USRUASB好氧工艺处理酒糟废液及沼气高值利用刘建广

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檲檲檲檲檲檲檲檲檲檲檲檲檲檲檲檲檲檲檲檲檲檲殘殘殘殘USR/UASB/12331.2501012.2501013.250101USRUSR55℃3000mg/L4kgCOD/m3·d500mg/LpH6.7~7.61.8m3/m3。USR/UASB/COD>99%。98%、<20mg/m3。X703.1C1000-4602201114-0069-03TreatmentofAlcoholWastewaterbyUSR/UASB/AerobicProcessandHighValueUseofBiogasLIUJian-guang1ZHANGChun-yang2ZHANGGuang-lan3GANHai-nan31.SchoolofMunicipalandEnvironmentalEngineeringShandongJianzhuUniversityJinan250101China2.SchoolofThermalEnergyEngineeringShandongJianzhuUniversityJinan250101China3.ShandongSifonEnvironmentalProtectionandBio-energyCo.Ltd.Jinan250101ChinaAbstractThethermophilicfermentativeprocessinupflowanaerobicsolidreactorUSRwasusedfortreatinghigh-concentrationalcoholwastewaterandthebiogasproducedwaspurified.Whenthedi-gestiontemperatureis55℃thealkalinityofmixedliquoris3000mg/Landtheorganicloadis4kg-COD/m3·dtheeffluentVFAisbelow500mg/LpHis6.7to7.6andthespecificvolumebiogasproductionis1.8m3/m3.TheremovalrateofCODbyUSR/UASB/aerobicprocessis99%andtheef-fluentqualitymeetsthedischargerequirement.Afterpurificationtreatmentthemethanecontentinbio-gasis98%andthehydrogensulfidecontentisbelow20mg/m3.Thehighvalueuseofbiogasisachieved.KeywordsalcoholwastewaterupflowanaerobicsolidreactorUSRaerobicprocessbiogas2008BADC4B092600m3。、·96·271420117CHINAWATER&WASTEWATERVol.27No.14Jul.2011、、、、。/UASB/。、。1>90%。80~90℃pH3~5COD50000mg/L60%~80%BOD5/COD0.4~0.6。50%。、1。1、Tab.1DesigninfluentandeffluentqualitypHCOD/mg·L-1BOD5/mg·L-1SS/mg·L-14~55000025000250006~9≤300≤100≤15022.1、1USRCODUASB1。1Fig.1Flowchartofalcoholwastewatertreatmentprocess2。2Fig.2Flowchartofbiogaspurification2.2①。60℃。②USR。53℃。822m×18m36000m3。15gVSS/L0.5kgCOD/m3·d1.5kgCOD/m3·d。pH4~5pHpH0.15kgCaO/m33000mg/L500mg/LpH6.9~7.6。1.5kgCOD/m3·d100.5kg-COD/m3·dUSR13.5d4kgCOD/m3·d25m3/m31.8m3/m3。。·07·2714.watergasheat.com。。。③USRUASB。。④UASB126m×7mUASB3700m335℃。⑤30m×39m×5m。4~6mg/L。⑥124m5m0.5m3/m2·h。⑦2CO290%。a.24.2m350℃0.4MPaFe2O3。b.50.5MPa7.4m3。。33.1①CODCOD45000~60000mg/LUSRCOD3000~8000mg/LUASBCOD800~1200mg/LCOD300~400mg/LCOD<300mg/L。COD99%。②<20mg/m3>98%15000m3。3.2①CODCOD4.67×104t。②60000m355%。15000m398%4/m36。4①。USRCOD90%。②USR/UASB/COD。③<20mg/m3>98%。1.“+UASB+”J.200518421-23.2.CO2J.200827351-52.13953118255E-mailliujgljg@163.com2011-01-30·17·.watergasheat.comUSR/UASB/2714

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