61 6 Vol.61 No.6 20106 CIESC Journal June 2010CANON王俊安,李 冬,张 杰,李 占,陶晓晓(,100124):。,(8~25℃)NH+4-N(60~90mg·L-1),,、3,/。,DO,,DO。pH,pH。:;;;;CANON:X703.1 :A:0438-1157(2010)06-1528-06RealizationofCANONprocessinbiofilterforwastewaterwithlowammoniaandroomtemperatureWANGJun'an,LIDong,ZHANGJie,LIZhan,TAOXiaoxiao(KeyLaboratoryofBeijingforWaterQualityScienceandWaterEnvironmentRecoveryEngineering,BeijingUniversityofTechnology,Beijing100124,China)Abstract:Biologicalautotrophicdenitrificationbasedonanaerobicammoniumoxidation(ANAMMOX)hasbeenconsideredasthemosteconomicalwayinbiologicalsewagetreatmentprocessesfornitrogenremovalpresently.Usingbio-ceramicfilterwithvolcanicactivity,urbansewagepilotstudywascarriedoutatroomtemperature(8—25℃)undertheconditionoflowNH+4-N(60—90mg·L-1),bychangingtheoperatingconditionssuchasaerationetc.Afterthreestages—nitrificationhangingfilm,preferrednitritebacteriaandculturinganaerobicammonia-oxidizingbacteria,CANON(completelyautotrophicammoniumremovalovernitrite)processisrealizedinbiofilter.TheresultsshowthatDOcontrolcanbethemainfactorforcontrollingreactorstartup.Throughcombinedtreatmentofaerationatthetopofwatercolumninbiofilterandinternalrecyclingoftreatedwaterwithoxygen,thecontrolofDOconcentrationinthebiofilmsystemiseasilyachieved.Furthermore,thereactioncyclecanbejudgedfromthechangeofpHvalueintherunprocessanditssecond-jumpisasignalofendofreactionperiod.Keywords:partial-nitrosification;ANAMMOX;biologicalnitrogenremoval;biofilter;CANONprocess 2009-12-03,2010-02-03。:(1981—),,。:(50878003);(8092006);(2008ZX07208-003-003,2008ZX07420-004-BJUT001,2008ZX07208-005-003)。 Receiveddate:2009-12-03.Correspondingauthor:WANGJun'an,wangjunan001@163.comFoundationitem:supportedbytheNationalNaturalScienceFoundationofChina(50878003). (anaerobicammoniumoxidation,ANAMMOX)[1-2]/,CO2,。ANAMMOXNH+4-N、NO-2-N,NH+4-N,ANAMMOX。,/,SHARON(singlereactorforhighammoniumremovalovernitrite)[3]-ANAM-MOXOLAND(oxygenlimitedautotrophicnitrificationanddenitrification)[4],SNAP(single-stagenitrogenremovalusingANA-MMOXandpartialnitritation)[5]CANON(completelyautotrophicammoniumremovalovernitrite)[6]。ANAMMOX,(30℃)NH+4-N(100mg·L-1)[7-11],NH+4-N。,/(A/O),,NH+4-N/,ANAMMOX。1 1.1 ,1,185mm,3.0m,6.0~8.0mm,1.4m,200mm,200mm,1.0m,,。1.2 A/O,1 Fig.1 Experimentalarrangementschematicdiagramofnitrosificationbiofilter :CODCr50~100mg·L-1;NH+4-N60~90mg·L-1;NO-2-N1mg·L-1;NO-3-N1mg·L-1;TP0.05~1.00mg·L-1;8~25℃;pH7.5~7.8。,,DO,。1.3 NH+4-N;NO-2-NN-(1-)-;NO-3-N;DOWTWinoLabStirrOxG;pHOAKLONWaterproofpHTestr10BNCpH;CODCr。