高温ASBR处理热水解污泥的梯度升温法启动试验研究欧阳二明

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ASBR1,2,1*,3,4(1.,100084;2.,330031;3.,100083;4.,710054):、ASBR.,131dASBR.3(35℃※40℃※47℃※53℃),,※(35℃※40℃)、※(47℃※53℃),※(40℃※47℃)、、COD,,40℃47℃.,2.038Ld,72.0%,COD(CH4COD)188.8mLg,TCODSCOD63.8%83.3%.DGGE,,(35℃)(53℃).:;;;;PCR;DGGE:X705 :A :0250-3301(2009)04-1105-05:2008-05-27;:2008-06-24:(863)(2006AA06Z384):(1976~),,,,.*,E-mail:solid@tsinghua.edu.cnGradientElevationofTemperatureStartupExperimentofThermophilicASBRTreatingThermal-HydrolyzedSewageSludgeOUYANGEr-ming1,2,WANGWei1,LONGNeng3,LIHuai4(1.DepartmentofEnvironmentalScienceandEngineering,TsinghuaUniversity,Beijing100084,China;2.SchoolofCivilEngineeringandArchitecture,NanchangUniversity,Nanchang330031,China;3.SchoolofCivilandEnvironmentalEngineering,UniversityofScienceandTechnologyBeijing,Beijing100083,China;4.DepartmentofEnvironmentalScienceandEngineering,ChanganUniversity,Xian710054,China)Abstract:Startupexperimentwasconductedforthermophilicanaerobicsequencingbatchreactor(ASBR)treatingthermal-hydrolyzedsewagesludgeusingthestrategyofthestep-wisetemperatureincrement:35℃※40℃※47℃※53℃.Theresultsshowedthatthefirststep-increase(from35℃to40℃)andfinalstep-increase(from47℃to53℃)hadonlyaslighteffectonthedigestionprocess.Thesecondstep-increase(from40℃to47℃)resultedinaseveredisturbance:thebiogasproduction,methanecontent,CODeffluentandmicroorganismallhavestrongdisturbance.AtthesteadystageofthermophilicASBRtreatingthermal-hydrolyzedsewagesludge,theaveragedailygasproduction,methanecontent,specificmethaneproduction(CH4CODinfluent),TCODremovalrateandSCODremovalratewere2.038Ld,72.0%,188.8mLg,63.8%,83.3%respectively.TheresultsofSEMandDGGEindicatedthatthedominantspeciesareobviouslydifferentatearlystageandsteadystage.Keywords:thermal-hydrolyzedsewagesludge;anaerobicsequencingbatchreactor(ASBR);gradientelevationoftemperature;startup;PCR;DGGE  (ASBR)HRT()SRT()、MCRT()[1~3],[4~6].(thermalhydrolysis)[7~9],.“-”[10~12].ASBR,ASBR,PCR-DGGE.1 1.1 ASBR15cm、32.5cm.ASBR5L,4L,1L.30420094      ENVIRONMENTALSCIENCEVol.30,No.4Apr.,2009DOI:10.13227/j.hjkx.2009.04.024,.,..1.2 .6(:3.2mm×3.2mm),170℃、30min.(3℃).ASBRASBR.1.,SCOD601mgL12434mgL,.1 Table1 Characteristicsofrawandthermal-hydrolyzedsewagesludgepH6.806.66(CaCO3)mg·L-18001021TSg·L-136.28033.056VSg·L-123.50620.646SSg·L-133.56123.033VSSg·L-118.66015.615TCODg·L-140.31738.857SCODg·L-10.60112.434VFAg·L-145423441.3 ASBR,TS24.748gL、VS12.272gL、SS23.668gL、VSS11.220gL,VSSSS0.474.3L,1LHRT20d、(TCOD)1.943kg(m3·d).ASBR24h,30min,20h,3h,30min.ASBR10minh.ASBR(35℃)(53℃):35℃※40℃※47℃※53℃.1~15d,ASBR35℃;16~29d40℃;30~91d47℃;92~131d53℃.1.4 