20145232JournalofMUCNaturalSciencesEditionMay2014Vol.23No.22014-02-10No.1112KYZY53.1988-2011..1967-.金源,吴燕红,夏建新100081“”.、HRT、、、.....X703A1005-8036201402-0081-07.“”15mg/L12mg/L50mg/L15mg/L...1800mg/L1、300mg/L.11.1A/OA/O-2...1A/O.A/O.23.1000m3/d100~300mg/L8mg/L90%.1A/OTab.1Thecasesstudyofanoxic-oxicammoniawastewatertreatmentprocessm3/dmg/Lmg/L%/m3340020<0.5900.85600200591.43.041368207.97.696.33.464800<1600.4>992.31.2A2/OA2/OA-A-O--NH3-NNO3-NNO2-NN2NH3-N.2A2/O.2A2/OTab.2Thecasesstudyofanaerobic-anoxic-oxicammoniawastewatertreatmentprocessm3/dmg/Lmg/L%/m3736063.79.485.20.881100301.096.70.992160100-250<10>905.31020000383.590.81.212A2/OA/O215mg/L90%.1000m3/d.1.3SBRSBR.51112345.3SBR.3SBRTab.3ThecasesstudyofSBRammoniawastewatertreatmentprocessHRThm3/dmg/Lmg/L%/m31216720300≤30>905.013831010<1>901.414723600282.46.696.53.21524400465>89.12.2SBR.28210mg/L90%.1.4MBRMBR16、.4MBR.4MBRTab.4Thecasesstudyofmembranebio-reactorammoniawastewatertreatmentprocessm3/dmg/Lmg/L%/m31750020-35<1>951.318400015-35<1>931.7191805.6-24.4<1951.120200050-110<5>931.1MBR100mg/L5mg/L93%.1.5BAFBAF21..5BAF.5BAFTab.5Thecasesstudyofbiologicalaeratedfilterwastewatertreatmentprocessm3/dmg/Lmg/L%/m322480030-70<5>901.8232000500-7004.8-6890.2-98.82.52410000≤50<5>901.52520011.02.181.30.6BAF.BAF.100mg/L5mg/L90%.1.6OxidationDitch2050.6.3823.50mg/L80%.6Tab.6Thecasesstudyofoxidationditchwastewatertreatmentprocessm3/dmg/Lmg/L%/m326300≤507>861.4273000030<3>901.728AAO1000025<5>801.229200030<1>951.122.1.30.7.7Tab.7Thecasesstudyofnitrificationdenitrificationwastewatertreatmentprocessmg/Lmg/L%31300-530<20>9532940-1200150-24079-8733120.75.694.934750-135010-15>9835FCC952-1049<15>9515mg/L95%.2.2SNDSND..8.8Tab.8Thecasesstudyofsimultaneousnitrificationanddenitrificationwastewatertreatmentprocessmg/Lmg/L%36585-790<10>9937319-8420.17-3.54>99810mg/L99%.4822.3ANAMMOXANAMMOXNH4+NO2-NO3-NH4+、NO2-NO3-N2.38SHARON“”250mg/L80%90%..3、9.9、Tab.9Theanalysisofapplicabilityprosandconsremovalrateandcostindifferentindustrialwaystoremoveammonia/A/O100~300mg/L1000m3/dpH.>90%2~3/m3A2/O<400mg/L.>90%1/m3SBR<1000m3/d、.>90%MBR<5mg/L.>93%1/m3BAF>2000m3/d、.>90%1~2/m3<50mg/L>2000m3/dBOD.BOD>80%1/m3.95%pH.99%.5823.90%.A2/O、MBR1/m3.4.、、..1.--A/OJ.200733990-93.2ZEIKUSJ.G.AnaerobicDigestionM.AppliedSciencePublisherLtd.1980.3.A/OJ.200930657-60.4.A/OJ.200922146-48.5.A/OJ.2006291085-86.6.-A/OJ.20102618102-105.7.A2/OJ.200319659-61.8.A2/OJ.2008341068-70.9.A2/O2J.20103816-17.10.AAO+FentonJ.2012394136-137.11CHANGCHHAOOJ.SequencingbatchreactorsystemfornutrientremovalORPandpHprofilesJ.ChemTechBiotechnol19966727-38.12.SBRJ.20063221-22.13.SBRJ.201030374-76.14.SBRJ.20113710128-130.15.J.200127545-47.16LIGCYANGTCHENJetal.StudyonthetreatmentofhighstrengthammoniawastewaterbyusinginnercirculationimpingingstreambiofilmreactorJ.MeteorologicalandEnvironmentalResearch2010112104-106.17.J.200521283-85.18.MBRJ.201030687-90.19.J.201032568-72.20.MBRJ.2010269131-133.21ROTHEECORNELP.OptimizingdesignoperationandenergyconsumptionofbiologicalaeratedfiltersBAFfornitrogenremovalofmunicipalwastewaterJ.Wat.Sci&Tech2004506131-139.22.UBAFJ.200525366-68.23.J.2008281187-89.24.J.2009252067-69.68225.J.200316116-17.26.ABR+A/OJ.2012396167-168.27.J.201137122-26.28.AAOJ.2010262226-29.29.J.201041383-88.30UABELINGCFSEYFRIED.Anaerobic-aerobictreatmentofhighstrengthammoniumwastewater-nitrogenremovalvianitriteJ.Wat.Sci&Tech.1992265/61007-1015.31.J.200319811-14.32.J.201226796-102.33.J.2011311153-56.34.J.2012389128-131.35.FCCJ.201041159-61.36.J.200827440-44.37.J.200936965-970.38.-“”J.2006321043-46.ComparativeAnalysisofBiologicalAmmoniaNitrogenRemovalProcessesinIndustrialWastewaterJINYuanWUYan-hongXIAJian-xinCollegeofLifeandEnvironmentSciencesMinzuUniversityofChinaBeijing100081ChinaAbstractAmmonianitrogenhasbeenoneofthewaterpollutioncontrolbindingtargetsin12thFive-YearPlan.Thispaperbasedonbiologicalapplicationscomparesandanalyzestheapplicableconditionstreatmenteffectsandcostsondifferentbiologicalprocesses.Italsoanalyzesapplicabilityadvantagesanddisadvantagesamongdifferentprocesses.Thoughtheprocesseshavedifferentinfluentammoniarequirementtheireffluentammoniamostlycanbedischargeddirectly.Bycomparingandanalyzingtheconclusionisthatthecostsarequitedifferentindifferentprocessesorindustrialwastewater.Itcanbeapartofbasisinchoosingbiologicalammonianitrogenwastewaterremovalprocessandparameters.Keywordsammonianitrogenindustrialwastewaterbiologicalnitrogenremoval[责任编辑:白玲]78