DO对除磷过程的长期影响彭赵旭

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43420114JOURNALOFHARBININSTITUTEOFTECHNOLOGYVol.43No.4Apr.2011DO1211111.150090pyz@bjut.edu.cn2.130024DOSBRDO5.5~7.0mg/L0.5~1.5mg/LDOEBPR.pH7.2~7.623±0.5℃DO.DO43.08%.30minDO6.2711.45mg·g-1·h-145.24%.βPHBDO.DODO.SBRX703.1A0367-6234201104-0042-05Long-termeffectofDOonphosphorusremovalprocessPENGZhao-xu1HUOMing-xin2PENGYong-zhen1GUILi-juan1LIUXu-liang1YUZhen-bo11.StateKeyLaboratoryofUrbanWaterResourceandEnvironmentHarbinInstituteofTechnology150090HarbinChinapyz@bjut.edu.cn2.SchoolofUrbanandEnvironmentalSciencesNortheastNormalUniversity130024ChangchunChinaAbstractTostudythelong-termeffectofdissolvedoxygenDOonphosphorusremovalprocessthecharac-teristicsofenhancedbiologicalphosphorusremovalEBPRundertheDOlevelof5.5-7.0mg/Land0.5-1.5mg/LwereinvestigatedsystematicallyusingsequencingbatchreactorSBR.TheresultsshowedthatwhenpHwasin7.2-7.6andtemperaturewasat23±0.5℃highDOhadadverseimpactonbothphos-phorusreleaseprocessandphosphorusuptakeprocess.Theamountofreleasedphosphorusinanaerobicperiodwas43.08%lowerthanthatunderlowDOcondition.Phosphorusuptakeprocesswentfastduringtheinitial30mininaerobicperiod.Themaximumspecificphosphorusuptakeratewas6.2711.45mg·g-1·h-1un-derhighDOandlowDOconditionsrespectively.Analysisindicatedthatthemainreasonofdeteriorationofphosphorusremovalprocesswasdeficiencyofpoly-β-hydroxybutyratePHBcausedbyexcessiveaerationandmoreinfluentcarbonsourceusedfordenificationprocess.HighDOdidnothaveobviousadvantageonre-strainingfilamentoussludgebulkingthanlowDO.Theimprovementofphosphorusremovalwasusuallyassoci-atedwiththeimprovementofsludgesettleability.KeywordsdissolvedoxygenSBRprocessexcessiveaerationphosphorusreleasephosphorusuptake2009-11-20.“”EDBS07/1-53974092.1983—1949—..DO1.DO.DO2DO3、4-5.6DOSND.7DO.DOSBRDO.11.1CH3COONa·3H2O0.66g/LNH4Cl0.17g/LKH2PO40.02g/LNaHCO30.4g/LMgSO4·7H2O0.08g/LCaCl20.04g/L10.5mL8.1mg·L-1CODNH4+-NPO43--PCaCO3300~33040~454.5~5.0400~4501.2SBR700mm200mm12L1.10cm...3L、0.5h、2.0h、、.100mLMLSS2000mg/L.SRT12.5d10h.23±0.5℃.pH、DO、ORP.A2O1SBR1、SBR2.DOSBR1、SBR2.1.3COD、NH4+-N、NO2--N、NO3--N、PO43--P、SV、SVI、MLSSMLVSS90.45μm4℃3hPHB10.DO、pH、ORPWTW340i.34512681291013111—DO2—pH3—4—DO5—pH6—ORP7—8—ORP9—10—11—12—13—.122.1DOPO43--PDONOx--N11-12、13.14.Jens15NO2--N5mg/L.DO.2DOSBR1DO6mg/L.NH4+-N120minNOx--NpHaDOb16-17.30minPHB18.PHB19.PO43--PPO43--P.DO.2.2DOPO43--PSBR2SBR1.