02138－788．52003．13KingJrJosephA．MethodformakingorganiccarbonatesUS5132447P1992－07－21．14JoyceＲPKingJrPressmanEJ．MethodformakingaromaticcarbonatesUS5231210P．1993－07－27．15HirotoshiIshiiMeenakshiGoyalMitsuruUedaetal．OxidativecarbonylationofphenoltodiphenylcarbonatecatalyzedbyPddinuclearcomplexbridgedwithpyridylphosphineligandJ．JournalofMolecularCatalysisAChemical1999148289－293．16VavasoriATonioloL．Thepromotingeffectofchelatingligandsintheoxidativecarbonyla－tionofphenoltodiphenylcarbonatecatalyzedJ．JofMolCatAChemical200015134－45．17OkuyamaKSugiyamaJNagahataＲetal．JMolCatalA20032031/221．18．J．2008295489－496．19．Pd/CJ．2003319114－116．20．Pd/J．2009387檵檵檵檵檵檵檵檵檵檵檵檵檵檵檵檵檵檵檵檵檵檵檵檵檵檵檵檵檵檵檵檵檵檵檵檵檵檵檵檵檵檵檵檵檵檵檵檵檵728－732．(上接第7页)11SinghalAGomesJPraveenVVetal．AxialdispersionmodelforupflowanaerobicsludgeblanketreactorsJ．BiotechnologyProgress1998144645－648．12FuentesMScennaNJAguirrePA．AcouplingmodelforEGSBbioreactorsHydrodynamicsandanaerobicdigestionprocessesJ．ChemicalEngineeringandProcessingProcessIntensification2011503316－324．13．UASBJ．2007038－10．14LiuYHHeYLYangSC．ThesettlingcharacteristicsandmeansettlingvelocityofgranularsludgeinupflowanaerobicsludgeblanketUASB－likereactorsJ．BiotechnologyLetters200628201673－1678．15．EGSB1———J．2003013－7．16．EGSBⅡ—J．2003023－6．17．ABＲJ．199704317－20．18ChenXGZhengP．Flowpatternsofasuper－high－ratespiralanaerobicbioreactorJ．ActaScientiaeCircumstantiae2010305941－946．19ChenXGZhengPGuoYJetal．Flowpatternsofsuper－high－rateanaerobicbioreactorJ．Bioresour．Technol．2010101207731－7735．20．J．199502170－177．21．EGSBJ．2004025－9．22．SPACJ．2008081413－1419．23．J．201005941－946．