好氧低氧生物滤池对低碳氮比污水脱氮研究陈秀荣

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3210201110ENVIRONMENTALSCIENCEVol.32No.10Oct.2011-200237-.DO3.5~4.3mg/L、DO0.9~1.1mg/L2、HRT、C/N.3C/NC/N=3∶11∶1HRT+10+5h、8+4h、6+3h、4+2hC/N=3∶1HRT+=10+5h1∶2、1∶1、2∶12HRT+=10+5h1∶1C/N2∶1、3∶1、5∶1、10∶1.C/N5∶11∶1HRT10h5hCOD、254、37.248.2mg/LCOD、48、9.314.8mg/L.、、.-X703.1A0250-3301201110-2986-072010-11-182011-03-05510081241975~E-mailxrchen@ecust.edu.cnEffectiveNitrogenRemovalinLowC/NWastewaterwithCombinedAerobic-LowDOBiofilmTreatmentProcessCHENXiu-rongAIQi-fengXUWen-luWUMin-linSchoolofResourceandEnvironmentalEngineeringEastChinaUniversityofScienceandTechnologyShanghai200237ChinaAbstractThemunicipalwastewaterinChinaischaracterizedbylowratioofcarbontonitrogenwhichisthekeyrestrictivefactorforeffectivebiologicalremovalofnitrogen.Inthisstudytheaerobic-lowDObiofilmprocesswasusedforthenitrogenremovalofmunicipalwastewater.Bymeansofadjustinginflowratiosofaerobicsectiontolow-DOsectionhydraulicretentiontimeHRTandinflowratioofcarbontonitrogenC/Ntheperformancesofnitrificationinaerobicbiofilmsectionanddenitrificationinlow-DOsectioncouldbeimprovedthegoodperformanceofnitrogenremovalwasachieved.Inordertoinsurethegoodeffluentqualityespeciallyforammonianitrogenandtotalnitrogenindexesthenitrificationanddenitrificationcouldbemadeupinaerobicandlow-DObiofilmsectionrespectivelyduetothecoexistenceofaerobicandanoxiczoneinbiofilm.Therewere3stagesfortheresearchprocess.InthefirststagetheoriginalC/Ninflowratiosofaerobicsectiontolow-DOsectionwerechosenas3∶1and1∶1respectivelythentheeffectsofvariousHRTaerobicsection+lowDOsectionvaluessuchas10+5h8+4h6+3h4+2htonitrogenremovalwereanalyzed.AccordingtotheconclusioninthefirststagetheoriginalC/Nwaskeptat3∶1HRTaerobicsection+lowDOsectionwas10+5h.Thentheeffectsofvariousinflowratiostonitrogenremovalwerestudiedinthesecondstage.InthethirdstagewhenHRTaerobicsection+lowDOsectionwas10+5handinflowratiowas1∶1theoriginalC/Nwereadjustedfrom2∶13∶15∶1to10∶1.ToconcludetheoptimalparametersfornitrogenremovalinthebiofilmsystemwereasfollowsoriginalC/N=51inflowratioofaerobictolow-DOsection=1∶1HRTofaerobicandlow-DOsectionswere10hand5hrespectively.AsaresultCODammonianitrogenandtotalnitrogencouldberemovedfrom254mg/Lto48mg/L37.2mg/Lto9.3mg/Land48.2mg/Lto14.8mg/Lrespectively.Keywordsmunicipalwastewaterlowratioofcarbontonitrogenaerobic-lowDObiofilmprocessinflowratio、1SHARON2SND34.CANON5-OLAND.DOI:10.13227/j.hjkx.2011.10.03110-67、8~15.、16.、.-17.