2 2.1 CANON,,,DO2~4mg·L-1,15d,NO-3-NTN50%,,1,AOB,·1529· 6 :CANON,,DO,DO(7~8mg·L-1),4.02m·h-1,10,(NH+4-N200mg·L-1,1500mg·L-1)NOB,2,DO,80%,TN,,DO,TN,3,SBR(12h,),TN80%,《》(GB18918—2002)A,CANON。2.2 SBR2.79m·h-1,22.5~23.5℃SBR,NH+4-N、TNCOD,NO-2-N,1~11h2.6~4.0mg·L-1,NO-3-N,pH,。NH+4-N、NO-2-N、NO-3-N、TN、CODpH2。2,NH+4-NTN,,R20.99,5.69mg·L-1·h-14.82mg·L-1·h-1。,NO-2-N,NO-3-N,0.92mg·L-1·h-1,TNNH+4-N,3。,COD,83.55mg·L-129.89mg·L-1,64.2%,4h,8h3.27,,,COD,COD,、,,。,pH,0~1h11~12h,AB2,,NH+4-N,,CO2,pH,1~4h4~11h,CODNH+4-N/。3 NH+4-NTNFig.3 RelationshipofconcentrationchangebetweenNH+4-NandTN2.3 ,4.02m·h-1,2.21.44。SBR,6h,2.2·1530· 61 0.5,TN8.91mg·L-1·h-1,1.85,NH+4-N、NO-2-N、NO-3-N、TN、pH4。4,2.2。NO-2-N1.23~2.62mg·L-1,NH+4-N、TNNO-3-N1h,58.2%、51.8%50.2%,,,DO,NH+4-N、TN,,,1h,,,1~6hNH+4-N6.00mg·L-1·h-1,。,,pH,AB。1,,NH+4-N、NO-2-NNO-3-N70.74、0.98、0.34mg·L-1,20.5~24.0℃,pH7.94~8.16,29.3ml·min-1、0.40m·h-1,NH+4-N、NO-2-NNO-3-N0、0.73、10.17mg·L-1,,,TN2.83mg·L-1·h-1,84.9%。SBR,TN,,,,pH,7.9~8.1,。10~15℃SBR,TN,2d,。,1,,,,:CODCr25~50mg·L-1,NH+4-N0~5mg·L-1,NO-2-N0~1mg·L-1,NO-3-N5~15mg·L-1,TP0.05~1.00mg·L-1,0.01~2NTU,。3 3.1 CANONDOAOBDONOB[12],DO,AOB,。,,DO,DO,,AOBDO,。,DO,,NH+4-NNO-2-N,ANAMMOX,ANAMMOX,,NH+4-NNO-2-NN2,TN。TNANAMMOX,。,,,,,,TN,NH+4-NNO-2-NNO-3-N,·1531· 6 :CANON,NH+4-N,TN,TN,。,,,1.20m·h-1,NaNO2ANAMMOXNO-2-N,NH+4-N77.57mg·L-1、NO-2-N83.62mg·L-1、18~21℃11.5h,NH+4-N、NO-2-NNO-3-N47.56mg·L-1、57.10mg·L-16.51mg·L-1,1∶1.20∶0.14,ANAM-MOX1∶1.32∶0.26[13],,pH8.0611.5h8.39,[14-15],,ANAMMOX,TNANAM-MOX,SBR/。3.2 ,DO,/。DO,TN,,DO,NOB,NO-3-N,TN。SBR,/。,SBR,,,,、。,SBR,pH,[16-18]。,SBR,pH,pH/,DO。SBR/,NH+4-N,ANAMMOX,/———A/O,、,。4 (1)DONH+4-N/,,DO。(2)SBRNH+4-N/,pH,pHSBR。(3)NH+4-N,/,,/A/O。References[1] MulderA,vandeGraafAA,RobertsonLA,etal.Anaerobicammoniumoxidationdiscoveredinadenitrifyingfluidizedbedreactor.FEMSMicrobiologyEcology,1995,16(3):177-183[2] vandeGraafAA,MulderA,deBruijnP,etal.Anaerobicoxidationofammoniumisabiologicallymediatedprocess.Appl.Environ.Microbiol.,1995,61(4):1246-1251[3] HellingaC,SchellenAAJC,MulderJW,etal.TheSHARONprocess:aninnovativemethodfornitrogenremovalfromammonia-richwastewater.Wat.Sci.Tech.,1998,37:135-142[4] HanakiK,WantawinC,OhgakiS.Nitrificationatlowlevelsofdissolvedoxygenwithandwithoutorganicloadinginasuspendedgrowthreactor.WaterResearch,1990,24(3):297-302[5] FurukawaK,LieuPK,TokitohH,etal.Developmentof·1532· 61 single-stagenitrogenremovalusinganammoxandpartialnitritation(SNAP)anditstreatmentperformances.WaterScienceandTechnology,2006,53(6):83-90[6] Str