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a,a,a,a,b,a,a(a.;b.,541004):4,,,6.6%,(15e),20,3555e,41d,,,,35e31d,20e,,20e,20e,,,,:;;;;:S216.4:A:1003-188X(2010)04-0170-050,,[1],,[2];,,,,,,,[3-5],,,,,11.1,:2009-07-01:/0([2007]71);(0801Z005):(1983-),,,,(E-mail)willenwe@i163.com:(1962-),,,,,(E-mail)chenggw@glite.edu.cn,150L,,,,1Fig.1Constanttemperatureanaerobicdigestiondevice1.2,,1.31.3.1,,1#,2#,3#4#4,,6.6%,39.2%,25.5kg#170#201044(15e),20,3555e,40d1.3.24,,4,,1,,20,3555e1Tab.1Materialofanaerobicdigestion/kg/kg/%1#7.41.485.82.30.200.815.80025.51.686.6TS19.9%TS8.6%2#7.41.485.86.90.200.811.20025.51.686.6TS19.9%TS2.9%3#7.41.485.83.10.200.815.00025.51.686.6TS19.9%TS6.5%4#7.41.485.810.50.200.87.60025.51.686.6TS19.9%TS1.9%1.3.3:(TS)1)TS105~110e2)6L(FLJ-A,),1,24h,(Clapyronequation)98kPa25e,3)SP-6890():,(TDX-01);1.5m@3mm;60e;80e;100e;;,100uL4d1,22.122Fig.2Biogasdailyyieldatdifferenttemperatures2,20d,,;35e3d;55e,,,[6];(15e)20e,,41d33Fig.3Cumulativebiogasyieldatdifferenttemperatures3:,55e,693.4L;35e,641.7L;20e471.6L294.1L,,,[7],,35e15d;#171#20104455e27d;20e36d;,,,,,,2.2[8],,,9d,41d,8,3,22Tab.2Gaschromatographtestresultsofbiogascomponent%/d1#2#3#4#942.7210544.3928047.8659550.418051341.5789046.5986055.0179558.530101842.4855548.7429059.5204555.440702244.0310054.0094555.3230550.081952741.6261559.4678053.8579056.439953144.4441062.8741554.5245558.086853642.8166560.9644053.6855551.757454145.4992060.5197053.5795048.11575/d1#2#3#4#937.0783550.4135547.5502037.710201349.3591548.0970035.9230531.389501845.8223045.0007537.5092532.675052249.7105041.5841539.8439035.119752753.1915038.4248541.3247534.133803152.7151035.5092040.8096031.778503656.0274037.4590041.7497037.521604150.5878037.9455040.6057037.40840/d1#2#3#4#920.200655.193704.5838511.87170139.061955.304359.0590510.080351811.692106.256302.9702511.88425226.258554.406404.8330014.79830275.164402.112304.817309.42630312.840801.616704.6659010.13470361.559001.576704.5647010.72100413.913001.534905.8148014.475902.2.12:1)1#,,2),,,,;,,,,,,3),,,4)55e,2.2.222,,31d41d[9],33:1),;,,2)31d,,20e,35e55e89.3,199.2,318.0333.0L,41d70.4%,82.2%,96.0%9011%,,35e31d41d96%,,31d3)(15~35e20e,35~55e20e),31d41d,35~55e1.3%,4.7%8.1%,11.6%,15~35e196.6%,256.1%118.2%,161.2%;35~55e14313%157.1%,15e~35e29.7%26.8%,,,,,;[10],,#172#2010443Tab.3Cumulativeyieldandcontentofbiogascomponent/d/L/L/L/L/%/%/%1#89.395.223.7208.242.945.711.4312#199.2183.220.0402.449.545.55.03#318.0268.830.7617.551.543.55.04#333.0217.674.8625.353.234.812.01#126.8142.325.0294.143.148.48.5412#242.3208.820.5471.651.444.34.33#331.2278.831.7641.751.643.44.94#369.7242.281.5693.453.334.911.82.3,20e35e55e31d,44Tab.4EnergyconsumptionandproductionduringanaerobicdigestionofswinemanurekJ1#00003509.493509.492#507.28634.41398.611540.297828.566288.273#2029.102537.631594.436161.1612497.406336.244#4058.215075.253188.8612322.3213086.90764.583.93@107J/m34:1)4#55e,94.2%[11],,,2)1#,,,,,3)2#20e3#35e,,,,,3#4),,31d,32.9%,69.1%,,,,,31),2),,;,,,,,,35e31d,;20e20e3),,,:[1],,,.#173#201044[J].,2008,19(8):1817-1822.[2],,,.[J].,2004,15(11):2179-2183.[3]BuswellAM,HatfieldWD.Laboratorystudiesofsludgedigestion.MillerTL.AnaerobicFermentations[C]//Urba-na:StateofIllinoisDepartmentofRegistrationandEduca-tion,1936.[4]AhringBK,IbrahimAA,MladenovskaZ.Effectoftem-peratureincreasefrom55eto65eonperformanceandm-icrobialpopulationdynamicsofananaerobicreactortreatingcattlemanure[J].WaterResearch,2001,35:2446-2452.[5]KettunenRH,RinalaJA.Theeffectoflowtemperature(5-20e)andadaptationonthemethanogenicactivityofbio-mass[J].ApplMicrobiolBiotechno,l1997,48:570-576.[6]Young-ChaeSong.Mesophilicandthermophilictemperatureco-phaseanaerpbicdigestioncomparedwithsingle-stagemesophilicandthermophilicdigestionofsewagesludge[J].WaterResearch,2004,38:1653-1662.[7]SanthaH,SungS.Valuableby-productsrecoveryfromcattlewastesusingtemperature-phasedanaerobicdigestionprocess[C]//HanzeM.WEFsBiosolidsSpecialtyConfer-enceVerona:LagoOrtaPress,2001.[8],,.[J].,2003,23(6):42-46.[9]CHENGGuanwen,ZHUZongqiang,HULening,eta.lRe-seachaboutbiogasfermentationofvariouscommon[C]//TheProceedingsoftheChinaAssociationforScienceandTechnology.Beijing:SciencePress,2009.[10]KJChae,AmJang,SKYim,eta.lTheeffectsofdiges-tiontemperatureandtemperatureshockonthebiogasyieldsfromthemesophilicanaerobicdigestionofswinemanure[J].BioresourceTechnology,2008.[11],,.[J].,2008,29(4):79-83.ExperimentontheMethaneProductionCapacityandEnergyOutputofDifferentTemperaturesduringAnaerobicDigestionofSwineManureWeiRongronga,ChengGuanwena,LuoJiejuna,LiangLinga,ZhuZongqiangb,XuShana,WeiWenyuana(GuilinUniversityofTechnology,a.DepartmentofResourcesandEnvironmentalEngineering;b.TheGuangxiKeyLa-boratoryofEnvironmentalEngineering,ProtectionandAssessment,Guilin541004,China)Abstract:Thisstudywascarriedoutbyexperimentingwiththeself-manufactureddigestiondeviceswhichwerefedwithswinemanureasmaterialwithadomesticatedinoculumaddedasyeast.Theexperimentwasontheconditionof6.6%massfractionoftotalsolid,thedigestiontemperaturesweresetatroomtemperature,20,35,and55e,andthebiogasyieldofthefourtemperatureswererecordedin41days.Throughthetestingofme