超滤在微污染水源水处理中的研究进展丁剑秋

　2009年6月第34卷第3期贵州化工GuizhouChemicalIndustry超滤在微污染水源水处理中的研究进展丁剑秋　祝亚男　蔡小琴　高建国(;,,550003)　　　　,,。　　X131.2　　　　A　　　　1008-9411(2009)03-0039-05　　,。、、(---)。,,[1],,。1　超滤技术1.1　MF(Microfiltration)、UF(Ultrafiltration)、NF(Nanofiltration)RO(ReverseOsmosis)。(1.1[2]),,;、、[1];;[3](1)。1　[3],,,,,,。1　1.2　:1);2)、[1.4-5]。,,,,,,。,,,[6-7],。BrinckJ.[8],pH,,。[9]。、,,·39·　贵州化工GuizhouChemicalIndustry2009年6月第34卷第3期。1.3　,。17,:a.,b.,c.,d.,f.。,。,;,。,、,。[10-13],,,,,,。(、),、,,。1.4　[1]。、、、。(1.2),、、,。1.2　,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,2　超滤在微污染水源水处理中的现状,、、,“”、[14-16],,、。,,。2.1　-UF,()、()()。:1.-;2.;3.。,,,(),,,。[17](MCR),:,MCR,0.1NTU;CODMn3mg/L;pH7.9-8.2。[18](),-,,0.1NTU,DOC2mg/L。[19]:,,0.2NTU,。Mierzwa.J.C.[20]Guarapiranga,:TOC、UV254、85%、56%95%,。2.2　-UF,-UF(),[21-22],,[16],[22]。。-UF。[23]-UF,0.08NTU,0.10mg/L,0.95mg/L,5,TOC0.26mg/L,CODMn0.77mg/L,0cuf/ml、0/L。·40·　2009年6月第34卷第3期　　　丁剑秋等:超滤在微污染水源水处理中的研究进展。MariaTomaszewska[24]:50mg/LPAC(),、36%、49%97%。[25]1:-UF、、UV254、、。()、。2.3　-()-UF、,,、,。[27]--,:,,CODMn65.8%,55.9%。Bhavanas.Karni[28]:-,85%,90%,85%,、50%。M.Has-gino[29]:O32mg/L5,,O3,O3。3　膜污染及防治措施3.1　、、,。,、,。6:、、、、、、、。[30]。,、,。:a.;b.;c.。Malogorzata。ChulWooJung[31]-:。Laine:-(=100000)、(=30000)(=100000),(=5000)。[32],,。[7]pH。[3]:,,,,4h。[33]:,。3.2　,,。:、。,,,XinjunChai,:。(、、、),[34]NaOH、NaClOH2O2,0.3g/lNaOH4h0.9%H2O22h,。,,。4　展　望,,,,20[35],,,,。·41·　贵州化工GuizhouChemicalIndustry2009年6月第34卷第3期,、。2　超滤在微污染水源水处理中的现状,、、,“”、[14-16],,、。,,。2.1　-UF,()、()()。:1.-;2.;3.。,,,(),,,。[17](MCR),:,MCR,0.1NTU;CODMn3mg/L;pH7.9-8.2。[18](),-,,0.1NTU,DOC2mg/L。[19]:,,0.2NTU,。Mierzwa.J.C.[20]Guarapiranga,:TOC、UV254、85%、56%95%,。2.2　-UF,-UF(),[21-22],,[16],[22]。。-UF。[23]-UF,0.08NTU,0.10mg/L,0.95mg/L,5,TOC0.26mg/L,CODMn0.77mg/L,0cuf/ml、0/L。。MariaTomaszewska[24]:50mg/LPAC(),、36%、49%97%。[25]1:-UF、、UV254、、。()、。2.3　-()-UF、,,、,。[27]--,:,,CODMn65.8%,55.9%。Bhavanas.Karni[28]:-,85%,90%,85%,、50%。M.Has-gino[29]:O32mg/L5,,O3,O3。3　膜污染及防治措施3.1　、、,。,、,。6:、、、、、、、。[30]。,、,。:a.;b.;c.。Malogorzata·42·　2009年6月第34卷第3期　　　丁剑秋等:超滤在微污染水源水处理中的研究进展。ChulWooJung[31]-:。Laine:-(=100000)、(=30000)(=100000),(=5000)。[32],,。[7]pH。[3]:,,,,4h。[33]:,。3.2　,,。:、。,,,XinjunChai,:。(、、、),[34]NaOH、NaClOH2O2,0.3g/lNaOH4h0.9%H2O22h,。,,。4　展　望,,,,20[35],,,,。,、。[1].[M].:,2004:2-18[2].[D].:,2006[3].[D].:,2004[4],.[J].,1992(6):1-10[5],.[M].:,1991:90-100[5],,.[J].,2006,31(4):25-29[6],,.[J].,2005,26(1):90-93[7],,.