·34·4DODO1.0mg/L3DOSBR1pHaDOb.PO43--P120min.30min11.45mg·g-1·h-1DO6.27mg·g-1·h-182.62%.NH+4-NPO3-4-PNO-2-NDONO-3-NpH2420161284020406080100120140160t/min10864208.48.38.28.18.07.97.8pHDO/(mg·L-1)籽(NH+4-N,NO2--N,NO3--N,PO3-4-P)/(mg·L-1)ab2DO、NH+4-NPO3-4-PNO-2-NDONO-3-NpH302520151054.03.53.02.52.01.51.00.50DO/(mg·L-1)8.07.97.87.77.67.57.4pH020406080100120140160t/min籽(NH+4-N,NO2--N,NO3--N,PO3-4-P)/(mg·L-1)ab3DO、DODO.SBR11/4PHB.MLVSSPHB4.5mg.PHBSBR2CODDO.2.3DO.20-21.DO.SBR1SBR2DO6.36、1.25mg/L4.205.SBR1SBR2PO43--P21.02、27.49mg/LPO43--P5.44、0.12mg/L.SBR1SBR243.08%.7.56.55.54.53.52.51.50.5020406080100周期数DO/(mg·L-1)SBR1SBR24SBR1SBR2DO020406080100周期数籽(PO43--P)/(mg·L-1)SBR1厌氧末SBR1好氧末SBR2厌氧末SBR2好氧末2824201612845SBR1SBR2NOx--N.SBR1DOSBR2SNDSBR222.23SBR1SBR2SND24.43%34.74%SBR1SBR2NOx--NPHB24.·44·432.4DODO.Rob25、SVI3.DO.26A/ODO2mg/L0.5mg/LSVI110mL/g160mL/g.27SBRDODO.SVI460mL/gDO5.5~7.0mg/LDO0.5~1.5mg/L6.30SBR1SBR2SBR1SBR2DO.SBR1COD30mg/LSBR2SBR2SBR1SBR2SBR1.Andrew28.1.23g/mL291.005g/mL28.525500475450425400375350325300020406080100周期数低DO高DOSVI/(mL·g-1)6SRTSRT.DO.30SBR1SBR2SRTDO.31PHBMLVSS4.5mgDOEBPR.2DO0.5~1.5mg/L、DO5~7mg/LSNDNOx--NDOEBPR75.67%.3DO..1MINOTLOOSDRECHTvanMCMHEIJNENJJ.MicrobiologyandbiochemistryoftheenhancedbiologicalphosphorusremovalprocessJ.WatRes199832113193-3207.2ETTERERTWILDERERPA.Generationandproper-tiesofaerobicgranularsludgeJ.WaterSciTechnol200143319-26.3.A/OJ.200726117-20.4.SBBRJ.2006265728-733.5.SBRJ.200420840-42.6GUOJianhuaPENGYongzhenWANGShuyingetal.Long-termeffectofdissolvedoxygenonpartialnitrifi-cationperformanceandmicrobialcommunitystructureJ.BioresourceTechnology20091002796-2802.·54·4DO7.、J.200829123342-3346.8TSUNEDASOHNOTSOEJIMAKetal.Simultane-ousnitrogenandphosphorusremovalusingdenitrifyingphosphate-accumulatingorganismsinasequencingbatchreactorJ.BiochemicalEngineeringJournal200627191-196.9.M.4.200238-40.10WANGDBLIXMYANGQetal.Biologicalphosphorusremovalinsequencingbatchreactorwithsingle-stagleoxicprocessJ.BioresourceTechnolo-gy2008995466-5473.11KUBATVLOOSDRECHTvanMCMMURNLEIT-NEREetal.Kineticsandstoichiometryinthebiolog-icalphosphorusremovalprocesswithshortcycletimesJ.WatRes1997314918-928.12KUBATMURNLEITNERELOOSDRECHTvanMCMetal.Ametabolicmodelforbiologicalphosphor-usremovalbydenitrifyingorganismsJ.Biotechnolo-gyandBioengineering199652685-695.13.、J.200319133-36.14.J.2003256323-325.15MEINHOLDJARNOLDEISAACSS.Effectofni-triteonanoxicphosphateuptakeinbiologicalphos-phorusremovalactivatedsludgeJ.WatRes19993381871-1999.16GUOJHYANGQPENGYZetal.Biologicalni-trogenremovalwithreal-timecontrolusingstep-feedSBRtechnologyJ.EnzymeMicrobTech2007401564-1569.17PAVELJNHVALANKOCIJANJetal.Experi-mentaldesignofanoptimalphasedurationcontrolstrategyusedinbatchb
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