您好,欢迎访问三七文档
当前位置:首页 > 商业/管理/HR > 质量控制/管理 > 常温条件下CAST工艺亚硝酸型硝化的实现及特性刘艳辉
57Vol.5No.720117ChineseJournalofEnvironmentalEngineeringJul.2011CAST121212312121241.3003842.3003843.1001244.980-8576CASTDO0.13~0.74mg/LDO0.7~3.36mg/L1.5h。14℃NO2-N90%TN68%SVI105NH4-N8mgNH4-N/gMLSS·h6mgNH4-N/gMLSS·h。X703.1A1673-9108201107-1454-05RealizationandperformanceofnitrificationvianitriteinCASTprocessatnormaltemperatureLiuYanhui12SunLiping12WangShaopo123LiuYuan12YuJingjie12LiYuyou1241.DepartmentofEnvironmentalandMunicipalEngineeringTianjinInstituteofUrbanConstructionTianjin300384China2.TianjinKeyLaboratoryofWaterQualityScienceandTechnologyTianjin300384China3.CollegeofEnvironmentalandEnergyEngineeringBeijingUniversityofTechnologyBeijing100124China4.TohokuUniversitySendai980-8576JapanAbstractSimulateddomesticsewagewastreatedthroughthecyclicactivatedsludgetechnologyCASTresultsshowedthatthroughaerationdurationcontrolpartialnitrificationwascarriedoutinalab-scaleSBRatnormaltemperaturewhenDOconcentrationrangedfrom0.13mg/Lto0.74mg/LandpartialnitrificationwasmaintainedforalongtimewhenDOconcentrationrisedto0.7~3.36mg/L.Accumulationrateofnitritewassteadilykeptover90%averagetotalnitrogenremovalrateofeffluentwas68%afterasludgeretentiontimethoughaccumulationrateofnitritewaslowandfluctuatedattheinitialexperimentalstage.TheSVIofthesystemwasabout105duringtheexperimentthesludgewasingoodsettlementnosludgebulking.Atthesametimeaccordingtothecomparionofnitrificationrateofnitrousnitrificationandcompletenitrificationammoniaoxida-tionratedroppedfrom8mgNH4-N/gMLSS·hto6mgNH4-N/gMLSS·h.InadditionpartialnitrificationcouldbetransformedintocompletenitrificationeventhroughaccumulationrateofnitritewassteadilykeptifaerationtimeandtheDOconcentrationwereunreasonablycontrolled.KeywordspartialnitrificationnormaltemperaturelowDOconcentrationammoniaoxidationrate50808128“”2008ZX07209-006200904601822010-03-162010-04-131985~。E-mailliuyanhuijiayou@126.com25%40%12。、、7CAST34。AOBNOB56。。DO。78。CASTCAST。11.128.8L21.6L13.3%、、、、。。。pH、DO1。1CASTFig.1DiagramofCASTreactor1.2COD300mg/L。NH4-N50mg/LPO4-P5mg/L。NaHCO3NaHCO3600mg/L。。1.3CAST4、、。212h2h1h1h4h6。20%1。21h0~30min311.5h1h1h10.5h0.5h2。2。0~4210.2m3/h43243~480.1m3/h3dNO2-N>95%。490.2m3/hNO2-N。MLSS4000~5000mg/LHRT12hSRT21d14℃。2Fig.2OperationproductioninCAST1.49CODNH4-NNO3-NNO3-NN-1--PO4-PSV、SVIMLSSpH、DOWTW340i55415。23NH4-N、NO3-NNO2-NTNNO2-N。TN61.36%TNNO3-N2TN68.36%TNNO2-N。TNNO3-N。3Fig.3PerformanceofnitrogenremovalinCASTsystemunderdiferentconditions2NH4-NN02-N3d18>95%。0.2m3/hSVI105。NO2-NNO2-N90%NOBNOBAOBNOB10“”AOBNOBAOB。4~6。4Fig.4Nitrogenconcentrationofaerobiczoneinonecycleinconventionalmode5Fig.5Nitrogenconcentrationofaerobiczoneinonecycleduringtheprocessoftherealizationofpartialnitrification6Fig.6Typicaltransformationofnitrogenduringonecycleaftertherealizationofpartialnitrification65417CAST44NH4-NNH4-N0mg/LNO2-N0mg/L。5NH4-NNO2-N。NH4-N。NO2-N95%6630minNO2-N4.45mg/L2.55mg/LNO2-N1hNO2-N11.25mg/LNO3-NNO2-N90~120NO2-NNO3-N120min。120NH4-N0mg/LNH4-N120~150minNO2-NNO2-NNO3-NNO3-N。SBR。SBR4L3LSBR1h。NH4Cl50mg/LNH4-N、KH2PO4、NaHCO30.3m3/h0NH4-NMLSS4000mg/L。775minNH4-NNO3-N。7Fig.7Nitrogenconcentrationinnitrationactioninconventionalmode8Fig.8NitrogenconcentrationinnitrationactionaftertherealizationofpartialnitrificationNH4-N8mgNH4-N/gMLSS·h8120minNH4-N6mgNH4-N/gMLSS·hNH4-N880minNO2-N50%NOB。80NO3-N110NO2-N。31NO2-N90%。2TN61.36%TNNO3-NTN7541568.36%TNNO2-N。3NH4-N8mgNH4-N/gMLSS·hNH4-N6mgNH4-N/gMLSS·h。1VerstraeteW.PhilipsS.Nitrification-denitrificationprocessesandtechnologiesinnewcontexts.EnvironmentalPollution1998102S1717-7262TurkO.MavinicD.S.Preliminaryassessmentofashortcutinnitrogenremovalwastewater.Can.J.Civ.Eng.19866613600-6053..200840101552-1557ZhuGuibingPengYongzhenGuoJianhua.Biologicalni-trogenremovalwithnitrificationanddenitrificationviani-tritepathway.JournalofHarbinInstituteofTechnology200840101552-1557inChinese4RuizgG.JeisonD.ChamyrR.Nitrificationwithhighnitriteaccumulationforthetreatmentofwastewaterwithhighammoniaconcentration.WaterRes.20033761371-13775HaoXiaodiJosephJ.MarkC.M.Model-basedevalua-tionoftemperatureandinflowvariationsonapartialnitrifi-cationANAMMOXbiofilmprocess.WaterRes.200236194839-48496..200526163-67GaoDawenPengYongzhenWangShuying.Stabilityofshortcutnitrification-denitrification.EnvironmentalSci-ence200526163-67inChinese7GarrIdo-FernandezJ.M.MendezR.etal.Thecircu-latingfloatingbedreactorEffectofpaniclesizedistribu-tionofthecarrieronammoniaconversion.Wat.Sci.Tech.2000414-5393-4008.-.200016229-31YuanLinjiangPengDangcongWangZhiying.Short-cutnitrificationanddenitrification.ChinaWaterandWastewater200016229-31inChinese9.4.200210BlackburneR.VadiveluV.M.YuanZ.etal.De-terminationofgrowthrateandyieldofnitrifyingbacteriabymeasuringcarbondioxideuptakerate.WaterEnviron.Res.200779122437-24458541
本文标题:常温条件下CAST工艺亚硝酸型硝化的实现及特性刘艳辉
链接地址:https://www.777doc.com/doc-6546742 .html