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当前位置:首页 > 办公文档 > 总结/报告 > 不同运行方式下低溶解氧污泥微膨胀的可行性研究王中玮1
32820118ENVIRONMENTALSCIENCEVol.32No.8Aug.20111112111.1001242.150090DO.4SBRDODO=0.5mg/L、、.60~90min.DO、2.//.X703.1A0250-3301201108-2347-062010-09-102011-01-2720091103110011QAK2010061986~.*E-mailpyz@bjut.edu.cnFeasibilityStudyforLimitedFilamentousBulkingUnderLowDissolvedOxygenatDifferentOperationRegimesWANGZhong-wei1PENGYong-zhen1WANGShu-ying1GUOJian-hua2HUANGHui-jun1ZHENYa-nan11.KeyLaboratoryofBeijingforWaterQualityScienceandWaterEnvironmentRecoveryEngineeringBeijingUniversityofTechnologyBeijing100124China2.StateKeyLaboratoryofUrbanWaterResourceandEnvironmentHarbinInstituteofTechnologyHarbin150090ChinaAbstractLimitedfilamentousbulkingunderlowdissolvedoxygenDOisanewtechnologyforenergysavingandhighqualityeffluent.InordertoinvestigatethefeasibilityofthistechnologyfoursequencebatchreactorsSBRswereoccupiedtooperateatdifferentregimestostimulatedifferentprocessesunderlowDO0.5mg/L.Sludgesettleabilityflocstructurepollutantremovalandaeratedenergyconsumptionwereinvestigated.TheresultsshowedthatlimitedfilamentousbulkingunderlowDOwashardtorealizeinthesingle-stageaerobicreactorsfortheywerepronetobulkingseverelywhileitcouldbeachievedstablyinthepre-denitrificationreactorswhenthefeedlengthwasbetween60and90minutes.ComparedwithnormalsludgeatthesameDOlimitedfilamentousbulkingsludgeacquiredbylowDOdisplayeditshighenergy-savingeffect.Inadditionthespecificammoniaconsumptionrateoflimitedfilamentousbulkingsludgewasabout2timeshigherthantheoneofnormalsludge.Onthecontrarythetotalnitrogenremovalefficiencywaslower.Furtheranalysisindicatedthatstablelimitedsludgebulkingcouldbeachievedinagoodalternativeanoxic/anaerobic/aerobicconditionwithouttoohighorganicloading.Keywordslowdissolvedoxygenlimitedfilamentousbulkingfeasibilityoperationregimesenergysaving.、.12.2、34A/O5SBR.A/OSBRDO、..4SBR、A/O4.DOI:10.13227/j.hjkx.2011.08.0513211.11.SBR5LPLC.DO0.5mg/LPLCDO0.5mg/LDO0.5mg/L.DO26.40L/h.500r/min25℃pH7.0~8.0.15dMLSS1500~2500mg/L.2.5L0.5..4SBR1.SBR1SBR2SBR1+SBR2SBR31.PLC2.3.4.5.pHDO6.7.8.9.10.11.12.13.HCl14.NaOH1SBRFig.1SchematicdiagramoftheSBRSBR4SBR3+A/OSBR4A/O.6h4.1SBR1/minTable1OperatingphaseandlengthduringoneSBRcycle/minSBR10~100~180180~182182~350350~360SBR20~1800~180180~182182~350350~360SBR30~100~120120~300300~302302~350350~360SBR40~600~120120~300300~302302~350350~3601SBR330~47d90min1.2.NaAc4.69mmol/LCOD300mg/LNH4Cl2.14mmol/LNH+4-N30mg/LNaH2PO40.48mmol/LPO3-4-P15mg/LKCl0.48mmol/LCaCl20.10mmol/LMgSO40.37mmol/L1ml/L7.30d.1.3.COD、SV、MLSS、NH+4-N、NO-2-N、NO-3-N、PO3-4-P3.OLYMPUS2BX52.MalvernMastersizer2000MalvernInstrumentsLtd.UK.22.12.1.122a.