页数:32页文件大小:8.92 MB来源: 环境工程学ppt课件
本课件讲解物理化学处理法中的膜分离技术,介绍膜的定义、性能评价指标与按驱动力划分的膜过程,比较微滤、超滤、纳滤与反渗透的截留特性,并结合超滤膜的微观结构与膜污染控制说明其在纯水制备与废水回用中的应用。
物理化学处理法膜分离
Conventional:Physical-chemicalProcessRawWaterRapidMixCoagulation/FlocculationSedimentationFiltrationDisinfectionDisinfectionAdditionCoagulantAdditionResidualDisinfectionAdditionToDistribution1Dis
MembraneModuleToDistributionResidualDisinfectionAdditionDisinfectionPermeateTankSmallareaRawWaterRawWaterTankEasytooperate2MembraneProcess
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IDEALMEMBRANEPermeateFeedDrivingForceREALMEMBRANEPhase1Phase2DefinitionofamembraneAmembranecanbedefinedasabarrier(notnecessarilysolid)thatseparatestwophasesasaselectivewalltothemasstransfer,makingtheseparationofthecomponentsinamixturepossible.4
∆E∆T∆c∆PElectrodialysisThermo-osmosisPervaporationMicrofiltrationElectro-osmosisMembranedistillationGasseparationUltrafiltrationMembraneelectrolysisVapourpermeationNanofiltrationDialysisReverseosmosisDiffusiondialysisAdrivingforcecanmakethemasstransferthroughthemembranepossible;usually,thedrivingforcecanbeapressuredifference(∆P),aconcentrationdifference(∆c),anelectricalpotentialdifference(∆E).Membranescanbeclassifiedaccordingtheirdrivingforces:6DrivingForces
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WaterpassesSaltspassMacromoleculespassSolidParticlesreturnMicrofiltrationTypicalRetentatesSolidsKaolin,silica,yeast,bacteria,‘mud’,granularstarch,pigments8NominalPoreSize:0.1um
UltrafiltrationSaltspassWaterpassesMacromoleculesreturnSolidparticlesreturnTypicalRetentatesMacromoleculesproteins,polyvinylalcohol,gelatinizedstarch,pectin,disperseddyes9NominalPoreSize:0.01um20000MWCO
NanofiltrationSomesaltspasssomereturnWaterpassesMacromoleculesreturnSolidparticlesreturnTypicalRetentatesSalts(smallmolecules)sodiumnitrate,sugar,solubledyes,aminoacid10NominalPoreSize:250MWCO
SaltsreturnWaterpassesMacromoleculesreturnSolidparticlesreturnReverseOsmosisTypicalRetentatesDissolvedionssodium,chloride,macromolecules11
MembraneShapeFlatmembraneTubemembraneHollowfibermembrane12
MembraneMaterials1.PolymericmembranesPhaseinversion2.CeramicmembranesStretchingTrack-etchingAnodec,anodicoxidationUSFilter,sintering(surface)(crosssection,upperpart)13MF
crosssectionsurfaceSymmetricceramicmembrane(Al2O3)MembraneMorphologyorStructureTheactivelayerissupportedovertheporouslayer.Theactivelayerissupportedovertheporouslayer.Cross-sectionofanasymmetricPSmembraneThecrosssectionshowsauniformandregularstructure14
AcasedescriptionofUFmembraneUFmembranefromLitreeCompany15Micro-structureAsinglemembraneMembranemoduleinlab-scaleMembranemoduleinfull-scale
AcasedescriptionofUFmembraneMicrostructure(SEM)Internalsurface16Internalcross-section
AcasedescriptionofUFmembraneMicrostructureAFM17
AcasedescriptionofUFmembraneAsinglemembraneMembranemoduleinlab-scaleMembranemoduleinfull-scale18
AcasedescriptionofUFmembraneMembranesystem19
AcasedescriptionofUFmembraneMembraneprocess20
AcasedescriptionofUFmembranetime,tflow,JRpRaRmRgRcpporousmembranegellayermPRRcJMembranefouling21
permeatepermeatepermeatepermeateJtRestorablefluxwithphysicalcleaningIrreversiblefoulingstartingpointsMethodstoreducefoulingAcasedescriptionofUFmembraneflushingbackwashingFlushing-backwashingpermeatepermeate22
UF&ROforPureWaterAcasedescriptionofUFmembrane23
TapWaterUFSystem24FiltrateAcasedescriptionofUFmembrane
AcasedescriptionofUFmembraneROSystem25
AcasedescriptionofUFmembrane26UF&ROforPureWater
UF&ROforReuseofElectroplantingWastewaterAcasedescriptionofUFmembrane27
AcasedescriptionofUFmembrane28UF&ROforReuseofElectroplantingWastewater
AcasedescriptionofUFmembrane29UFsystemforsurfacewatertreatment
VFD2CV10CV3CV4CV6CV9CV1PermeatetankRawwatertank10%FeCl3P1UMFIBVBPRVFD1YPRRawwaterLSLSFTFIPILSPTPITMPIPIFTCMPHTMTIPIPTSVCV2LSLSLSP2P4P3CV7LSChemicalcleaningtankCV8CV5VFD310%NaClO30%-45%NaOH35%HClAcasedescriptionofUFmembraneUFsystemforsurfacewatertreatment30
Questions?31
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