pHOrion868pH;ZDJ-4A:(TS)、(VS)、(SS)、(VSS)[13];COD[13].SQ-206(FID);SQ-206(TCD);.FEIQUANTA200.1.5 DNA、PCRDGGEMPBiomedicals(FastDNA★RSPINforSoilKit)DNA,PCR.16SrDNAPCRPRBA8FPRUN518R,(PRUN518R)GC.PCRMJ-RESEARCHPTC-200PCR.:94℃7min;94℃1min;55℃30s,72℃1min,24;72℃10min.PCR1%,.510bpDGGE.PCR35%~60%(8%),D-Code(Bio-RAD).100V、60℃12h.,SYBRGold,(UVP)[14].2 2.1 (ASBR),,ASBR.1131d.,(),3L1L,,,,1d3.337L,2d2.680L,200mL(HRT=20d),,.35℃15d,40℃,(1.682Ld2.67Ld),1.600Ld,14d(40℃),,1.621Ld(40℃).29d,40℃53℃,,29d1.537Ld30d0.740Ld,,1106      3036d(0.030Ld),,,,.,37~47d,(0.12Ld1.92Ld),.,,,,48~51d2.5Ld.52~91d,47℃,1.380~1.960Ld.92d,47℃53℃,.111~131d,,1.890~2.24Ld,2.038Ld,COD(CH4COD)188.8mLg,.,1~15d(35℃)、16~29d(40℃)、30~91d(47℃)、92~131d(53℃)72.3%、72.6%、60.2%、72.0%,40~47℃,.1 ASBRFig.1 DailygasproductionoftheASBR2.2 pHpH,pH.,pH..2ASBRpH.131d,pH6.97~7.94,40℃47℃,pH,,,,,pH.(111~131d),pH7.58~7.88,(CaCO3)5685~5795mgL(5739mgL),.2 ASBRpHFig.2 pHprofilesinoutflow2.3 COD3ASBRTCODSCOD.,TCOD5.609gL14.282gL,SCOD0.607gL2.146gL.47℃33d,TCODSCOD9.211gL1.403gL,,(40℃)(47℃),,COD.(111~131d),TCODSCOD13.862~14.282gL9.362~9.782gL,63.8%83.3%.3 ASBRSCODTCODFig.3 SCODandTCODprofilesinoutflow2.4 .ASBR,.11074:ASBR,VSS,,[15].4,,48.9nmolmL,35℃40℃,32.1nmolmL(18d),5d51.6nmolmL.35~40℃,,.2(40~47℃),:33d(23.3nmolmL),,48d31.7nmolmL;(48~89d),89d116.6nmolmL.3(47~53℃),,,125d124.3nmolmL.4 ASBRFig.4 MicroorganisminASBR2.5 (SEM)ASBR(35℃)(53℃),5.,ASBRSEM,.,,、,;,,、,,,,、.,DNA,PCRDGGE,6.1ASBR,2.2,26,5 ASBRFig.5 SEMphotoofthemicroorganismsintheASBR6 Fig.6 EubacteriacommunitystructuresintheASBRatearlystageandsteadystageofstartup1a、1b、1c、1e2a、2b、2c、2f,4;,,,,,.,11108      301b、1c、1d,22d、2e、2f,3,.,ASBR、,.3 (1),131dASBR.,ASBRTCODSCOD63.8%83.3%.(2)3(35℃※40℃※47℃※53℃),,※(35℃※40℃)、※(47℃※53℃),※(40℃※47℃)、、COD,,40℃47℃.(3),2.038Ld,72.0%,COD(CH4COD)188.8mLg.(4)DGGE,,(35℃)(53℃).:[1] DagueRR.Initialstudiesontheanaerobicsequencingbatchreactor[J].WaterScienceandTechnology,1992,26(9):2429-2432.[2] IoannisS,DavidMB.Improvinganaerobicsequencingbatchreactorperformancebymodifyingoperationalparameters[J].WaterResearch,2002,36(1):363-367.[3] AngenentLT,SungS,RaskinL.Methanogenicpopulationdynamicsduringstartupofafull-scaleanaerobicsequencingbatchreactortreatingswinewaste[J].WaterResearch,2002,36(18):4648-4654.[4] RuizCJ,TorrijosM.Treatmentofwinerywastewaterbyananaerobicsequencingbatchreactor[J].WaterScienceandTechnology,2002,45(10):219-224.[5] HurJM,ChangD,ChungTH.Dynamicprocessresponsetosludgethickeningbehaviorsintheanaerobicsequencingbatchreactor

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