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MBR100044。《》。MBR、、、。MBRSISI、、。MBR。MBR。。MBRX703A1000-4602201607-0014-1051578036“———”2015QuantitativeEvaluationofSustainabilityofMBRProcessHAOXiao-diLIJiCAODa-qiKeyLaboratoryofUrbanStormwaterSystemandWaterEnvironment<MinistryofEducation>andRandDCentreforSustainableWastewaterTreatmentBeijingUniversityofCivilEngineeringandArchitectureBeijing100044ChinaAbstractSustainabilityisacruxforthefuturedevelopmentofwastewatertreatmenttechnologies.EspeciallyundertheconditionwheretheParisAgreementconcerningclimatechangewassettleddownenergyconsumptionwilldeterminethefuturedevelopmentofsustainabletechnologiestoalargeextent.InthiscasetechnologyofmembranebioreactorMBRwhichhasbeendebatedextensivelyathomeandabroadhastobequantitativelyevaluatedtoconcludeacomprehensivebenefitontheirmeritsanddemer-itsineconomysocietyandenvironment.BasedonestablishinganevaluationindexmodelSIforthesustainabilityofMBRprocessescapitalandoperationalcostprocesses’effectandtheirreliabilityandresourcerecoveryandutilizationwereelaboratedandallrelatedparametersandtheirreasonablerangesintheestablishedmodelwereanalyzedandidentified.ThecalculatedresultsofthemodelrevealedthatthesustainabilityofMBRprocesseswasnotasgoodasconventionalactivatedsludgeprocesses.InotherwordsMBRisbasicallynotasustainableprocessasthehighenergyconsumptionandoperationalcosthavetotallyshieldtheirmeritsongoodeffluentqualityandsmallfootprint.·41·32720164CHINAWATER&WASTEWATERVol.32No.7Apr.2016KeywordsMBRprocessconventionalprocesssustainableindexquantitativeevaluationmembranefoulingoperationalenergyconsumption。MBR、、1234。MBR/、/、/35MBR67。MBRVarsseveld+25%8、。MBR、MBR。89。MBR、。1MBRSS≤5mg/LCOD、N、PSS。、、。MBR10①②、、③。MBR1SI1。SI=α·C+β·P+γ·E11Tab.1ParametersandtheirexplanationsinmodelSI1、2CPE、<1>1=1、αCαβPβγEγCCI、OCI、、、、、EQIMBRSSPRIPMILIMBR/ECIMBRORIMBR·51·.watergasheat.comMBR327α、β、γ2①α+β+γ=1②α≥0.2、β≤0.4、γ≤0.4。C、P、EMBR。1MBR1。ELI、ECI、ORI。LI=0.8MBR0.80.8ECI=3MBR33ORI=1MBR1MBR、。C、P、E1。ELIECIE=0.8+3/2=1.9MBR1.9。C、PE。12、i/l、m、n。SI=α·∑li=1Cil+β·∑mi=1Pim+γ·∑ni=1Ein2SIC、P、EMBR、。SI=1MBR、SI>1MBRSI<1MBR。SI=1MBR“、”8。21。MBRMBR>1=1<1SISI=琢·(li=1移Cil)+茁·(mi=1移Pim)+酌·(ni=1移Ein)琢茁酌CPE()()()1=11()MBRCCIOCIEQIPRIPMILIECIORIPCE1Fig.1Flowsheetofmodel’scalculationandevaluation2.1CPPPMBRNPV11MBRNPVTMBRCASC3、4。NPV=∑nt=0OCIt+CCIt1+it3C=TMBRTCAS4i———6%n———t———·61·327.watergasheat.com2.1.1CCIMBR。。MBR———。、、A2/O+MBR4300、3100、3300/m3MBR4100、3067/m3。3500/m32500/m312~14。2.1.2OCI、、、、、。MBR515。。MBR。MBRSRTMBR16。MBR。MBR。4017①Q≤5×104m3/dMBR>1.00/m3MBR3.00/m30.80/m3②Q>5×104m3/dMBR>0.70/m30.50/m318~20。