工业废水中的生物脱氮工艺及其应用效果比较金源

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