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j2012/,,,2,2,3(l.,,518055;2.,,52300;3.,):,,,ZmL,sm,100L/(mZ.h)5dZKPa,2m10CNT/mL,UV25;6595%,c0DMll7198%,coD*0.5mL;3.smL,0.lmL,,,85%,,:;;;;1IO0nm,,[11,,[2],,[3],,,,,,,,,,,,,5,,,[el/,,1.1.1/120m3/d,,3mLl20121PH//mg.L-TUTab.1Qualityofrawwater}7.17.3414.118.146.77.4122COD/mL1V254jel/mg.L/mg.L,1.25~3.970035~0.0522.434.150.061~0.3241.21,,,24min,,,,Zm,10m/h,ZhPLC,()A12o:,6070nm,100,50m21.smL(A12O:)OZONIACFS3ZG,,OZONIAODI031rig.lFxowehartofPilotsealetreatmentProeess1.3:HAcH2100P;:GRlo0A(IBR);CoD:,Sinsehe88(TA88);UVZs4:HitaehiU30lo;:LCS/MS;:(TA~88);:(TA88);:,tachiU3010;:HAeHHQ10;:ozONEANAzERBMT964BT()20122.:¹;ºZmL;»21119/L,smL(11:1)5d,,100L/(mZ.h),4h,2105,2.1,,2,ZmLsmL5dSKPa3.SKPaZKPa,smL,,,[v],,,ZmL,,smL,,O,O,Zu{{{{{5111110,2Fig.2EffeetofozonedosageontransmembranePressure2.23,20122NTU,0.INTU,0.SNTU,GB574920064,2ml0CNT/mL;,210CNT/mL[8],50CNT11L,[91,,O,,2012:::::3Fig.3TheremovalofturbiditybytheintegratedtestingProeess25000000nUQUU,j.ld4Fig.4DistributionofPartielenumberineffiuentofmembraneunit2.35UV25;,UV25;0.0390.052cm,,UV25;1030%,Uv25;5%;,UV25;46.9%UV25;,UV25;0.0010.009em,COD6,COD23mL,CODMn530%,CODMn,COD*2040%,COD,;,CODMn20%,CODMn6090%,CoD0.5mL,,,,,CODMnUV25;6595%,CoDM70%,20120.0.050.0.0.01....,.,{}..(-~;5UV25;Fig.5TheremovalofLJV254bytheintegratedtestingProeess~~--~-~-~----~~---~,6CODFigTheremovalofCODbytheintegratedtestingProcess2.47,2.434.15mL,,,95%,70%4.786.77mL,4.57mgOmgNH3)[l0],,1113mL,3mL,,2012,;,0.lmL,GB574920060.5mL,95%(4mL),,8,0.0610.4mL,,,,,,;,0.0lmL9,,,ZmL;,3mL,,,0~3.0!0J1O7F19.7TheremovalofammoniabytheintegratedtestingProeessZFig.8Change5108ofNOZNeoneentrationduringnitrificationofammonia2012{g}Zn~Z;Z9Fig.9ChangeofNO3eoneentrationduringnitrifieationofammonia2.5(HAAs),,(DCAA)(TCAA)80%,2.0mL(HAAFP),10,HAAFP32.8%,DCAAFPHAAFP,TcAAFP,,HAAFPDCAAFPTCAAFPHAAFP84.4%74.0%83.2%,HAAFP85.2%,,10Fig.10TheremovalofHAFPbytheintegratedtestingProeess20123.l),,100L/(mZ.h),ZmL,smL,5dZKPa;,2m10CNT/mL,2),Uv2546595%,COD70%,85.2%;3mL,0.lm,GB574920063),,,,:[l],,.[Jl.,2007,l(5):1417.[2],,.[J].,2010,36(8):1115.[3],,,.[J].,2000,20(),6974.[4]SartorM.,SehiiehterB,GatjalH,etal.,DemonstrationofanewhybridProeessforthedecentraliseddrinkingandservieewaterProduetionfromsurfacewaterinThailand[J].Desalination,2008.222(l3):528540.[5]VanGeluwe5.,VinekierC,BobuE,etal.,EightfoldincreasedmembranefluxofNF27003oxidationofnaturalhumieaeidswithoutdeterioratedPermeatequality[J].JournalofChemiealTechnologyandBioteehnology,2010.85(11):14801488.[6,.[J].,2009,37(2):15128.[7],,.[J].,2009,29(l):1116.[8]NurMuhammad,RajibSinha,E.RadhaKrishnan,etal.,CeramieFilterforSmallSystemDrinkingWaterTreatmeni:EvaluationofMembranePoreSizeandImPortaneeofIntegrityMonitoring[J].JournalofEnvironmentalEngineering,2009,135(11):11811191.[9],,.[J].,2010,26(7):3033.[l01,,.[J1.,2008,59(9):23162321.:(1985),,,:Email::075526036759;:15999626650;:L201;:518055
本文标题:臭氧平板陶瓷膜新型净水工艺中试研究
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