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当前位置:首页 > 商业/管理/HR > 公司方案 > UASB反应器处理高浓度蛋白质废水启动特性的研究叶芃铖
UASBUASBUASB、。88dUASB。COD7000mg/L2.00kgCOD/m3·dCOD80%。UASBup-flowanaerobicsludgebedUASBWageningenLettinga·G12070。UASB2~5。UASB6。UASB、。UASB-。。UASB。11.1UASB60mm120mm。580mm80mm2.8L。1。1UASB1.2。、、。1。1pHCODmg/Lmg/Lmg/Lmg/Lmg/LSSg/L4.5~7.66000~7000100~160300~380220~350400800~12001.31250%MLVSS10.52g/LMLVSS/MLSS0.61。1.41.4.1UASBUASB35℃。2000mg/LCOD80%1000mg/LHRT。VFAVFA200mg/LVFApH6.5~7.5。9820116UASBDOI:10.14127/j.cnki.jiangxihuagong.2011.02.0763.5d。1.4.2、pH、VFA3dCOD7dMLVSSMLSS10d。COD、pH、MLVSSMLSS7VFA、、889。22.1UASBUASB23。2COD3OLRCODCOD2000mg/LHRT3.5~4dCOD0.6kgCOD/m3·dCODCOD。。。10d50%。22dCOD80%0.53kgCOD/m3·d。092011223d。0.53kgCOD/m3·d1.87kgCOD/m3·d。COD。1.87~2.00kgCOD/m3·d、80%。110d88dHRT2.5~3d2.30~2.53kgCOD/m3·d50%COD75%HRT84hUASBHRT。2.2UASB4.4MLVSSMLVSS/MLSSMLVSS/MLSS。4MLVSS9.46g/LMLVSSMLVSS/MLSSMLVSS18.73g/LMLVSS/MLSS0.78。2.3UASB7d5。51920116UASBSchmidt100.14~5mm0.5mm。5<0.5mm38.6%11。<0.5mm16.4%。>2mm18.6%14.2%10。。2.4UASB。1020m/h18~50m/h50~100m/h。650d90d。650d90d60.5~1.0mm55.25~57.33m/h1.0~2.0mm80.02~83.65m/h>2.0mm89.48~91.36m/h。。>2.0mm。2.5UASB。MLVSS10g/L25mL100mLCOD2000mg/L。7。7。138mL40d17.95%。292011273UASB。1UASB。88d。COD7000mg/LHRT3.5d2.00kgCOD/m3·dCOD80%。2MLVSSMLVSS/MLSSMLVSS18.73g/LMLVSS/MLSS0.78。3<0.5mm38.6%16.4%。>0.5mm55.25~91.36m/h。4138mL。1Lettinga.G.VanVelsenAFMHobmaSWetal.UseoftheupflowsludgeblanketUSBreactorconceptforbiologicalwastewatertreatmentespeciallyforanaerobictreatmentJBiotechnologyandBioengi-neering198022699-734.2MajumderPSGuptaSK.Degradationof4-chloro-phenolinUASBreactorundermethanogenicconditionsJ.BioresourceTechnology200899104169-4177.3TawfikaASobheybMBadawyaM.Treatmentofacombineddairyanddomesticwastewaterinanup-flowanaerobicsludgeblanketUASBreactorfollowedbyactivatedsludgeASsystemJ.Desalination2008227123167-177.4SubramanyamRMishraIM.Co-degradationofresorcinolandcatecholinanUASBreactorJ.Biore-sourceTechnology200899104147-4157.5OktemYAInceOSallisPetal.Anaerobictreat-mentofachemicalsynthesis-basedpharmaceuticalwastewaterinahybridupflowanaerobicsludgeblanketreactorJ.BioresourceTechnology20089951089-1096.6ShowKYWangYFoongSFetal.Acceleratedstart-upandenhancedgranulationinupflowanaerobicsludgeblanketreactorsJ.WaterResearch20043892293-2304.7.M.2006.8..M.1998.9.UASBJ200930123630-3638.10SchmidtJEAhringBK.GranularsludgeForma-tioninupflowanaerobicsludgeblanketUASBreac-torsJ.BiotechnologyandBioengineering19963920116UASB49229-246.11GrotenhuisJTCKisselJCPluggeCMetal.Roleofsubstrateconcentrationinparticlesizedistribu-tionofmethanogenicgranularsludgeinUASBreactorsJWaterResearch199125121-27.CharacteristicsofStart-upPeriodinUASBReactorforTreatingProteinWastewaterYePeng-chengTheEnvironmentalProtectionBureauofShanggaoJiangxiAbstractThestart-upthecharacteristicsofgranularsludgeandthetreatmenteffectofanupflowanaerobicsludgeblan-ketUASBreactorundermid-temperaturewerestudiedwithhighconcentrationProteinwastewaterastreatingobject.Experimentresultsshowedthatitspent88daystostartupUASBbygraduallyincreasingtheinfluentProteinconcentra-tionandtheseedsludgewasthemixtureoftheinoculumgranularsludgeandthedigestionsludge.TheremovalrateofCODcouldreachabove80%whenthevalueofinfluentCODconcentrationwas7000mg/Landtheorganicloadingwas2.00kgCOD/m3·d.Granularsludgehasbeenobtainedinthereactorandthespecificmethanogenicactivityofthegranularsludgewaswell.KeyWordsup-flowanaerobicsludgeblanketproteinwastewateranaerobicgranularsludge4920112
本文标题:UASB反应器处理高浓度蛋白质废水启动特性的研究叶芃铖
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