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*112311.5410042.5410043.100029CASS-AOB。AOB32d0.29kg/m3·d5.25kg/m3·d90%。4。1.32。ExperimentalStudyonthePartialNitrificationofHighConcentrationAmmonia-nitrogenRareEarthWastewaterHOUWanbing1WULuhan1JINYue2YEYe3ZHANGWenjie11.GuangxiScientificExperimentalCenterofMiningMetallurgyandEnvironmentCollegeofEnvironmentalScienceandEngineeringGuilinUniversityofTechnologyGuilinGuangxi541004AbstractActivatedsludgeistakenfromCASStanklocatedatGuilinMunicipalSewageTreatmentPlantasinocula-tedsludge.ThecombinedprocessofaerobictankandefficientsedimentationisadoptedtoenrichAOBbacteriaandthenbatchexperimentiscarriedouttotreatrareearthhighammonianitrogenwastewaterusingthecultivatedsludge.Thecultivatedperiodlasts32daysthetotalnitrogenloadispromotedfrom0.29kg/m3·dto5.25kg/m3·dandnitritenitrogenaccumulationratereachesabove90%.Afterthecultivationperiod4batchtestsareconduc-tedusingrealrareearthwastewaterproducedbyarareearthsmeltingenterprisesinGuangxiasinfluentaimingtostudytheremovaleffectsfrompartialnitrificationtosuchwastewater.Theresultsshowthatafteramonthofcultiva-tingpartialnitrificationsludgehasahighconversioneffectonhighconcentrationammonia-nitrogenrareearthwastewaterthenitratenitrogenaccumulationrateineffluentishighandnitratenitrogenandammonianitrogenratioisabout1.32ineffluentmeetingtherequirementsoftheinfluentofanammoxreactor.KeyWordshighconcentrationammonia-nitrogenwastewaterpartialnitrificationrareearthwastewaternitrite02060、、、、。-、、、。AOBNOB。。11.11*511081082013GXNSFCA019018、2014GXNSFBA1182651347004-152013ZD031、2013ZL076、ZL2014051。·1·20154110October2015IndustrialSafetyandEnvironmentalProtection。1-2-3-4-5-pH6-7-8-9-。132℃±1℃pH7.5~7.6pH7.0~7.11。2mg/L。。1.2N-1--SV30100mLMLSSMLVSSpHJENCOMODEL6010DOJENCOMODEL9010。1.3CASSMLSS8028mg/LMLVSS5880mg/LVSS/SS0.732。。NH42SO4、KH2PO4、NaHCO3CaCl2·2H2O0.113g/LMgSO4·7H2O0.1g/LⅠ0.5mL/LⅡ1mL/LⅠFeSO4·7H2O10g/LC10H14N2Na2O35.6g/LⅡMnCl2·4H2O0.352g/LCoCl2·6H2O0.096g/LNiCl2·6H2O0.08g/LCuSO4·5H2O0.1g/LZnSO4·7H2O0.172g/LNaSeO4·10H2O0.105g/LNaMoO4·2H2O0.11g/LC10H14N2Na2O35.0g/L。0.5mol/LNaHCO3Na2CO3。4750mg/LCOD。22.1300mg/L24h0.29kg/m3·d。1.322-3。2。22。AOB。13d535mg/L206mg/L283mg/L33mg/LAOBNOB。14d0.61kg/m3·d1.67kg/m3·dAOB1900mg/L230mg/L。28d4000mg/L1600mg/L5.25kg/m3·d。NOB。。3。310dSV30、MLSS、MLVSSSV303220MLSS8028mg/L3910mg/LMLVSS5880mg/L1638mg/L。10d·2·、NOB。10d10dAOB。31dSV3025MLSS5844mg/LMLVSS4246mg/L。32.2。445。444750mg/L5.2kg/m3·d。1950mg/L2564mg/L~2741mg/L。580mg/L96%。AOB。。6NO-2/NH+46NO-2/NH+41.29~1.48NO-2/NH+41.32。-。56NO-2/NH+431CASS。5.25kg/m3·d90%。20NOBAOB。3NO-2/NH+41.32-。1.PNHJ.201320685-89.2JettenMSMWagnerMFucrstJctal.Microbiologyandappli-cationoftheanacrobicammoniumoxidationanammoxprocessJ.CurrentOpinioninBiotechnology2001123283-288.3.EGSBJ.201339257-61.。2015-01-20·3·
本文标题:高氨氮稀土废水短程硝化试验研究侯宛冰
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