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431420157GuangzhouChemicalIndustryVol.43No.14Jul.2015SBＲ(，315000)SBＲSＲT、。6hSBＲSＲT20dSBＲSBＲ。SBＲX703.1B1001－96772015014－0157－031971－。SBＲExperimentalStudyonSewageProcessingintheVillagesandTownsTAOPeiFENGPu－rongYINGShuai－ruiHUChen－jieZhejiangBusinessTechnologyInstituteZhejiangNingbo315000ChinaAbstractThisexperimentstudiedtheSBＲtreatmentsystematdifferenthydraulicretentiontimedifferSＲTsludgeageunderdifferenttemperatureconditionsofruraldomesticsewageremovaleffectoforganicmatternitrogenandphosphorus.Ｒesultsshowedthatconsideringtheeffectofnitrogenandphosphorusandtheprincipleofcombiningeconomichydraulicretentiontimeby6hwasreasonabletheoptimalSＲTSBＲreactorwas20d.TemperatureSBＲphosphorusremovaleffectwaslessaffectedSBＲreactorwasmoresuitablefordealingwithsewageatlowtemperature.KeywordsSBＲHＲTSＲT、1。SBＲ2－8、。11.1SBＲ。1。1Table1sewagemainwaterqualityindicatorsCOD/mg/LBOD5/mg/LNH3－N/mg/LpHTN/mg/LTP/mg/L200～30080～15035～506.5～7.560～1005～121.2UASBMLSS28.66g/LMLVSS20.56g/L。SBＲMLSS0.42g/LMLVSS0.25g/L。SBＲ4h6h、9h、12h。10dCOD、NH3－N、TNTP。2SBＲTable2SBＲsystemtestrunningparametersh1210.51.50.50.514212111632411194262111222.1HＲTSBＲ20℃HＲT4、6、912hSBＲCOD、NH3－N、TN、TP。1SBＲ。158201571SBＲFig.1CyclerunningtimeofSBＲreactorandtheeffectsofnitrogenandphosphorus1COD。4h、6h、9h12hCOD50mg/L《》GB18918－2002A。NH3－N。4hNH3－N9mg/LGB18918－200225mg/L6hNH3－N5.6mg/LGB18918－2002B9h12hNH3－NNH3－N＜5mg/LGB18918－2002A90%。TN。4hTN16.7mg/LGB18918－2002B6h、9h12h70%TN≤15mg/LGB18918－2002A。TP。4hTP65.1%2.3mg/L6h9h86.4%、90%TP1.0mg/LGB18918－2002B12h92.2%TP0.5mg/LGB18918－2002A。SBＲ6h。2.2SBＲSBＲ6hSBＲ15d20d。5～25℃SBＲCOD、NH3－N、TN、TP。SBＲ2。2COD。5～10℃70%10～15℃75%25℃85%。COD。NH3－N。5～10℃73%10～15℃81%25℃87%。TNTN。5～10℃50%10～15℃57%TN16.7mg/L25℃74%。TP。5～10℃85%TP1.0mg/L20℃91%。10℃GB18918－2002B。2SBＲFig.2TheeffectsofprocessingtemperatureofSBＲreactor2.3SＲTSBＲSＲTSBＲ3。3SBＲFig.3TheinfluenceofsludgeagetreatmenteffectofSBＲreactor3CODSＲT。SＲTCOD80%COD30mg/L《》GB18918－2002A。NH3－NSＲT。SＲT10dNH3－N53%SＲT15d79.5%SＲT20d84.6%NH3－N4.7mg/LGB18918－2002A。TNSＲT。SＲT10dTN41%SＲT15d60%TN17mg/LGB18918－2002BSＲT20d69%TN15mg/L。GB18918－2002ATPSＲT。SＲT10d15dTP4%SＲT15d20dTP3%。SＲT20dTP1.0mg/LGB18918－2002B。NH3－NTNSＲTNH3－NSＲT10d20d84.6%TNSＲT20d。SＲT10d(194)194201573Fig.3Compositecurves4Fig.4Grandcompositecurve5Fig.5heatexchangenetworkAspenEnergyanalyzer、、、。5AspenEnergyanalyzerAspenEnergyanalyzer。。1．M．198110－17．2．M．19914－12．3．M．20023－10．4．M．20091－5．5．《》J．20107280－282．6．AspenplusJ．201214檵檵檵檵檵檵檵檵檵檵檵檵檵檵檵檵檵檵檵檵檵檵檵檵檵檵檵檵檵檵檵檵檵檵檵檵檵檵檵檵檵檵檵檵檵檵檵檵檵173－174．(158)20d7%TP。SＲT20dGB18918－2002B。SBＲSＲT20d。3SBＲHTＲ6hSＲT20dSBＲ10℃GB18918－2002B。1．—M．200645－54．2．SBＲJ．200522130－34．3．SBＲJ．200324353－356．4．SBＲJ．200520320－23．5HarperW．F．Jr．ApplicationofanaerobicandaerobicActivatedSludgetoPhosphorus－DeficientWastewaterTreatmentJ．WaterEnvironmentＲesearch2005773234－245．6．A2/O－J．200723322－26．7TsunedaSatoshiOhnoTakashiSoejimaKoichietal．Simultaneousnitrogenandphosphorusremovalusingdenitrifyingphosphate－accumulatingorganismsinasequencingbatchreactorJ．BiochemicalEngineeringJournal2006273191－196．8Y．UbukataD．TomlinsonA．AddagadaA．Shafagati．FundamentalMechanismsofPhosphateＲemovalbyAnaerobic/AerobicActivatedSludgeinTreatingMunicipalWastewaterJ．EngineeringinLifeSciences20056151－56．