常温条件下厌氧氨氧化生物滤池影响因素李冬

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42620106JOURNALOFHARBININSTITUTEOFTECHNOLOGYVol.42No.6Jun.20101222211.1500902.100124lidong2006@bjut.edu.cnANAMMOX、、ANAMMOX.NO-3-N500mg/L10mg/LNH+4-NNO-2-N.ANAMMOX.ANAMMOXANAMMOX.X703.1A0367-6234201006-0869-04EffectfactorsforANAMMOXbiofilteratroomtemperatureLIDong12WANGJun-an2TAOXiao-xiao2LIZhan2ZHANGJie11.StateKeyLaboratoryofUrbanWaterResourceandEnvironmentHarbinInstituteofTechnologyHarbin150090China2.KeyLaboratoryofBeijingforWaterQualityScienceandWaterEnvironmentRecoveryEngineeringBeijingUniversityofTechnologyBeijing100124Chinalidong2006@bjut.edu.cnAbstractInordertopromotetheengineeringapplicationsofanaerobicammoniumoxidationANAMMOXforurbansewagetreatmenttheimpactofnitratephosphateammoniaandnitriteontherunningperformanceofANAMMOXbiofilterreactoratroomtemperaturewasinvestigatedrespectively.ExperimentalresultsshowthatthereisnosignificantimpactontheTNremovalloadwhentheinfluentNO-3-Nconcentrationisin-creasedtoabout500mg/L.HowevertheTNremovalloadwilldropobviouslywhentheinfulentTPconcen-trationishigherthan10mg/Lwhichcanberestoredafterstoppingdosingphosphate.Appropriatelyincreas-ingtheconcentrationofNH+4-NandNO-2-NisbeneficialtotheimprovementofTNremovalload.AtroomtemperatureconditionsnitratebasicallyhasnoeffectontheANAMMOXbiofilterformunicipalwastewaterwithlowammonia.ButforphosphateithasacertainimpactontheactivityofANAMMOXandtheimprove-mentoftheinfluentphosphateconcentrationhasareversibleinhibitionforANAMMOXreactionintheurbansewagewithlowammonia.KeywordsANAMMOXbiofiltermunicipalwastewaterbiologicalnitrogenremovalroomtemperature2010-03-01.5087800308UWQA0880920062008ZX07208-003-0032008ZX07420-004-BJUT0012008ZX07208-005-003.1976—1938—.anaerobicammoniumoxidationANAMMOX1-5.ANAMMOX6-9.ANAMMOX.、、ANAMMOX.11.170mm2.0m5.0~8.0mm1.50m300mm200mm.1.123上向流进水出水取样口41—进水箱(140%L);2—蠕动泵;3—承托层;4—ANAMMOX陶粒滤床11.2/A/ONaNO2ANAM-MOX.CODCr=50~60mg/LρNH+4-N=60~80mg/LρNO-2-N1mg/LρNO-3N1mg/L0.18~0.74mg/L8~25℃pH=7.50~8.00.1.3NH+4-NNO-2-NN-1--NO-3-NDOWTWinoLabStirrOxGpHOAKLONWaterproofpHTestr10BNCpHCODCr.1d.“”.TNANAMMOX.22.1ANAMMOXANAMMOXANAMMOX———ANAMMOXAN-AMMOX.ANAMMOX2.60040020001%%%%%%2%%%%%%3%%%%%%%4%%%%%%5%%%%%%6%%%%%%%7%%%%%%8%%%%%%%9%%%%%10%%%%11t/d进水硝氮出水硝氮去除负荷硝氮质量浓度/(mg·L-1)4.03.02.01.00总氮去除负荷/(kg·m-3·d-1)22NO-3-N16.85mg/L500.31mg/LNO-3-NNO-3-NANAMMOX.NO-3-NANAMMOXTNNO-3-N500.31mg/L3.43kg/m3·dANAMMOXA/OCODNO-3-NTN.ANAMMOXTNCODANAMMOX.2.2ANAMMOXAN-AMMOXANAMMOX·078·42ANAMMOX.Na3PO4·12H2OANAMMOX.