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215001A2/OSBR。。DPBCOD/TP、DO、MLSSSRT。、。X703A1000-4602201107-0026-04StudyonBiologicalPhosphorusRemovalinImprovedIntegratedAlternativeReactorWUWei-gangSuzhouDrainageCo.Ltd.Suzhou215001ChinaAbstractImprovedintegratedalternativereactorcombinesA2/OprocessandSBRprocessandachievesgoodnitrogenandphosphorusremovalwithcompactstructurearrangementandlowrunningcosts.CombinedwiththeproductionoperationofLoujiangWWTPinSuzhoutheoperationconditionsofthereactorforachievinggoodphosphorusremovalwereinvestigated.Theresultsshowthatadequateni-tratenitrogentoprovideelectronacceptorsforDPBsiscrucialtoimprovedenitrifyingphosphorusremovalefficiency.AtthesametimeCOD/TPratioininfluentDOinaerobictankMLSSandSRTaremainfactorsaffectingbiologicalphosphorusremoval.Inadditionfornon-idealphosphorusremovalefficiencyduetolow-loadoperationinrainyseasonthecorrespondingmeasuresareproposednamelyreducingaerationratedecreasingrecycleratiofromaerobictanktoanoxictankoraddingflocculantsforchemicalphosphorusremoval.Keywordsimprovedintegratedalternativereactorbiologicalphosphorusremovaldenitrif-yingphosphorusremovalgradualaeration1UNI-TANK、。、、。15、、/。8h4h1h。·62·27720114CHINAWATER&WASTEWATERVol.27No.7Apr.20111Fig.1LayoutofintegratedreactorFEAABC。B。B、CCAB。B、C。BC。。2。2Fig.2Flowchartofimprovedintegratedreactor21250m3/dHRT23.3h、、1∶4.4∶7.4F/M0.14kg-BOD5/kgMLSS·d15d1.0kgMLSS/kgBOD5300%。2009GB18918—2002B。。22.1、、TPTP。TP4.22mg/L1.34mg/L68.2%0.35mg/L91.7%。TP74.4%25.6%。DPB。、350%O2NO-3-NO2。。NO-3-NNO-3-NPO3-4-P。NO-3-N>5mg/LPO3-4-P>60%NO-3-N3mg/LPO3-4-P40%。DPB。200%~300%。2.2COD/TPCOD/TP。3COD/TPTP。3COD/TPTPCOD/TP32112TP1.08mg/L0.2mg/LCOD/TP50TPCOD/TP<50TP·72·.watergasheat.com277TPCOD/TP>50TPCOD/TP>80TP90%。TP。3COD/TPTPFig.3InfluenceofCOD/TPratiooneffluentTP2.3DODO。DODODONO-3-N。1DO。1Tab.1Influenceofaerationmodeonbiologicalphosphorusremoval1231#2#3#DO/mg·L-13.882.621.313.602.441.02DO/mg·L-10.980.760.230.260.91.22.52.4/%74.581.671.187.4/mg·L-1TP1.030.871.160.49TN10.49.9713.28.76NH3-N2.043.034.712.0910d1#、2#、3#、。DODO。DODOTPDO。。DODO61.85mDODO3.0~4.5mg/LDO2.0~3.0mg/LDO1.2mg/L。DODO。2.4SRT、MLSS。MLSSSRT5、8、10、12、14、16d。4。4MLSSFig.4InfluenceofSRTandMLSSinanaerobictankonphosphorusremoval45~8d8d·82·277.watergasheat.comSRT8d51.2%14d77.6%SRT14d。SRT10~14d。MLSS。MLSS。DO2~3mg/LMLSS2.5g/LTP0.5mg/LMLSS<2.0g/LTP。SRTMLSSSSSRTMLSS。2.5。2C/P50%。DODOPHBPHB1。PHB。。2Tab.2Comparisonofindexesbetweenrainyandnon-rainyseasonDO/mg·L-1C/P/104m3·d-1TP/mg·L-1/%0.5~1.5≤0.540~8012~140.2~0.680~952.0~4.00.5~1.020~40≥140.8~1.565~80TP0.2~0.5mg/L≤2d。、TPB3~5d。3①。COD/TPCOD/TP>80TP90%。②DODO。③C/PDO、。④。5~8dSRT10~14dMLSS2.5g/LTP0.5mg/L。1.J.200218783-85.1982-。E-mailchenwu1017@yahoo.com.cn2010-11-18·92·.watergasheat.com277
本文标题:改良型一体化交替反应池工艺的生物除磷研究吴魏刚
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