2.1.3C5×104m3/dMBR3、4。224∶63015。2NPV3。2MBRQ=5×104m3/dTab.2InvestmentandpaybackofMBRandCASprocessesQ=50000m3/d/103/·m-3/·m-3/·m-3/103MBR17.51.001.100.100.182512.50.701.100.400.73003MBRNPVTab.3NPVofMBRandCASprocesses103MBR1-7.00-5.002-9.91-7.081~15-0.98751+6%t-0.10331+6%t16~300.18251+6%t0.731+6%t-9.338.283308280MBRNPV-9330。MBR1/41.5。MBR9015MBRC6。Q=5000~10000m3/d2MBRC。1.801.601.401.201.000.800.60/(·m-3)0.4001234567891011109876543210TMBR/(104m3·d-1)2MBRCFig.2TrendsofoperationalcostsandindexCofMBRandCASprocessesalongwithtreatedcapacities·71·.watergasheat.comMBR3272MBR。MBR10×104m3/dC4。C≥4。2.2P2.2.1EQIMBRSSCOD、N、PSRT2122。SSSS≤5mg/L8。MBRSS。C60H8O23N12P8N13%、P2.4%。MBRA2/OPAOspoly-PP10%8。MBRSSMBRN、P13%10%。MBR4523。4MBRTab.4OperationalconditionsinpartialWWTPswithMBRprocessesathomeandabroad/104m3·d-1NorthLasVegas11.40.1mgP/LTP0.3mgN/LNH+4-N、2011102mgN/LNH+4-N、2010YellowRiverGwinnettCo.8.30.3mgP/LTP1mgN/LNH+4-N、2011BallengerFrederickCo.7.63mgN/LTN0.3mgP/LTP、20135.00.5mgN/LNH+4-N、2010CoxCreekAnnArundelCo.4.53mgN/LTN0.3mgP/LTP、2013BroadRunLoudounCo.4.23mgN/LTN0.1mgP/LTP、2008Henderson3.40.2mgP/LTP0.1mgP/L10mgN/LTN、2012SpokaneCo.3.210mgN/LTN0.05mgP/LTP4—10、2012Redlands2.50.1mgN/LNH+4-N2004TraverseCity3.21mgN/LNH+4-N0.5mgP/LTP、2004GippslandTraralagonVIC1.54mgN/LTN1mgP/LTP、2011Clovis1.060.1mgN/LNH+4-N8mgN/LTN2009MBRN、P1EQI0.8。2.2.2PRIMBRMLSS、3。MLSS8~10g/L5。2425MLSSMLSS8~18g/L4·81·327.watergasheat.com。MBR。MBR1PRI1。2.2.3PMIMBR。MBR、。MBR1PMI0.9。2.3E2.3.1LIMBR2/3~1/24MBR1/3。FI0.6。。。。/ξ5。5/MBRξTab.5FootprintfactorsξofMBRprocessesindifferentareas/cities、1.00~1.401.40~1.801.80~2.101.40~1.701.70~2.102.10~2.401.60~2.002.00~2.302.30~2.67①②③ξ。MBRξ。LI5。LI=ξ·FI5FIMBR。/1≤ξ≤1FI。2.3.2ECIMBR2627①、28②DO=3~4mg/L。ECIAHP29、LCA29、30。/。31、、、、、、0.67、0.64、0.53、0.45、0.39、0.36、0.29kW·h/m3632。0.14~0.28kW·h/m30.19~0.36kW·h/m30.29kW·h/m3。MBR0.8~2.4kW·h/m333MBR3435。17MBR、ECI2~5。6Tab.6EnergyconsumptionindomesticWWTPs/104m3·d-1/kW·h·m-30.720.2831.20.2182.00.2323.40.395150.280500.150260.1621.40.255·91·.watergasheat.comMBR3277MBR、Tab.7EnergyconsumptioninsomeWWTPsbeforeandafterapplyingMBRprocesses/104m3·d-1/kW·h·m-3ECI20.300.702.3330.350.601.7130.210.653.102.3.3ORIMBR36。MBRSRT、。MBR/、。1ORI0.9。3MBRC、E、P2MBRSI。8。8Tab.8Relatedmodelparametersassociatedwithdifferentareasξ1ECIMBR3α0.2β0.4γ“、”0.4ξ2.67ECIMBR3α0.4β0.2γ“、”0.428MBRSI3。MBRQ≤10×104m3/dSI>1.8。α=0.2、β=0.4、γ=0.4>20×104m3/dMBRSI=1MBR8。/SIMBRSI≤1。MBR。5.54.53.52.5SI1.5012345678910(0.2,0.4,0.4)(0.4,0.2,0.4)(0.4,0.4,0.2)(0.2,0.4,0.4)(0.4,0.2,0.
本文标题:MBR工艺可持续性能量化评价郝晓地
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