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当前位置:首页 > 商业/管理/HR > 公司方案 > 不同上升流速IC反应器OCC废水启动过程功能菌群落分布周轩宇
。*2012A032300015。ICOCC*1121221.5106402.510006IC“+OCC”。COD、VLR、SMA、F420、DHAFISH。R12730.76%52.63%2.76R257R233.74%1.162.67。ICR2ICR1。ICOCCF420X793A1671-4571201306-0091-07ICPAQUES2080UASB1、、、。IC4~8m16~25m2IC。IC。ICIC1/2。1。IC、。IC。ICIC3。。FluorescenceinsituhybridizationFISH。ICIC。19《》2013326DOI:10.19696/j.issn1671-4571.2013.06.02311.1ICR11/2ICR29L1/3。3000mg/LCOD24h。COD5kgCOD/m3·dCOD15kgCOD/m3·d。COD80%。R12715kgCOD/m3·d4.8h10。R25715kgCOD/m3·d4.8h18。11.2“+OCC”COD∶N∶P=200∶5∶1。、KHPO4、NH4Cl、CaCl2、NaHCO3COD10%、20%、50%1/10000411/g·L-1FeSO4·7H2O1.12MnCl2·4H2O0.2NiCl2·6H2O0.02NH46Mo7O24·4H2O3.6/g·L-1CaCl2·6H2O0.8ZnCl20.02CuSO4·5H2O0.018H3BO30.02EDTA0.41.3。TSS105.95g/LVSS70.4g/LVSS/TSS0.6611.07mLCH4/hgDHA65.603TFμg/mLF4200.1165μmol/gVSS50.00%±2.33%2.47%±0.19%13.3%±0.42%。9L1/3。1.4CODXJ-Ⅲ5VSSTSS6F42067TTC89。1.5FISH1.5.1FISH、。311。SYNM700SYNM700Syn-trophomonasspp.10AWAWAcetobacteriumsp.E.limosum11MG1200MG1200Methanomicrobia-les121。TAMRAFITC5'3'HPLC。29PaperScience&Technology2013Vol.32No.625’to3’SYNM700ACTGGTRTTCCTC-CTGATTTCTASyntrophomonasspp.TAMRAAWGGCTATTCCTTTC-CATAGGGAcetobacteriumsp.E.limosumFITCMG1200CGGATAAT-TCGGGGCATGCTGMethanomicrobialesTAMRA1.5.2FISH13-20℃。K141546℃2h50%、80%、95%、100%1∶85ng/mL1646℃Thermo-BriteIris2h。。DAPI17。LeicaTCSSP5Leica18。ImageProPlus1920。1.5.3。、ImageProPlus119DAPI。%=×100%122.12。R19kgCOD/m3·dCOD73.2%COD80%27R115kgCOD/m3·d4.8hCOD92.7%。R1R2COD43.5%CODCOD80%。R2R1。R1R2R2。R2R1COD80%。57R215kgCOD/m3·d4.8hCOD92.3%。R2。R2。ICR2ICR1。2COD2.2、F420。5kgCOD/m3·d、10kgCOD/m3·d、15kgCOD/m3·dVSSF420。3、439《》2013326F420、R1R2。11.07mLCH4/h·gF4200.1165μmol/gVSS13.3%±0.42%。R126.66mLCH4/h·gF4200.2602μmol/gVSS50.00%±1.24%R222.97mLCH4/h·gF4200.2328μmol/gVSS42.86%±1.12%。。5kgCOD/m3·dR2VFAR213.30%±0.42%12.12%±0.52%。。3、4、F420。R2R1R2R1R2R1。34F4202.321。、lhμgTF。532.8TFμg/mL·h5kg-COD/m3·dR172.1TFμg/mL·hR254.6TFμg/mL·hR197.1TFμg/mL·hR2102.8TFμg/mL·h。。R2。R2R1R1R2R1。R2R2R1R2R1R2R1。R2R2。。49PaperScience&Technology2013Vol.32No.6、。52.4IC7。2R130.76%52.63%2.76R233.74%1.162.67R2R12.28%R141.38%R12.28%。622。R2。R2、R2R1。。350.00%±2.33%2.47%±0.19%13.3%±0.42%R165.38%±2.09%3.77%±0.17%50.00%±1.24%R266.87%±1.71%5.33%±0.07%48.86%±1.12%59《》2013326633.1ICR127d15kgCOD/m3·d4.8hCOD92.7%。ICR257d15kgCOD/m3·d4.8hCOD92.3%。R130.76%52.63%2.76R233.74%1.162.67。3.2、。。3.3R2。7FISH69PaperScience&Technology2013Vol.32No.6ICR2ICR1。