CASS工艺中PAC强化除磷试验研究

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CASSPAC1111122221.4300742.528415CASS《》GB18918—2002A。PACCFDPAC。1/230min4mg/LPACTPA4mg/LPAC。CASSPACX703C1000-4602201609-0135-05PhosphorusRemovalEnhancedbyPACinCASSProcessandItsEffectonActivityofSludgeMADa1XIONGYa1LIUYan-peng1LIAng-ze1WANGZong-ping1OUWei-song2LIJian-hua2ZHONGYan-lin2HEWei-feng21.SchoolofEnvironmentalScienceandEngineeringHuazhongUniversityofScienceandTechnologyWuhan430074China2.XiaolanWaterCo.Ltd.Zhongshan528415ChinaAbstractCyclicactivatedsludgesystemCASSwasappliedinasouthernsewagetreatmentplantbutthetotalphosphorusineffluentcouldnotmeetthefirstlevelAcriteriaspecifiedintheDis-chargeStandardofPollutantsforMunicipalWastewaterTreatmentPlantGB18918-2002inwinter.TheeffectofPAConenhancingphosphorusremovalandtheactivityofsludgewasinvestigatedbythesimulationofCFD.Theresultsshowedthatadditionof4mg/LPACinthemiddleofaerationtank30minbeforestoppingaerationcouldmaketheeffluentTPmeetthefirstlevelAcriteria.Continuousadditionof4mg/LPACintheshorttermwouldinhibittheactivityofsludgebuthadnoadverseeffectoneffluentin-dexes.KeywordscyclicactivatedsludgesystemCASSPACenhancingphosphorusremovalactivityofsludgeE-mailzongpingw@hust.edu.cn《》GB18918—2002A·531·32920165CHINAWATER&WASTEWATERVol.32No.9May2016。1~3。CASS。CASS。CASS1CASSPAC。11.1CASS61h2h45min1h15min。201311—2014311.5mg/L。1201311—20143Tab.1AveragequalityofinfluentandeffluentfromNovember2013toMarch2014COD/mg·L-1BOD5/mg·L-1/mg·L-1/mg·L-1/mg·L-1pH196104.53.9629.221.87.46255.30.7913.53.157.11.2CASSSBRSBR12L。、、。430min30min2h30min15min15min。CASS。1.3TP、TN、NH3-N、COD、pH、OUR、SOUR、MLSSMLVSS。1.4①CFDCASS。②50、40、30、20、10min3.8mg/LPAC50、40、30、20、10minTP。③。1.5mg/L3.8mg/LPACAl2O30、1、2、3、4、5、6mg/LPACTP。④PAC6dPAC。7PAC36d。PACOUROUR。22.1CFDCASS。1。、。1/3、、L、B、Dvtd=vt=LBD/3BD=L/3。1CASSFig.1WaterflowstateinCASStankCFD·631·329.watergasheat.com1/2。2。。1/2。2.23.8mg/LPACTP2TP3.12mg/L。2TPTab.2EffectofTPremovalatdifferentcoagulantdosingtime/min1020304050TP/mg·L-10.610.560.480.500.55/%80.482.184.684.082.4230minPACTP。TP。TP。TP。20~30min。30minPAC。2.3PACTP3TP3.57mg/L。3TPTab.3EffectofTPremovalwithdifferentPACdosage/mg·L-10123456TP/mg·L-11.030.680.610.560.470.440.43/%71.181.082.984.386.887.788.03PAC4mg/LTPGB18918—2002A86.8%4~6mg/L4mg/L。1.5mg/L3.75mg/LAl3+OH-4PAC。2.4PAC2.4.1TPAPAC8mg/L230min。SOURSOUR2。2SOURFig.2VariationofSOURincontinuousculture227dSOUR27d23%。30%45%。TPCOD34。3TP80%TPGB18918—2002A7dPACTP80%。PACTP。4COD80%CODGB·731·.watergasheat.comCASSPAC32918918—2002A。PACCOD。COD。3TPFig.3VariationofTPremovalincontinuousculture4CODFig.4VariationofCODremovalincontinuousculture4TN55%NH3-N90%GB18918—2002A。DO5。DONH3-NNH3-NPAC。MLVSS/MLSSSVIMLVSS/MLSSSVI163.7%92mL/g58.5%86mL/g3。36d8mg/LPACPAC。COD、TP、TN、NH3-N。。PAC。2.4.2PACPAC4。PAC1020mg/L。4PACTab.4InhibitionofPACtoAOBandNOBactivityPACOUR/mgO2·L-1·min-110mg/LPAC20mg/LPACOUR/mgO2·L-1·min-1/%OUR/mgO2·L-1·min-1/%OUR0.850.6621.60.4941.8OUR0.130.0929.10.0834.5OUR0.080.0447.90.0454.04PAC10mg/L29.1%47.9%PAC20mg/L34.5%54.0%。PAC3Zhou1。3①CFD、、1/2。②PAC30min。③PAC·831·329.watergasheat.com4mg/L。④36dPAC。PAC。1ZhouZChenYXingCetal.Inhibitoryeffectsofsimul-taneouschemicalphosphorusremovalonmicrobialactivityintheunitankprocessJ.AdvMaterRes2013610/6131672-1675.2.J.201129423-2545.3.J.201036638-41.4.pHJ.20101297.5BroughtonAPrattSShiltonA.Enhancedbiologicalph-osphorusremovalforhigh-strengthwastewaterwithalowrbCOD∶PratioJ.BioresourTechnol20089951236-1241.1992-。E-mail1449631736@qq.com櫆櫆櫆櫆櫆櫆櫆櫆櫆櫆櫆櫆櫆櫆櫆櫆櫆櫆櫆櫆櫆櫆櫆櫆櫆櫆櫆櫆櫆櫆櫆櫆櫆櫆櫆櫆櫆櫆櫆櫆櫆櫆櫆櫆櫆櫆2015-12-1213412BennisSCrobedduE.NewrunoffsimulationmodelforsmallurbancatchmentsJ.JHydrolEng2007125540-544.13NasrABruenMJordanPetal.AcomparisonofSWATHSPFandSHETRAN/GOPCformodellingphos-phorusexportfromthreecatchmentsinIrelandJ.Wa-terRes20074151065-1073.14.J.2004243270-274.15LenhartLEckhardtKFohrerNetal.ComparisonoftwodifferentapproachesofsensitivityanalysisJ.PhysChemEarth2002279645-654.16BarcoJWongKMStenstromM.AutomaticcalibrationoftheU.S.EPASWMMModelforalargeurbancatch-mentJ.JHydraulEng20081344466-474.17.J.2011314717-723.18.SWMMJ.201228145-48.1989-。E-mailgf19891989@126.com2015-11-10·931·.watergasheat.comCASSPAC329

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