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27420118JournalofHarbinUniversityofCommerceNaturalSciencesEditionVol.27No.4Aug.20112011-02-20.1978-.11231.3000512.2501013.475004A、B、、CODMn、UV254、NH3—N.GB5749-2006、、、、.X703A1672-0946201104-0574-05ContrastivestudyonoperationcapacityoftwoultrafiltrationcomponentsusedindrinkingwaterproducingWANGXu-yang1TANGKai-feng1ZHANGYan-ping2TONGZhi-qi31.TianjinMunicipalEngineeringDesignandResearchInstituteTianjin300051China2.ShandongMetallurgicalDesignInstituteCo.Ltd.Jinan250101China3.SchoolofEnvironmentandPlanningHenanUniversityKaifeng475004ChinaAbstractInordertoconfirmsuitableUFformorcomponenttwoUFcomponentsofdomes-ticfamousbrandstreateffluentofSFandAFrespectivelywereusedinconventionprocessandshortstagewaterproducingprocessinsuchaparalleltestmakingacomparativeanaly-sisonwater-qualityindexesofturbidityalgaeCODMnUV254NH3—NwhichshowednosignificantdifferenceofeffluentbothreachedalllimitindexesofGB5749-2006.Inpracti-calengineeringthefactorsasinitialinvestmentservicelifedamagedquantitybrokenwiresratematerialconsumptionenergyconsumptionandothersuitableUFformsshouldbecon-sideredfurther.Keywordsmunicipalwaterengineeringultrafiltrationsandleachairfloatation12009..、.11.1250m3/d.211.22.111.212.221/μm/mm/kPa/L·m-2·h-1/ntuAPVDF0.020.8/1.28040~80300BPVC0.011.0/1.620060~16050212/h/d/kPaA807030min25min+30s+10s24300×10-6NaClO3048B807030min28min+40s72200×10-6NaClO60252、、CODMn、UV254、NH3—N.2.110.24~0.49ntu0.36ntuA0.07~0.19ntu0.1ntu72.2%B0.08~0.22ntu0.12ntu66.7%.21.4~2.8ntu2.03ntuA0.09~-0.33ntu0.16ntu92.1%B0.09~0.19ntu0.12ntu94.1%.3~7.《》GB5749-2006≤1.0~7ntu《》CJ94-2005≤0.5ntu..AB.0.1ntu.·575·42.211.08~10.4/L0.64/LA360~1800/L864/L86.5%B360~1800/L1080/L83.1%.2.2~4.8/L3.56/LA3600~9000/L6240/L82.5%B1800~7200/L4671/L86.9%...AB.85%.2.3CODMn1CODMn2.24~2.88mg/L2.58mg/LA1.68~2.53mg/L2.25mg/L13.0%B1.76~2.46mg/L2.19mg/L15.4%.2CODMn2.8~4.4mg/L3.16mg/LA1.91~2.93mg/L2.46mg/L21.96%B1.83~3.34mg/L2.44mg/L22.86%.CODMn、CODMn.CODMn《》GB5749-2006≤3.0mg/L《》CJ94-2005≤2.0mg/L.12BA.8.82CODMn·675·272.4UV2541UV2540.043~0.0590.052AUV2540.039~0.0550.0496.6%BUV2540.042~0.0570.0504.5%.2UV2540.045~0.0590.052A0.042~0.0590.0513.26%B0.044~0.0560.0512.82%.UV254TOCTHMFP2.PVDFPVCUV254.AUV254B.9、10.2.5NH3—N1NH3—N0.02~0.3mg/L0.11mg/LA0.04~0.39mg/L0.16mg/L37.2%BNH3—N0.03~0.46mg/L0.15mg/L33.1%.2NH3—N0.10~0.40mg/L0.19mg/LA0.08~0.30mg/L0.17mg/L5.3%B0.10~0.32mg/L0.18mg/L4.8%.11、12.1NH3—N30%NH3—N.GB5749-20060.5mg/L.2NH3—N70%NH3—N5%.NaClONH3—N.NH3—N.·775·431.GB5749-2006、、、、.3.2、ABBA.BCODMnAAUV254B.NH3—NNH3—N.4.3A、.B.4、、5-6.1.—J.2007411-3.2.UV254J.200224261-65.3.21M.2003.4.J.201137127-33.5.J.20103631.6./J.2011273304-307323.57015NOOPHANPSRIPIBOONSDAMRONGSRM.Anaerobicammoniumoxidationbynitrosomonasspp.andanammoxbacte-riainasequencingbatchreactorJ.JournalofEnvironmentalManagement200990967-972.·875·27
本文标题:不同膜组件在净水工程中运行效能对比研究
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