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56Vol.5No.620116ChineseJournalofEnvironmentalEngineeringJun.2011--SBR123111.4100032.4100823.410082、、-SBR。COD6000~7000mg/L、LAS600~650mg/LCODLAS76.4%77.1%、PAC。SBRCOD≤500mg/LLAS≤17mg/L92.4%92.4%。。SBRLASX703.1A1673-9108201106-1251-06Treatmentofhigh-strengthsyntheticdetergentwastewaterbyflyash-coagulationandSBRprocessLiRongxi1YangChunping23XuDifa1SongYong11.DepartmentofBiologicalEngineeringandEnvironmentalScienceChangshaUniversityChangsha410003China2.CollegeofEnvironmentalScienceandEngineeringHunanUniversityChangsha410082China3.KeyLaboratoryofEnvironmentalBiologyandPollutionControlHunanUniversityMinistryofEducationChangsha410082ChinaAbstractAimingathighlyconcentratedlowbiodegradabilityandhighlyloadcharacteristicsonthesynthet-icdetergentwastewateramethodfortreatingithasbeenstudiedusingflyashadsorptionandcoagulationwithpretreatmentandthenSBRprocessestreatment.TheresultsshowedthatatnormaltemperaturethedosagesofflyashandPACwerethemaininfluencingfactorsandthepretreatmentremovalratesofCODandLAScouldreachto76.4%and77.1%respectivelywhenCODwere6000~7000mg/LandLASconcentrationswere600~650mg/Linthewastewater.ThefinaleffluentconcentrationsofCODandLASwerelessthan500mg/Land17mg/LaftersequencingbatchreactorSBRtreatmentcorrespondingtothetotalremovalratecouldbeuptoover92.4%and97.3%respectively.Theeffluentcouldmeetthethirddegreeofsyntheticdetergentwastewaterrequiredandtheprocesscouldbesuitableforhigh-strengthsyntheticdetergentwastewater.KeywordsflyashcoagulationSBRLAShigh-strengthsyntheticdetergentwastewater507780662008013382008SK30042008C1412010-11-092011-01-201966~。E-maillirongxi1966@yahoo.com.cn12。LAS、23。LAS、。。。45、6-891011-13。COD、、、。5、、、、、1415。-、SBRLAS。11.1、、。LAS、、、。pH3.7~10.5COD6000~7000mg/LLAS600~650mg/L。SiO258.82%Al2O327.58%Fe2O38.43%CaO1.85%MgO1.32%SO30.38%。1.21.2.1SiO2SO3。《》16CODLASpH1.2.2200KDB-3721pHPHS-3DF-1101BMY3000-6B。SBRSBR1。SBR3.8L、2.3L0.6。SBR“—————”。1.3200mL500mL。H2SO4NaOHpH13100r/min20min1mLCODLAS。1SBRFig.1ExperimentalapparatusofSBRPAC120r/min10minPAM60r/min15min。CODLAS。-SBRCODLAS。22.12.1.1CODCOD200mL50、70、90、110、140、170200g2。2COD。170gCODLAS80.3%83%200gCODLAS0.7%3.8%。COD。30g110g25216--SBR2CODFig.2EffectofflyashdosageonCODremovalefficiency。3COD。。0.55g/mLCOD70%。2.1.2pHCODCODpHWpH1、5、11COD50%pHLAS17pH1170%18。pH9、10、11、121320min。1mLCOD3。3pHCODFig.3EffectofpHonCODremovalefficiencypH10COD60%。pHCOD。pH12~13LASLAS1819。pH13。2.1.3CODpH1310、20、30、4060min。COD4。4CODFig.4EffectofreactiontimeonCODremovalefficiency430minCOD65.4%。COD。30min。、—3。。30min。2.1.40.55g/mLpH1330minCODLAS63.1%。2.2-、、PAC11PAC、2035215PAC。COD2159.1mg/LLAS229.6mg/LPACPAC200、400、600800mg/L120r/min10min0.5%PAM5mg/L60r/min15min。5。CODLASPAC75%PAC400mg/L800mg/L2%。。PAC。PAC400mg/LCOD74.2%。5PACFig.5EffectofPACdosageonremovalefficiencyPAM0.5%PAM5mg/L。2.3--SBR-CODLASMLSSLAS3h。6Ⅰ、Ⅱ、Ⅲ、、SBR。SBR3h、21h、2h、0.5h、0.5h27hpH6.5~7.5。CODLAS92.4%97.3%SBRCOD485mg/LLAS17mg/L67.8%88.2%。917212217CODLAS91%~93%95%6--Fig.6Removalefficiencybytheflyashadsorptioncoagulationandaerobicbiologicalprocess1SBR2。91322COD6000~7000mg/LLAS600~650mg/LGB8978-1996--SBR。CODLAS。COD、LAS20h。SBR。31CODCOD。0.55g/mLpH1345216--SBR30min。2PAC400mg/L5%PAM5mg/LCODLAS76.4%77.1%。3--SBR。COD6388mg/LLAS629mg/L92.4%97.3%。1..2002ZhangTianshengLiMingrong.TreatmentTechnologyandItsApplicationsofCommodityChemicalWastewater.Bei-jingChemicalIndustryPress2002inChinese2..1994144296-301QiMenglan.StudiesonthetreatmenttechniquesofwastewaterfromsyntheticdetergentproductioninChina.ChinaEnvironmentalScience1994144296-301inChinese3.LAS.20044282-85JiangAnxiXiaBingLiYaxuan.AdvanceintreatingwastewatercontainingsurfactantsLAS.JournalofSafetyandEnvironment20044282-85inChinese4KallioinenaM.PekkarinenaM.MnttrviM.etal.Comparisonoftheperformanceoftwodifferentregeneratedcelluloseultrafiltrationmembranesathighfiltrationpres-sure.JournalMembraneScience20072941-293-1025BoonyasuwatS.ChavadejS.MalakulP.etal.Anionicandcationicsuffactantrecoveryfromwaterusingamulti-stagefoamfractionator.ChemicalEngineeringJoumal2003933241-2526ChenH.SabatiniD.A.Simultaneousuptakeofanionicsurfactantsandmicellar-solubilizedcontaminantsusingani-on-exchangeresins.WaterResearch200236820-627..20023721-24ChenFutaiChuYongqianWangShuguangetal.Studyontheflocculationperformanceofthenovelpolymericalu-minium-silicaflocculantusedinbathingwastewaterreuse.TechniquesandEquipmentforEnvironmentalPollutionControl20023721-24inChinese8NatasjaSchoutenLouisG.J.vanderHamGert-JanW.Euverinketal.Selectionandevaluationofadsorbentsfortheremovalofanionicsurfactantsfromlaundryrinsingwa-ter.WaterResearch200741184233-42419.SBR.200663107-109XiaLiangshuChenZhongqing.Onbiodegrationofdailychemicalwastewaterbyusingthesequentialbatchrectorprocessing.JournalofSafetyandEnvironment200663107-109inChinese10LeonV.M.LopezC.Lara-MartinP.A.etal.Re-movaloflinearalkylbenzenesulfonatesandtheirdegrada-tionintermediatesatlowtemperaturesduringactivatedsludgetreatment.Chemosphere20066471157-116611..200323155-57WuJiandongWangZhenyouZhouXingqiu.Discussionofthedesignfortheproductionwastewatertreatmentengi-neeringofthesurfactant.I
本文标题:粉煤灰混凝SBR法处理高浓度洗涤剂废水李荣喜
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