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当前位置:首页 > 临时分类 > AF反应器对芳香族化合物反硝化降解特性研究王文燕
AF,*,,(, 100875):、,(AF),,CN.,,AF,COD1000mgL,、60mgL,COD90%,84%..CN5~30,90%,CN;COD、CN,CN15,COD、,90%、78%82%.:;AF;;;;:X703.1 :A :0250-3301(2007)03-0540-05:2006-03-24;:2006-07-13:(50508006);(973)(2004CB418502):(1981~),,,.*,E-mail:xchquan@yahoo.com.cnStudyontheTreatmentofAromaticHydrocarbonContainingWastewaterbyanAnaerobicFilterReactorUnderDenitrifyingConditionWANGWen-yan,QUANXiang-chun,YANGZhi-feng,HEMeng-chang(StateKeyJointLaboratoryofEnvironmentalSimulationandPollutionControl,SchoolofEnvironment,BeijingNormalUniversity,Beijing100875,China)Abstract:Withbenzene,naphthaleneandbiphenylasthemodelaromatichydrocarbon,thetreatmentofaromatichydrocarboncontainingwastewaterbyananaerobicfilter(AF)reactoroperatedincontinuousmodeandunderdenitrifyingconditionwereconducted.Withglucoseasthesupplementedcarbon,theinfluenceofCNratioonthedegradationoforganiccompoundswasalsoinvestigated.ResultsshowedthattheAFreactorcoulddegradethesearomatichydrocarbonseffectivelyunderabovementionedconditions.WhentheinfluentCODconcentrationwas1000mgL,andbenzene,naphthaleneandbiphenylconcentrationwas60mgL,theremovalefficiencyforCODandaromatichydrocarbonswas90%and84%,respectively.Benzenewasmoreeasilydegradedthannaphthaleneandbiphenylunderdenitrifyingcondition.WhenCNwasintherange5~30,benzeneremovalpercentagewasalwaysatabout90%,andCNratiodidnothaveobviouseffectonthedegradationofbenzene.ThedegradationofnaphthaleneandbiphenylandtotalCODwasgreatlyinfluencedbyCN.WhenCNwas15,thehighestremovalpercentagewasachievedanditwas90%,78%and82%forCOD,naphthaleneandbiphenyl,respectively.Keywords:denitrify;AFreactor;degradation;benzene;naphthalene;biphenyl ,、,,,,,[1~3].,,(PAHs),、、、,CO2[4~7].,,,.,、.(AF),,.1 1.1 (AF),1.,4.5L,90mm,1000mm.5~10mm,800mm.2,,,.28320073 ENVIRONMENTALSCIENCEVol.28,No.3Mar.,2007DOI:10.13227/j.hjkx.2007.03.0171 AFFig.1 StructureoftheAFreactor AF2.,,,,30℃.,.24h.1. 2. 3. 4. 5.6. 7. 8. 9. 10.11. 12.2 AFFig.2 SchematicdiagramofthesetupoftheAFreactor 1.2 、、,1∶1∶1.,,,C∶N∶P=200∶5∶1NH4Cl、KH2PO4,pH7.0~7.4.,VSS5.2gL,VSSMLSS0.4.1.3 (1) ,,NaNO3.,,,3.(2)CN ,,NaNO3,CODNO-3-NCN,,COD、.(3) ,,COD、、NO-3、NO-2,.1.4 、、Waters1525,8μL,∶=87∶13,1mLmin,,254nm.NO-3-NNO-2-NN-(1-)-;COD;MLSS.2 2.1 AFAF,230d.,,,1000mg(L·d).COD3、4.,、,COD50%,,,1d.,COD5413:AF 3 AFCODFig.3 RemovalofCODatvariousaromaticsorganicloadingsbytheAFreactorunderanaerobicdenitrifyingcondition 4 AFFig.4 DegradationofaromatichydrocarbonunderdenitrifyingconditionbytheAFreactoroperatedincontinuousmode,91%.44d,、,20mgL,COD,79%,,COD,,3,93%,0.5mgL,,3.76d,60mgL,COD,,.98d,100mgL,COD400mgL,60%,,.117d,60mgL,,COD100mgL,90%,,2mgL;,,,4mgL.,,NO-35.1~140d,NO-3-N30mgL,NO-3,NO-3NO-2.141d,NO-3-N,542 28 5 AFNO-3Fig.5 RemovalofNO-3bytheAFreactorunderanaerobicdenitrifyingcondition CN.NO-3-N50mgL,CN20,NO-3,NO-3,NO-2,.NO-3,CN,NO-3,NO-2.CN15,AF,.2.2 ,、.1,,.COD3,6.6,CN10~20,COD80%,CN15,,90%.3.,,CN,CN5~30,90%.CN,.CN15,,82%78%.,,;CN10CN20,55%.6CN15.CN.CN,6 CNFig.6 EffectofCNonthedegradationoforganiccompounds ,,.CN,、,,.Jiunn[10],CN.,(92%~97%)CN(、、).,(97%~100%)CN.[7]USB,CN15,.Khursheed[3],CN,,,,,;CN,,,5433:AFCN.,,,CN;,2CN.2.3 CN15,,,78.7 AFFig.7 ChangesoftheorganiccompoundsalongtheheightofAFreactor8 AFNO-3NO-2Fig.8 ChangeofNO-3andNO-2concentrationalongtheheightofAFreactor 7,,,,.50cm,COD,3;50cm,、、75%、79%、83%,COD37%.70cm,COD,,77%COD.,,,,,,,COD.8NO-3,,NO-3,NO-2.50cm,NO-3NO-2,NO-2,NO-2,70cm,NO-2.3 (1)AF,,COD1000mgL,、60mgL,COD90%,83%.(2),.(3)CN5~30,90%,CN;COD、CN,CN15,COD、,90%、78%82%.:[1],.[J].,2001,21(1):42~46.[2],,,.[J].,2004,24(5):323~326.[3]KhursheedK,GuptaSK.Continuousbiotransformationandremovalofnitrophenolsunderdenitrifyingcondition[J].WaterResearch,2003,37:2953~2959.[4]KarlJR,StuartES.Anaerobicbiodegradationofnaphthalene,phenanthrene,andbiphenylbyadenitrifyingenrichmentculture[J].WaterResearch,2001,35(1):291~299.[5]KarlJR,JoanneCCS,RobertAS,etal.Anaerobicnaphthalenedegradationbymicrobialpureculturesundernitrate-reducingcondition[J].AppliedandEnvironmentalMicrobiology,2000,66(4):1595~1601.[6]RobertoA,LauraP,JoseLM,etal.AnaerobicPAHdegradationinsoilbyamixedbacterialconsortiumunderdenitrifyingcondition[J].Chemosphere,2005,60:1231~1236.[7],,.[J].,2005,31(3):51~54.[8],.USB[J].,2004,5(8):72~75.[9].[M].:,1997.188~189.[10]JiunnJH,JuS.InfluencesofcarbonsourceandCNratioonnitratenitritedenitrificationandcarbonbreakthrough[J].BioresourceTechnology,1995,54:45~51.544 28
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