氨氧化细菌的富集培养及影响因素的研究戴昕

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40420154ENVIRONMENTALSCIENCEANDMANAGEMENTVol.40No.4Apr.20152015-02-2320120461983-。1674-6139201504-0044-051221.2115002.210094、pH、DO、、。22.8mg/L·h80%32.6。30℃、pH=8.5、DO=0.5mg/L、HCO-3/NH+4-N=1.67、400mg/L。X703.1AStudyonEnrichmentCultureandInfluencingFactorsofAmmoniaOxidizingBacteriaDaiXin1WuYajie2AnLichao21.NanjingKeshengEnvironmentProtectionCo.LtdNanjing211500China2.SchoolofEnvironmentalandBiologicalEngineeringNanjingUniversityofScienceandTechnologyNanjing210094ChinaAbstractInthispaperenrichmentprocessofammonia-oxidizingbacteriaisstudiedundertheconditionsofintermittenttrainingmethods.Thispapermainlydiscussestheinfluenceofammoniaoxidizingbacteriagrowthconditionsonshortcutnitrifica-tionsuchastemperatureinitialpHvalueDOalkalinitytheinfluentammoniaconcentrationetc.Experimentalstudieshavefoundthatwhenammoniumoxidizingbacteriaenrichedprocessisfinishedthetreatmentindexstabilizeswithammoniaoxidationratereached22.8mg/L·hnitriteaccumulationrateofaround80%thenumberofammonia-oxidizingbacteriamayberaisedto32.6-foldenrichmentbefore.Inadditionontheinfluencefactorsoftheparalleltestfoundthatwhenthetemperatureis30℃pH=8.5DO=0.5mg/LHCO-3/NH+4-Nmolarratiois1.67andtheinfluentammonianitrogenconcentrationislessthan400mg/Listheoptimumgrowthconditionsfortheammoniaoxidizingbacteria.Undertheseconditionsitisthemostconducivetotherealizationofshortcutnitrification.Keywordsammoniaoxidizingbacteriaenrichmentcultureinfluencingfactorsshortcutnitrification“”。、、。NH+4-NNO-2-NNO-3-NNO-2-NN21。25%、60%、40%50%2-3。。。·44·40420154·Vol.40No.4Apr.201511.11.1.1。1.1.22L、、12h。1。11L。1.1.3。300mg/L250mg/LNaHCO33000mg/LK2HPO4·12H2O500mg/L。1.21.2.112h。5min11h50min5min1L。250mg/LNH4Cl1146mg/LNaHCO33000mg/LK2HPO4·12H2O500mg/LFeSO4·7H2O30mg/LMgSO4·7H2O30mg/L。30℃DO1.0mg/L。MLSS3000mg/L。1.2.2MPN4AOB。4。NH42SO42g/L、K2HPO40.75g/L、NaH2PO40.25g/L、MnSO4·4H2O0.01g/L、MgSO4·7H2O0.03g/L、CaCO35g/L、pH=7.2。25℃14dgriessMPN1。1.2.3、pH、DO、、、。1.2.4η1mg/L·dη1η1=CNH+4-N1-CNH+4-N2/tCNH+4-N1─mg/LCNH+4-N2─tmg/Lt─h。1.2.5η2%η2η2=CNO-2-NCNO-2-N+CNO-3-N×100%CNO-2-N─mg/LCNO-3-N─mg/L。1.2.65NO-2-NN-1--NO-3-NBDOYSI550ApHPHS-25pH。22.1300mg/L600mg/L。2、3。2·54·40420154·Vol.40No.4Apr.20153、2、35。。90%80%。2.2DO=1.0mg/L30℃pH=8.0、、4。4480%。。11h22.7mg/L91.7%22.8mg/L·h。2.3MPN25dMPN1.2×107/gMLSS3.91×108/gMLSS32.6。2.4pH=8.0DO=1.0mg/L=300mg/LHRT=12h、。5。55。15℃164.71mg/L32.43mg/L49.0%≥20℃210mg/L85%。20℃NOBAOB20℃AOBNOB。AOBNO-26。30℃35℃12h·64·40420154·Vol.40No.4Apr.201590%30℃93.2%82.23%。30℃。2.5pHT=30℃DO=1.0mg/L300mg/LHRT=12h、pH。6。6pH6pHpH=6.561.3%pHpH=8.599.32%272.27mg/L。pHpH>9.5pH1064.4%。FAAOBNOBAOB10mg/L~150mg/LNOB0.1mg/L~1.0mg/L。300mg/LpHFA。pH8.5FA76.1mg/LpH9.0FA160mg/LAOBpHAOBpH9.5~10。pH8.5。2.6DOT=30℃pH=8.5mg/L300mg/LHRT=12h、DO。7。7DO7DO90%80%。DO0.5mg/L96.7%DO2.5mg/L94.1%。AOBNOB7AOBNOBpH6.3NOB80%。BALMELLEDONO-2-N。DO0.5mg/L。2.7T=30℃pH=8.5mg/LDO=0.5mg/L300mg/LHRT=12h、。8。·74·40420154·Vol.40No.4Apr.201588。893mgCaCO3/L60.4%pH6.01786mgCaCO3/L97.9%pH6.5。。1786mgCaCO3/LNaHCO33000mg/L。HCO-3/NH+4-N=1.67。2.8T=30℃pH=8.5mg/LDO=0.5mg/LHCO-3/NH+4-N=7.26HRT=12h、。9。99100mg/L400mg/L90%500mg/L12h74.4%。80%。3180%。222.8mg/L·h。3MPN32.6。430℃、pH=8.5、DO=0.5mg/L、HCO-3/NH+4-N=1.67、400mg/L。1.M.2006.2XinZhangDaijunZhangQiangHeetal.Shortcutnitrification-denitrificationinasequencingbatchreactorbycontrollingaerationdurationbasedonhydrogenionproductionrateonlinemonitoringJ.EnvironmentalTechnology201435121478-1483.3L.WangJ.ZhuC.Miller.ShortcutNitrificationandDenitrificationofSwineWastewaterinaSequencingBatchReactorSystemJ.TransactionsoftheASABE2010533813-818.4GB/T26322-2010.MPNS.2010.5.M.2002.6HyungseokYoo.Nitrogenremovalfromsyntheticwastewaterbysimultaneousnitrificationanddenitrificationvianitriteinanintermittently-aeratedreactorJ.WaterResearch1999331146-149.7WiesmannU.BiologicalnitrogenremovalfromwastewaterM.Biotechnics/Wastewater.SpringerBerlinHeidelberg1994113-154.·84·

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