1.J.2010503400-402.2.M.2005.108.3.EGSBJ.2006221562-66.4..ICJ.201127333-36.5.Umax-CH4J.19851431-35.6.M.1990.7.F420J.19908211-15.8.MBRJ.2006231231-33.9.TTC-J.1995311-13.10HertoDATsukasaIKazumiYetal.PhylogeneticandFunction-alDiversityofPropionate-oxidizingBacteriainanAnaerobicDi-gestersludgeJ.ApplMicrobiolBiotechnol200775673-683.11KüselKPinkartHCDrakeHLetal.AcetogenicandSulfate-re-ducing-bacteriaInhabitingtheRhizoplaneandDeepCortexCellsoftheSeaGrassHalodulewrightiiJ.ApplEnvironMicrobiol1999655117-5123.12RaskinLStrinmleyJRittmannBEetal.GroupSpecific16SRNAhybridizationProbestoDescribeNaturalCommunitiesofmethanogensJ.ApplEnvironMicrobiol1994601232-1240.13NuriaFEmilianoEDRicardoAetal.AnalysisofMicrobialCommunityduringBiofilmDevelopmentinanAnaerobicWastewatertreatmentreactorJ.MicrobiolEcol200861121-132.14.FISHJ.2008404546-549.15.J.2002314362-363.16.J.20103171554-1560.17.J.20113045-8.18.J.201218149-50.19WallnerGAmannR.BeikerW..OptimizingFluorescentinSituHybridizationwithrRNA-targetedOligonucleotideProbesforFlowCytometricIdentificationofMicroorganismsJ.Cytometry199314136-14320.FISHJ.20074761038-1043.21.D.2006.17-18.22.J.2006262183-187.FunctionalBacteriaCommunityDistributioninDifferentRiseVelocityICReactorStart-upProcedurebyOCCWastewaterZhouXuan-yu1MaYong-wen12WanJin-quan12WangYan21.StateKeyLaboratoryofPulpandPaperEngineeringSouthChinaUniversityofTechnologyGuangzhou510006GuangdongChina2.CollegeofEnvironmentandEnergySouthChinaUniversityofTechnologyGuangzhou510006GuangdongChinaAbstractThetraditionalICreactorR1andthenewtwopointreturnflowICreactorR2whoserisevelocitywasabout1/2ofthetraditionalICreactor’sinthesameotherconditionswasstartedupundernormaltemperature.Bythewayofenteringwaterof“composedwaterbyglucose+OCCwastewater”theratioofOCCwastewatertocomposedwatercouldbegraduallyincreased.CODremovalratevolumetricloadingrateVLRspecificmetha-nogenicactivitySMAcoenzymeF420dehydrogenaseactivityDHAinthetwoICreactorsinthestart-upproce-durewasresearchedandfluorescenceinsituhybridizationFISHwasusedtobeacharacterizationoffunctionalbacteriacommunitydistributioninthetworeactors.Theresultsshowasthestart-upwassuccesscomparedwiththeseedsludgetheabundanceofthebutyrate-oxidizingacetogenicbacteriaSyntrophomonasspp.increasesby30.76%thehomoacetogenicbacteriaAcetobacteriumspeciesE.limosumincreasesby52.63%andmethanomi-crobiummethanomicrobialesincreasesby276%inR1.Andtheabundanceofthebutyrate-oxidizingacetogenicbacteriaSyntrophomonasspp.increasesby33.74%thehomoacetogenicbacteriaAcetobacteriumspeciesE.limo-sumincreasesby116%andmethanomicrobiumMethanomicrobialesincreasesby267%inR2.AlthoughR2tookalongtimetobestartedupreducedthedifficultyofmachiningandmaintenancegreatlybyreducingtheeffectiveheight.AndR2
本文标题:不同上升流速IC反应器OCC废水启动过程功能菌群落分布周轩宇
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