、ANAMMOX3.投加总磷浓度出水总磷总氮去除负荷1401201008060402001%%%%%%%%%%3%%%%%%%%%%%5%%%%%%%%%%7%%%%%%%%%%%9%%%%%%%%%10%%%%%%%%%13t/d总磷质量浓度/(mg·L-1)543210总氮去除负荷/(kg·m-3·d-1)3、3ANAMMOX.≤10mg/LANA-MMOX4kg/m3·dANAMMOX.10mg/LANAMMOX.=130mg/LANAMMOX0.67kg/m3·d16.8%ANAMMOX.ANAMMOX.ANAMMOX.ANAMMOXANAMMOX10.ANAMMOX24h2.06kg/m3·d51.5%.pHpH6.00~6.7010min24hANAMMOX3.55kg/m3·d88.8%.2.3ANAMMOXANAMMOX10~15℃ANAMMOX4.去除负荷去除率0.40.30.20.1%%%%%%%%%%%%%%100%%%%%%%%%%200%%%%%%%%%%300%%%%%%%%%%%400%%%%%%%%%%500氨氮质量浓度/(mg·L-1)总氮去除负荷/(kg·m-3·d-1)50403020100总氮去除率/%044200.52mg/L0.36kg/m3·d0.25kg/m3·d.ANAMMOX499.18mg/L500mg/LANAMMOX.ANAMMOX=1∶1.311.5.去除负荷去除率0.60.50.40.30.20.10200%%%%%%%%400%%%%%%%%600%%%%%%%800%%%%%%1%000%%%%1%200氨氮和亚氮质量浓度之和/(mg·L-1)50403020100总氮去除率/%总氮去除负荷/(kg·m-3·d-1)5·178·65.0.23kg/m3·d0.49kg/m3·d100.86mg/L137.85mg/L.0.49kg/m3·d241.12mg/L343.19mg/L400.00mg/L530.80mg/L0.27kg/m3·d.456ANAMMOX250mg/LANAMMOXANAMMOX.350mg/L530mg/L.ANAMMOX、ANAMMOX.提高氨氮浓度试验同时提高氨氮和亚氮浓度试验0.60.40.20总氮去除负荷/(kg·m-3·d-1)%%%%%%%%%%%%%%%%100%%%%%%%%%%%%200%%%%%%%%%%%%300%%%%%%%%%%%%400%%%%%%%%%%%%500氨氮浓度/(mg·L-1)631ANAMMOX.ANAMMOXANAMMOX.2ANAMMOX.ANAMMOX.3500mg/L、ANAMMOX.530mg/LANAMMOXANAMMOX.1MULDERAVANDEGRAAFAAROBERTSONLAetal.AnaerobicammoniumoxidationdiscoveredinadenitrifyingfluidizedbedreactorJ.FEMSMicrobiolo-gyEcology1995163177-183.2VANDEGRAAFAAMULDERADEBRUIJNPetal.AnaerobicoxidationofammoniumisabiologicallymediatedprocessJ.ApplEnvironMicrobiol19956141246-1251.3JETTENMSMSTROUSMVANDEPAS-SCHOO-NENKTetal.TheanaerobicoxidationofammoniumJ.FEMSMicrobiologyReviews199922421-437.4JETTENMSMWAGNERMFUERSTJetal.Mi-crobiologyandapplicationoftheanaerobicammoniumoxidationANAMMOXprocessJ.CurrentOpinionBiothchnology200112283-288.5VANDERSTARWRL.J.2007231815-19.6ABMAWRSCHULTZCEMULDERJWetal.FullscalegranularsludgeANAMMOXprocessJ.Wa-terSciTechnol2007558/927-33.7VANDEStarWRLABMAWRBLOMMERSDetal.StartupofreactorsforanoxicammoniumoxidationExperiencesfromthefirstfull-scaleANAMMOXreactorinRotterdamJ.WaterResearch200741184149-4163.8.J.20093051442-1448.9.-J.2009292219-224.10.J.2009251931-36.11STROUSMHEIJNENJJKUENENJGetal.Thesequencingbatchreactorasapowerfultoolforthestudyofslowlygrowinganaerobicammonium-oxidizingmicro-organismsJ.ApplMicrobiolBiotechnol1998504589-596.·278·42

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