[J].,2008,29(10):2783-2787[8]BrinckJ.,JonssonA.S.,JonssonB..InfluenceofpHontheadsorptivefoulingofultrafiltrationmembranesbyfattyacid[J].JournalofMembraneScience,2000,164(1-2):187-194[9],,,.pH[J].,2006,26(2):41-44[10]MurphyEF,LuJR.Thereducedabsoptionofproteinsatthephosphorylcholineincorporatepolymer-waterinterface[J].Langmuir,1999,15:1313-1322[11],,.[J].,2004,55(5):747-751.[12],.[J].,1999,6:29[13],,,.[J].,2007,33(7):1-5[14]KunikaneS.,MagaraY.,TanakaO..Roleofmicrofiltra-tionandultrafiltrationindrinkingwatertreatment[J].Wa-terSupply,1996,14(3-4):473-47[15]PryorM.J.,Jacobs.E.P.,Botes.J.p..LowpressureultrafiltrationmembranesystemforpotablewatersupplytodevelopingcommunitiesinSouth[J].Desalination,1998,119(1-3):103-111[16],,,.[J].,2006,37(3):7-10[17].[D].:,2007(下转第47页)·43·　2009年6月第34卷第3期　　　陈湘娥:降低原油加工损失,提高工厂经济效益ReducingCrudeOilProcessingLossandImprovingEconomicBenefitsofFactoryChenXiange(SINOPECWuhanCompany,WuhanCity,HubeiProvince430082)Abstract:Reducingcrudeoilprocessinglossisthekeymeanstoincreasetheeconomicbenefitsoftheoilrefi-ningenterprise.TheprocessinglossofWuhanCompanyin2008isanalyzedinthisarticle.Themaincausesinflu-encingonprocessinglossarefound.Severalmeasuresforreducingprocessinglossareposed.Keyword:crudeoilprocessing;cause;measures(上接第43页)[18],,,.-[J].,2004,21(4):119-120[19],,.[J]..2006,26(2):56-59[20]Mierzwa.J.C.,Hespanhol.I,daSilva.M.C.C..Diertdrinkingwatertreatmentbyspiral-woundultrafiltrationmembranes[J].Desalination.2008,230(1-3):41-50[21],.-[J].,2007,25(1):34-37[22],,,.-[J].(),2005,33(6):777-780[23].--[D].:,2007[24]MariaTomaszewska,SylwiaMozia.Removaloforganicmat-terfromwaterbyPAC/UFsystem[J].Waterresearch,2002,36(16):4137-4143[25],,,.[J].,2002,18(2):1-4[26]..[D].:,2006[27],,,.-[J].,2005,24(2):70-72[28]Bhavanas.Karnik,et.a1.Fabricationofcatalyticmembranesforthetreatmentofdrinkingwaterusingcombinedozonationandultraliltration[J].Environ.Sci.Techno1.,2005,39:7656—7661[29]M.Hasginoetal.Pilotplantevaluationofanozone-moco-filtrationsystemfordrinkingwatertreatment[J].JournalofWaterScienceandTechnology,2000,41(10):17-23[30].[M].:,2000[31]ChulWooJung,LimSeokKang.ApplicationofCombinedCoagulation-UltrafiltrationMembraneProcessforWaterTreatment[J].KoreanJ.Chem.Eng.,2003,20(5):855-861[32].[D].:,2007[33].[D].:,2007[34].[D].:,2004[35]MihailKochubovski.UseofMembraneFiltrationforWaterTreatmentwithExamplesfromTheRepublicofMacedona[J].NanotechnologyToxicologicalIssuesandEnviron-mentalSafety,2007:193-205ResearchanddevelopmentofUFinmicropollutedwatersourcestreatmentDingjianqiuZhuyananCaixiaoqinGaojianguoChentong(CollegeofResourceandEnvironmentofGuizhouUniversity,Guiyang,Guizhou,550003;KeyLaboratoryofCarstEnvironmentalandGeohazardPrevention,MinistryofEdcua