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当前位置:首页 > 商业/管理/HR > 质量控制/管理 > 生物倍增工艺实际生产运行工况优化探讨-田海宁
1231.3003842.1500903.300040。0.02~0.05kgCOD/kgMLSS·dCODCr69.8mg/L65.9%0.06kgCOD/kgMLSS·d100%SVI50~70C/N。C/NX703A1673-9353201206-0023-04doi10.3969/j.issn.1673-9353.2012.06.007Discussiononoperationoptimizationofbio-doublingprocessforpracticalapplicationTianHaining1ZhouChengjin2HeWenjie31.DepartmentofEnvironmentalandMunicipalEngineeringTianjinInstituteofUrbanConstructionTianjin300384China2.SchoolofMunicipalandEnvironmentalEngineeringHarbinInstituteofTechnologyHarbin150090China3.TianjinWaterworksCroupCo.Ltd.Tianjin300040ChinaAbstractThepracticalefficiencytotreaturbansewagewasinvestigatedbybio-doublingprocess.Theresultsshowedthatthelowsludgeloadingoperationof0.02to0.05kgCOD/kgMLSS·dwasnotbeneficialtothestableremovaloforganics.TheeffluentCODCrwas69.8mg/Lwiththeaverageremovalrateof65.9%only.Sludgeloadingshouldbemaintainedgreaterthan0.06kgCOD/kgMLSS·datleastinordertofitthedischargestandardrequirement.Theremovalrateofammonianitrogenwas100%.SludgesettleabilitywasgoodandSVIvaluewaskeptstablyfrom50to70.HoweverlowC/Nratioofinfluentformedthemajorconstraintforsimultaneousremovalofnitrogenandphosphorus.Measuresofaddingcarbonsourceandauxiliarychemicalremovalofphosphoruswereproposedforimprovingtheremovalofnitrogenandphosphorustofitthedischargestandards.Keywordsbio-doublingprocessBDPurbansewagesludgeloadingC/NBio-DoublingProcessBDP1。BDP①、、、②③④⑤·32·66201212WATERTECHNOLOGYVol.6No.6Dec.20121Fig.1DiagrammaticlayoutofBDP。《》GB18918—2002。+。1.0×104m3A、BBDP。BDP。1CODCr≤400mg/LBOD5≤200mg/LSS≤200mg/LNH3-N≤35mg/LTN≤45mg/LTP≤5mg/LCODCr≤60mg/LBOD5≤20mg/LSS≤20mg/LNH3-N≤8mg/LTP≤1mg/L。《》GB18918—2002B。BBDP。B5000m3/d。44.1m×13.2m×6.2m5.7m3318m3。、、。18.0m×6.0m22.4m×6.0m1.2m×6.0m42.9m×6.0m。1。BDP1。1BDPTab.1DesignandoperationalparametersofBDPHRT/hF/MkgCOD·kg-1MLSS·dSRT/d/℃pHMLSS/g·L-1DO/mg·L-1BOD/CODC/N16≥306~95~80.320~210.02~0.0621~257.3~7.75~80.3~0.40.52~62HRT、DOF/MC/N。2011822—1020800。MLSS、MLVSS、CODCr、BOD5、NH3-N、TN、TP、SS、SVI2DOHACH-HQ30dJNOECXSP-24N。33.1CODCrCODCr2。CODCr70%~90%80%CODCr44mg/LB。8—9MLSS7.0~8.3mg/L0.02~0.05kgCOD/kgMLSS·dCODCr。2CODCrFig.2EffectofsludgeloadingonremovalrateofCODCrBDP。。10·42·662012121—13CODCrCODCr69.8mg/L65.9%。1020.06kgCOD/kgMLSS·dCODCr。0.06kgCOD/kgMLSS·d。3.2SS3。SSF/M、。F/MSS。3F/M0.03~0.06kgCOD/kgMLSS·dSS20mg/LF/M。3SSFig.3EffectofsludgeloadingonSSSVI4。4SVIFig.4EffectofsludgeloadingonSVI4SVI50~70mL/g。。BDPDO。3.35。0.004~0.013kgCOD/kgMLSS·d。80%~100%。BDPSRT。5Fig.5Effectofamminianitrogenloadingonremovalofamminianitrogen3.4C/NTNTPC/NTNTP6。6C/NTNTPFig.6EffectofC/NonremovalofTNandTP6C/N3~550%~70%·52·2012126640%~60%。C/N8~15。F/M3。。4①。②CODCODCrCODCr69.8mg/LCODCr65.9%0.06kgCOD/kgMLSS·d。③100%。C/N。1.D.2005.2《》.4M.2002.3.A/OJ.200521980-82.1987-。E-mailtianwell@sina.com2012-10-2422J.201127771-74.4.M.2009.5.J.20072323104-108.6.J.200827116-19.7.J.2011402343-345.8.J.200726346-48.1987-。E-mailliuwei619813@163.com2012-07-23·62·66201212
本文标题:生物倍增工艺实际生产运行工况优化探讨-田海宁
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