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浙江科技学院学报,第19卷第2期,2007年6月JournalofZhejiangUniversityofScienceandTechnologyVol.19No.2,June2007:2007-04-16:(50478083):(1977— ),,,,,。UASB方程冉1,2,吴征宇3,龙於洋2,李 岚1,沈东升2(1.,310023;2.,310029;3.,200042) :,(UASB)。,,UASB,UASB。:,,95d,。COD5250mg/L,COD85%,COD8.4kg/(m3·d),5.0m3/(m3·d),。:UASB;;;:X705 :A :1671-8798(2007)02-0125-04Start-upMethodofUASBforLandfillLeachateTreatmentFANGCheng-ran1,2,WUZheng-yu3,LONGYu-yang2,LILan1,SHENDong-sheng2(1.SchoolofArchitectureandCivilEngineering,ZhejiangUniversityofScienceandTechnology,Hangzhou310023,China;2.DepartmentofEnvironmentandResource,ZhejiangUniversity,Hangzhou310029,China;3.ShanghaiJinganEnvironmentalMonitoringStation,Shanghai200042,China)Abstract:Landfillleachate,akindofhighorganicwastewater,hasbeenprovedtobetreatedbyUASBeffectively.Researchontherapidstart-upofUASBisstudiedusingthedifferentconcen-trationoflandfillleachateasinfluent.Itshowsthatthestart-upcanbecompletedin95daysbyincreasingtheloadingofthereactorstepbystepwithcommonanaerobicsludgeastheseedsludge.Meantime,theinfluentCODconcentrationis5250mg/L,theCODremovalrateis85%,theorganicloadingCODis8.4kg/(m3·d),thenetgasyieldis5.0m3/(m3·d)andsomegranularsludgeisformedatthebottomofUASB.Keywords:UASB;bioreactorstart-up;landfillleachate;wastewatertreatment 、,,。,,[1]。,77,(COD)(BOD)[2]。,。(UASB)BODCOD,[1,3,4]。,,UASB,、、UASB,,UASB。1 1.1 ,。,COD5250mg/L。1。1 /(g·L-1)KH2PO47.3NaHCO333NH4Cl0.3K2HPO4·3H2O2.527.5 UASB,14L,:150×1000,10cm,5cm,85cm,。1。1 UASB1.2 UASB,(30±1)℃,,,(2)。(COD3000mg/L)。UASB,8L((60%V),VSS10.3g/L;7L,COD5000mg/L,HRT48h;COD2.5kg/(m3·d);:1.11cm/h。2 COD/dCOD/(mg·L-1)/%/%/(L·d-1)1~55000100(5000mg/L)07.06~10260087.5(2600mg/L)12.5(2625mg/L)11.211~15290075(3000mg/L)25(2625mg/L)14.016~36290065(3050mg/L)35(2625mg/L)14.037~50352065(2590mg/L)35(5250mg/L)14.051~71426640(2790mg/L)60(5250mg/L)18.772~81525015(5250mg/L)85(5250mg/L)18.782~9552500100(5250mg/L)22.41.3 COD:;pH:pHS-3;:;:GC-9160-HD。2 UASB,COD。COD80%,(VLR)。UASB,:;,;,2。UASBCOD2.5kg/(m3·d),COD80%,[5]。12619,UASB,COD5000mg/L。COD80%,3~5d。2.1 UASBCODUASB、CODCOD2。2 UASBCOD,UASBCOD,5,COD5000mg/L,HRT48h,COD95%。6,,UASB,COD2600mg/L,COD,,80%COD。,COD,。1116,COD,COD,80%。37,35%,COD3520mg/L,COD66.6%,10d,。5172COD,,COD80%。82,,3~4d,UASB,,COD5250mg/L,COD85%。2.2 UASBHRTVLRUASBHRTVLR3。3 UASBHRTVLRCOD,COD80%。HRT,HRT48h,6、11、51、8230、24、18、15h。COD,62.1kg/(m3·d)UASB8.4kg/(m3·d)。2.3 UASBpH4,,pH,6.9~7.0,pH,,pH7.0~7.5。,。,,[6]。4 UASBpH2.4 UASB5,,。COD2.1~2.5kg/(m3·d),1.2~1.5m3/(m3·d)。COD2.9~5.7kg/(m3·d),2.0~3.2m3/(m3·d)。5.0m3/(m3·d)。,CH4CO2CH450%~55%,CO242%~48%。1272,:UASB5 UASB2.5 UASB,[6]。,(COD5250mg/L),COD80%。,,1mm,,。,UASBCOD,,。3 、、UASB,UASB,UASB。1)UASB,95COD5250mg/L,COD85%;COD8.4kg/(m3·d)。2)UASBpH,,pH7.0~7.5。5.0m3/(m3·d)。CH450%~55%。3),,,。。:[1] .[M].:,2003.[2] ,.———[J].,2006,40(6):769-773.[3] ,,.[J].:,2004,30(3):252-258.[4] ,.UASB[J].,2006,28(1):85-88.[5] ,,,.UASB--[J].,2003,16(S1):32-34.[6] ,,,.UASB[J].,2005,28(2):22-23,113.12819
本文标题:UASB反应器处理垃圾渗滤液的启动研究方程冉
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