倒置A2O系统中碳氮磷的物料平衡分析

29420114HENANSCIENCEVol.29No.4Apr.20112011-02-230821023500041986-1967-.1004-3918201104-0480-04A2/O、、11221．4500022．450001A2/O、、、、.A2/OX505X502AUCT、A2/O、A2/OA2/O、、A2/O、、.、、[1].A2/ONO－3－N、NO－2－N、TP、、.1A2/O170000m3/d9d12dCOD220～280mg/LTN40～60mg/LTP6～8mg/L45％10％45％.80％20％.1A2/OFig．1OperationalconditionandtechnologicalflowoftheinvertedA2/Oprocess、、、.△△△荥荥荥荥荥荥荦荦△茳茳荥45%10%45%80%20%Q0QrQRQwS0.TNS0.NO3-NS0.CODS0.TPSa.TNSa.NO3-NSa.CODSa.TPSb.TNSb.NO3-NSb.CODSb.TPSc.TNSc.NO3-NSc.CODSc.TPSd.TNSd.NO3-NSd.CODSd.TPSR.TNSR.NO3-NSR.CODSR.TP2011422．1CODA2/OCOD3CODCOD、COD.2．1．1CODkg/dCODQ0－QwCODSd．CODCODoff＝Q0－QwSd．COD.12．1．2、CODCODCODCODNO3－NCODPAOCODaer1COD.CODYwVSS∶wCOD=g∶gμNO3－Nd－1YY0．34[2]μNO3－NμNO3－N=μmax.NO3－N·SS+Ks×SNO3SNO3+KNO3×KiO2KiO2+c′2μNO3－N0．18CODNO3－N=XB.H×V×μNO3－N/Y.3μmax.NO3－N2．6d－1Ks200mg/LKNO30．14mg/LKiO20．15mg/LXB.H.2COD.Smolders30mgHAc32mgCOD12．5mg38mg28．6mgPHB47mg[3]CODPAO=△SC.TP×32/47.4△SC.TP.3COD.Q0+Qr+QR×Sc.COD=Q0+Qr+QR×Sd.COD+△Sd.COD.5Sd.CODCODCODaer＝△Sd.CODCOD.CODCODbig=CODNO3－N+CODPAO+CODaer.62．1．3CODMLVSSCODfCV＝1．48[4]CODw＝Qw×XVSS×fCV7CODCODoutCODout＝CODoff＋CODbig＋CODw.8CODCODinCODin＝Q0×S0.COD.9COD98．7%COD.A2/O、、481--294COD1.2．232.2.1TNoffQ0－QwTNSd.TNTNoff＝Q0－Qw×Sd.TN.102.2.2TNwfN[5]MLVSSTNfN＝0．10TNw＝Qw×XVSS×fN.112.2.3TNdenitTNTNanoxTNanaerTNanoxTNanaerTNdenit＝TNanox＋TNanaer＝△Sa.NO3-N＋△Sb.NO3-N＋△Sc.NO3-N.12NOx－NSNDSNDTNTNSND.TNout＝TNoff＋TNw＋TNdenit＋TNSND13TNin＝Q0×S0.TN.14TN92．6％2.2．3TP2.3.1kg/dTPQ0－QwTPSoffTPoff＝Q0－Qw×Soff＝46．6.152.3.2TPwkg/dSofffp0．04871mgVSS0．0487mgTP.TPw＝Qw×fp×X＝4538×2060×0．0487×0．65＝295．7916TPkg/dTPout＝TPoff＋TPw＝342．3917TPkg/dTPin＝Q0×S0.TP＝433．7.183.TP78．9％.2．412CODTNTNNO2CODCOD.COD/kg·d-1187873564400600306689891568244．23/％10019．62．13．116．347．810．21．31CODTab.1ThedistributionfortheremovalquantityofCOD2Tab.2ThedistributionfortheremovalquantityofTN/kg·d-137111044113328422607．38922．8273/％10028．13．08．811．416．424．97．43Tab.3ThedistributionfortheremovalquantityofTP/kg·d-1433．746．6295．7991．51/％10010．768．221．1482--20114.pH7．0~7．3＜0．1～0．15wBOD/wMLSS·dDO0．5mg/L、、COD、、COD..3..CODVFA、、pH.CODVFVpH7～7．51．5mg/L0．5mg/L.2.1、2.31COD、、A2/O.2.1NowakO．ParameterestimationforactivatedsludgeModelswiththehelpofmassbalancesJ．WaterScienceTechndogy1999394113-120．2UdoWiesmannInSuChoiEva-MariaDombrowski.M．2009182-185．3SmoldersGJF.Astructuredmetabolicmodelforthean-aerobicandaerohicstoichiometryofthebiologicalphosphorusremovalprocessJ．BiotechnologyandBioengineering199547277－287．4EwaLie．Carbonandphosphorustransformationsinafull-scaleenhancedbiologicalphosphorusremovalprocessJ．WaterResearch199731112689-2693．5WentzelMCUbisiMFEkamaGA．HeterotrophicactivebiomasscomponentofactivatedsludgemixedliquorJ．WaterScienceTechnol1998374/579-87．AnalysisofMaterialBalanceonCarbonNitrogenandPhosphorusinInvertedA2/OProcessHaoXiaoxu1GaoJianlei1LiSheng2GaoAihua21．CollegeofWaterConservancyandEnvironmentalEngineeringZhengzhouUniversityZhengzhou450002China2．ZhengzhouSewagePurificationCompanyZhengzhou450001ChinaAbstractBasedontheanalysisoncarbonnitrogenandphosphorusineachbiologicaltreatmentunitandthesecondarysedimentationtankoftheinvertedA2/Oprocessinamunicipalsewagetreatmentplantamassbalanceformulawasestablishedthematerialflowofcarbonnitrogenandphosphoruswereresearchedandtheremovalefficiencyofnitrogenandphosphoruswereanalysed．Theresultsshowedthatthesimultaneousnitrificationanddenitrificationwasexistedinaerobicpoolandlessaerationcannotonlyimprovetheremovalefficiencyofnitrogenandphosphorusbutalsosaveenergy．KeywordsinvertedA2/OcarbonCnitrogenNphosphorusPmaterialbalanceA2/O、、483--