、HRTCODTNC/N.11.1、、、、EDTA-Na1.1COD100~500mg/LC/N2∶1~10∶1.1Table1Waterqualityindexes/℃25±2/mg·L-130.0~40.0pH7.0~7.7/mg·L-140.0~50.0CaCO3/mg·L-1220/mg·L-11.0~4.0COD/mg·L-1100~500/mg·L-10.0~1.01.2Φ240mm×1000mm、.150mm150mm、、.700mm50%0.032m3.50mm310mm13.1.2DO3.5~4.3mg/LDO0.9~1.1mg/L.2C/N3∶1C/NHRT、-HRT、2∶1~10∶1C/N-1.2.3.4.5.6.7.8.9.10.1Fig.1SchematicdiagramoftestinstallationC/N.2.1HRTC/N3∶1789232HRTC/N3∶1.1∶1.50%HRTHRTHRT.HRT15、12、96h30d.10d20dHRT-2.2HRT-Table2Substratesremovalperformancesinaerobic-lowDOlevelbiofilmwithvariousHRTCOD/mg·L-1NH+4-N/mg·L-1NO-2-N/mg·L-1NO-3-N/mg·L-1TN/mg·L-1/%/%/%101554670.337.60.897.90.61.11.723.549.637.430.2Ⅰ51034160.219.99.850.80.91.612.63.942.424.941.3151554173.537.69.873.90.61.61.73.949.624.949.781635765.038.51.097.50.50.81.524.747.835.924.9Ⅱ41134560.220.712.738.60.71.813.14.342.628.333.6121634572.438.512.767.00.51.81.54.347.828.340.861666560.837.91.695.80.41.31.621.448.541.215.1Ⅲ31175553.020.912.540.20.92.511.55.843.232.425.091665566.937.912.567.00.42.51.65.848.532.433.241505861.336.51.994.90.61.91.820.146.942.210.0Ⅳ21106739.120.612.141.31.36.811.07.242.535.716.061506755.336.512.166.80.66.81.87.246.935.723.92..HRT15h6h、7.1%20.2%、25.3%25.9%COD9.0%、21.1%18.2%HRTCOD.HRT.COD∶TN>218.HRTCODCOD.DODO.HRT.DO190.2~0.4mg/L1.2~1.5mg/LDO0.9~1.1mg/L.HRT2hHRT4hHRT.2.2C/N3∶1HRT10h3.2L/hpH7.0~7.725℃±2℃.1∶2、1∶12∶19.6、6.44.8L/hHRT3.3、56.7h.1∶12.1HRT15h.2.2.1.-889210-..COD、、、、2.2Fig.2Low-DOfilterperformancesatvariousinflowratios2COD、、、.1∶2COD、518.0、107.5237.1mg/h.HRTHRT.HRT.HRT3.3hHRT6.7h.1∶2HRT3.3h77.8mg/h.SRT20HRT3.3h.1∶22∶1.421.2.0g/gMLSS/.43、、+.+/2/.>0+.、+2∶1→1∶11∶1→1∶2.、、2/+-=-/3.3Table3Organicnitrogentransformationamountinlow-DObiofilmwithvariousinflowratios/L·h-1/mg·L-1/L·h-1/mg·L-1/mg·h-1//mg·h-1+-/mg·h-1∶=1∶23.210.36.49.03.2×10.3+6.4×9.0=90.651.890.6-51.8=38.8∶=1∶13.29.03.29.73.2×9.0+3.2×9.7=59.83.859.8-3.8=56.0∶=2∶13.210.51.69.23.2×10.5+1.6×4.2=40.341.740.3+41.7=82.01∶2、1∶12∶13+38.8、56.0、82.0mg/h.+.989232HRT、.22、.HRT、HRT+./HRT2.HRT/./2/.2.2.2-41∶2HRT3.3h20.8mg/LCOD2∶11∶1.HRT3.3h.COD.COD、1∶1.2.3C/N4-Table4Substratesremovalperformancesinaerobic-lowDOlevelbiofilmwithvariousinflowratios∶/L·h-1/mg·L-1/mg·L-1/%CODNH+4-NTNCODNH+4-NTNCODNH+4-NTN2∶14.815537.147.4386.932.875.381.430.61∶16.415537.649.6419.824.972.473.949.71∶29.615737.447.35318.320.866.351.156.01∶1HRT15hHRT10hHRT5h.DO0.9~1.1mg/LDO3.5~4.3mg/L25℃±2℃pH7.0~7.7.CODC/N2∶1、3∶1、5∶110∶1.1∶1C/N1.9∶1、2.5∶1、4.0∶17.8∶1.2.3.1C/NC/NCOD34.0~10h10~15hCOD.3C/NCODC/NCOD.COD3C/NCODFig.3CODremovalperformancesatvariousinflowC/NratiosCODCODDO23COD24CODCOD、099210-4C/NTNFig.4TNremovalperformancesatvariousinflowC/NratiosCODCODCODCOD.CODC/NCOD.DO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