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20119991 ENVIRONMENTALSCIENCEVol.20,No.1Jan.,1999*赵兴利 兰淑澄(, 100037E-mail:bmiep@public.netChina.com.cn) (PVA)-,PVA,,A/O,.,SBR.:7;10.3mg/(L·h),420mg/(L·h);NH4-N240mg/(L·h);4%,NH4-N35mg/L65mg/L,5h9h,NH4-N99%;COD230mg/L,NH4-N35mg/L,4h,COD86%,NH4-N90%.. ,,,,,.* (ProjectSupportedbyNa-tionalNaturalScienceFoundationofchina):59378343:,30,:1998-05-23StudyonTheProcessofRemovingNitrogenfromWastewaterUsingImmobilizedNitrobacteria*ZhaoXingli LanShucheng(BeijingMunicipalResearchAcademyofEnvironmentalProtection,Beijing100037E-mail:bmiep@public.netChina.com.cn)Abstract Theimmobilizedmicrobespelletsweremadefromentrappingcultivatednitrifyingactivatedsludgeusingpolyvinylalcohol(PVA)crosslinkedwithboricacid,PVAisentrapmentcarrierandpowderedactivatedcarbonisinorganiccarrier.ThesourceofnitrifyingactivatedsludgecomefromA/Osystem.Inbiologicalfluidizedbedreactor(BFBR),SequencingBatchReactors(SBR)systemtreatingcomposedNH4-Nwastewaterwascarriedout.Theexperimentresultswereasfollows:theimmobilizednitrobacteria'slifewasmorethansevenmonths;theoxygenusingrate(OUR)recoveredfrom10.3mg/(L·h)to420mg/(L·h);theNH4-Nre-movalloadingcouldreach240mg/(L·h).Whiletheimmobilizednitrobacteriapelletspackagepercentagewas4%,influentNH4-Nconcentrationwas35mg/L,reactiontimewas5h,theNH4-Nremovalefficiencyreach99%;influentNH4-Nconcentrationwasabout65mg/L,reactiontimewas9h,theNH4-Nremovalefficiencyalsoreach99%.WhentheinfluentCODisabout230mg/L,NH4-Nisabout35mg/L,reactiontimewas4h,theCODremovalefficiencycouldreach80%,theNH4-Nremovalefficiencyalwayskept90%orso.Inthisresearch,thesituationofmicrobegrowthanddistributionofimmobilizednitrobacteriawasobservedwithscanningelectronmicroscope.Keywords immobilization,nitrobacteria,wastewatertreatment,removalofnitrogen,FluidizedBedReactor(FBR),SequencingBatchReactors(SBR). .,NH4-NDOI:10.13227/j.hjkx.1999.01.01090%.PVA,1.78L,NH4-N2kg/(m3·d).,,,[1].、,、.1 1.1 (polyvinylAlcohol,PVA)-,PVA,,A/O,3mm、3mm,[2].1.2 ,、.VenkatasubramanianKarkare,[3].,1.1 NH4-N2 2.1 ,,1,(SequencingBatchReactor,SBR).7L.,300%.,1g/cm3,,,.,,.(1) ,PVA,,,.1,2,PVA,,,,,.,,,1.1PVA,,,,.1,PVA,,,,,.,,,.(2) ,3mm3mm3mm,,,,,,.(3) PVA40 20,,1,PVA,,1.16g/cm31.05g/cm3.(4) ,,,,,.,.(5) ,.,,1,8.0cm/s5.4cm/s.2.2 (1)(Rrp) 2,Rrp,420mg/(L·h),Rrp,.,7.2 Rrp(2)RrpNH4-N ,NH4-N.3,NH4-NRrp,NH4-N240mg/(L·h).[4],100—150mg/(L·h).3 RrpNH4-N (3) .:①PVA,,,.②PVA,,,,,.③,.2.3 CODCr(mg/L),NH4-N(mg/L).(1) SBR,,7%,4%.NH4-N30—35mg/L,5h,、、、3h.NH4-N99%,Rrp.NH4-N65mg/L,9h,、、、3h,NH4-N99%,Rrp.(2) ,NH4-N,4h,4%,COD240mg/L,NH4-N35mg/L,4.411 4 CODNH4-N 4,,COD,12d86.1%,NH4-N.,,,,.,,:①,0.022h-1,0.08~0.3h-1;②BOD5[5].,,..,.,,,,,,.3 (1),,,,.(2),.Rrp10.3mg/(L·h)420mg/(L·h),7,NH4-N240mg/(L·h).(3)NH4-N,99%,.(4)PVA,,,,.PVA,,,,.1 ,..,1997,18(1):83—852 ,..,1997,18(2):18—203 []L·S·,..:,1993.2464 .によるりんシステム.,1994,31(368):85 ..:,1992.2142 20
本文标题:固定化硝化菌去除废水中氨氮工艺的研究赵兴利
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