+SBR120dSVI54mL/g340mL/gSBR214dSVI337mL/g.SVI<800mL/g15.6mL·g·d-125.4mL·g·d-1.DO.Palm8.CODDO8.843282Fig.2SludgesettleabilityexpressedasSVIduringthewholeoperatingperiodMonodμi=μmaxiSKSi+S·DOKOi+DOi=1、2S.DO2DO.240d.2.1.22SBR3SBR4.2bSBR310minSVI95mL/g50mL/g.60minSBR47dSVI203mL/g18.0mL·g·d-1SVI100~250mL/g.SBR390minSVISBR418.9mL·g·d-1SVI110~190mL/g.2Table2Physiologicalpropertiesoffilamentousbacteriaandfloc-formingbacteria1μmax/h-10.60.292KS/mg·L-16440103DOKDO/mg·L-10.10.027104Kd/h-10.0060.00295Y0.1530.13910610SVI4①1112②———2③RBCODPAOsGAOs.RBCOD132④PAOsGAOs7.PHA、PAOsGAOs2.DO..SVI943232①~③.2.22.2.13SBR1.3a.17dSVI=188mL/g3b.10d3c..SBR2SBR1.3SBR1×400Fig.3FlocstructureatdifferentstateinSBR1400multiplesphase-contrast2.2.2.10minSBR34a.60minSBR44b.SBR390minSBR4.4SBR3SBR4×400Fig.4FlocstructureatsteadystateinSBR3andSBR4400multiplesphase-contrast5.210min60min150μm200μm<200μm30.84%71.35%.5SBR3SBR4Fig.5GranulesizedistributionatsteadystateinSBR3andSBR42.3DO2.SBR1SBR2COD61.6%67.1%.DO.6SBR3SBR4.SBR36a.COD15~25mg/L05328PHA.4.40mg·g·h-1.NO-x-NNO-2-N+NO-3-NNO-2-NNO-3-N0.5mg/L1.0mg/LSND.SBR4CODDO8.88mg·g·h-1SBR326b.、SBR4SBR3DO.SBR4SNDSND.SBR390minSBR4.SBR3SBR4COD90%..60min90minSND10min79.7%57.4%.79.7%60.4%.6SBR3SBR4Fig.6TypicalparameterprofileduringanormalcycleonfourSBRs2.43DODO=0.5mg/LDO=2.0mg/L.DOPLC0.5mg/L..PLC3.DO.10min10%.6bCOD1hOUR.60min90min2hOUR10min36.1%34.8%..4.DO.DO.Martins14DO13min15min.DO.3、OURTable3AerationtimeOURandenergysavingeffectunderdifferentfeedinglength/h180~300minOUR/g·kg·h-1/%10min1.88±0.1420.13±4.33—60min1.70±0.157.22±2.479.690min1.68±0.177.02±1.6610.615323260~90min.A/O..//.//...DODO3415...31DO=0.5mg/L60~90minSVI100~250mL/g.DO.210min60min<200μm30.84%71.35%.3DODO210%.SND60min90min10min79.7%60.4%.4.//.1GuoJHPengYZPengCYetal.EnergysavingachievedbylimitedfilamentousbulkingsludgeunderlowdissolvedoxygenJ.BioresourceTechnology201010141120-1126.2.、J.200829123342-3347.3.A/OJ.200829123348-3352.4.J.200632121082-1086.5.SBRJ.20106161534-1539.6LiHJChenYGGuGW.Theeffectofpropionictoaceticacidratioonanaerobic-aerobiclowdissolvedoxygenbiologicalphosphorusandnitrogenremovalJ.BioresourceTechnology200899104400-4407.7MartinsAMPHeijnenJJVanLoosdrechtMCM.BulkingsludgeinbiologicalnutrientremovalsystemsJ.BiotechnologyandBioengineering2004862125-135.8PalmJCJenkinsDParkerDS.Relationshipbetweenorganicloadingdissolved-oxygenconcentrationandsludgesettleabilityinthecompletely-mixedactivatedsludgeprocessJ.JournalWaterPollutionControlFederation19805
本文标题:不同运行方式下低溶解氧污泥微膨胀的可行性研究王中玮1
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