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82017－04－072016102250112013E541994—1961—。MBＲ150040MembraneBioreactorMBＲ、。MBＲMBＲHＲT10h0．6m3/h93minCOD、、94．0%、96．5%、30．0%96．8%1TMP45．5kPa。。95．3%。X703A1008－021X201708－0181－06ExperimentalStudyonOptimizationofMBＲOperatingConditionsZhangBaoyiLiangQianweiPanNingyuanGuoYingQinWangyunWuYingxuLiYongfengNortheastForestryUniversityHarbin150040ChinaAbstractBioreactorMembraneMBＲisanewtypeofwastewatertreatmenttechnologywhichcombinestheactivatedsludgeprocesswithmembraneseparationtechnology．EffectofoperatingconditionsontheperformanceandmembranefoulingofMBＲoperationresultsshowthattheMBＲinHＲTwas10haerationintensitywas0．6m3/htogettheidealpumpingtimeratioof93minundertheconditionsofCODammonianitrogentotalphosphorusandturbidityaverageremovalratereached94%96．5%30%and96．8%respectivelyafter1monthsofoperationofTMPisabout45．5kPa．Althoughtheremovalefficiencyofpollutantsishighmembranefoulinghasnotbeensignificantlyimproved．Membranepollutedbytapwatercleaninghotwatercleaningwashingandsoakinginethanolandsodiumhypochloritebackwashcleaningthemembranefluxcanberecoveredto95．3%ofthenewmembranecleaningmethodseffectivelyprolongtheservicelifeofmembranecomponents．Keywordsmembranebioreactormembranefoulingoperatingconditions1MBＲ。MBＲ、。。2。。MBＲ。。MBＲ、、。11．1MBＲ1。、、、、、。70cm×52cm×53cm125L。11．2·181·MBＲDOI:10.19319/j.cnki.issn.1008-021x.2017.08.0711．2．11．2．1．2PVDF460mm×320mm×5mm0．2μm0．61．1mm1m210L/m2·h17cm13cm。1．2．1．310g/L50L。、NH4ClKH2PO4、NaHCO3pHCOD300～400mg/LNH+4－N30～40mg/LpH6．5～8．0。1．2．21。1CODCOD507－1UV1000PH100IC1010FA2004pHPHS－25CHX－6850DGYD100～1000SX2－2．5－10JBP－607HI9870379－1XMTD－2002MD－S800V1．31．2．3、50L、NH4Cl、KH2PO4。1h。1、。1．4COD300～400mg/L30～40mg/L20℃HＲT、。HＲT91011h0．20．40．60．8m3/h63、93、123min。MBＲ1MBＲ。22．1HＲTHＲT、、3HＲT。2．1．1HＲTHＲTMBＲ2。2HＲTCOD·281·SHANDONGCHEMICALINDUSTＲY2017468HＲT9h、10h11hCOD84．63%、90．09%90．93%。CODHＲTHＲT9h10hHＲT11h。HＲT。HＲT。2．1．2HＲTHＲT3。3HＲT3MBＲCODHＲT。HＲT9h10h86．93%92．22%HＲT1h。HＲT10h11h92．22%92．56%。HＲT。2．1．3HＲTTMP。5～50kPaTMP50kPa。MBＲTMP。4HＲT。4HＲTHＲT9h15dTMP44．1kPaHＲT。HＲT1h15dTMPHＲT9h10．2kPa。HＲT11h。HＲT10h。4HＲT2．2MBＲ4。2．15COD。5COD5COD。0．20．40．60．8m3/hCOD71．4%、86．5%、95．4%、95．4%COD。0．8m3/h0．6m3/h10d。0．6m3/hCOD93．6%～95．4%。2．26COD。0．6m3/h95．82%97．3%。0．2m3/h·381·MBＲ84．5%。0．8m3/h90%。62．376d0．2m3/h13dTMP50kPa。0．8m3/h6d。0．6m3/h。72．43min。2．4．18COD。6393minCOD94．31%94．62%。12minCOD86．6%。93minCOD。8COD2．4．29。63min97．5%95．4%～97．5%。9min95．1%。12min90．0%～92．5%。93min。92．510。。6min9min6dTMP·481·SHANDONGCHEMICALINDUSTＲY201746832．5KPa35．2KPa。12min15dTMP45．5KPa。。1063939min3min。2．6MBＲHＲT10h0．6m3/h93min。1MBＲ5d2。102MBＲ/%COD/mg/L375．00±25．0018．25±0．5693．43～95．51/mg/L37．50±2．500．94±0．0896．21～97．35TP/mg/L8．45±0．836．05±0．7421．54～42．78/NTU8．75±0．270．20±0．0696．23～97．12TMP/kPa45．5±3．521COD93．43%96．21%。MBＲ。TMPTMP9．2kPa145．5kPaTMP5～50kPa。MBＲ。2．6．1。PVDF10kPa20℃167mL/min1。33．9mL/min20．3%。5%～7%24h95%。11。1111·581·MBＲ95．3%。。3MBＲMBＲ1HＲT10hHＲT11hHＲT10hHＲT10h0．6m3/h93min。2HＲT10h0．6m3/h93min1COD、、、94%、96．5%、30%96．8%TMP45．5kPa。MBＲ150kPa。3。33．9mL/min159．2mL/min95．3%。1AileenNAlbertS．AMini－reviewofmodelingstudiesonmembranebioreactorMBＲtreatmentformunicipalwatersJ．Desalination20072121－3261－268．2StrandSEHaremGStenselH．Activated－sludgeyieldreductionusingchemicaluncouples．Waterenvironmentalresearch199971445－48．3．MBＲCODJ．2015412100－101．4．M．3．2008302－305．．MBＲJ．20174608179－184．檲檲檲檲檲檲檲檲檲檲檲檲檲檲檲檲檲檲檲檲檲檲檲檲檲檲檲檲檲檲檲檲檲檲檲檲檲檲檲檲檲檲檲檲檲檲檲檲………………………………………………………………………………………………………………………………………………………………………………、、………………………………………………………………………………《》………………………………………………………………………………………………………………………………………·681·SHANDONGCHEMICALINDUSTＲY201746