处理难生物降解有机物的厌氧颗粒污泥形成的技术进展刘雅巍

整理文档很辛苦,赏杯茶钱您下走!

免费阅读已结束,点击下载阅读编辑剩下 ...

阅读已结束,您可以下载文档离线阅读编辑

资源描述

          10 4 200412JournalofTianjinInstituteofUrbanConstruction Vol.10 No.4 Dec.2004刘雅巍,张春青,池勇志(,300384)        :为了加快以上流式厌氧污泥床(UpflowAnaerobicSludgeBlanket,简称UASB)为代表的无载体厌氧反应器处理含难生物降解有机物废水的启动速度,综述了影响厌氧颗粒污泥形成的因素.此外,为了高效、快速地降解废水中的难生物降解有机物,建议向厌氧反应器中投加优势菌,以进一步提高厌氧反应器降解废水中难生物降解有机物的效率和速度.  :;;;:X172   :A   :1006-6853(2004)04-0263-03  ,、,,.,,(UASB)、(EGSB)(IC).  UASB,:①,2~3,1[1];②,.,、.,.1 1.1   ,C∶N∶P200∶5∶1,.、、,[2].1.2   (COD),0.3kgCOD/(kgVSS·d),(),.0.6kgCOD/(kgVSS·d),,,COD0.6kgCOD/(kgVSS·d),[2].1.3   UASB,,,(SelectionPressure).().,,.:2004-09-15   :(20031003)   :(1980-),,,.,,,.,,.Ritta2.5~3.0m/d,UASB[3].1.4   :;.pH(pH),.,,SMA(SpecificMethanogenicActivity,);,SMA.,(pH8.2,),;,SMA[4].1.5   ,,1/4~1/3,[5].1.6   (20℃)、(35℃)、(55℃).,,,.,pH(6.8~7.6)[5].2   UASB,.“”,,,,、.、,、.  、、、,.———,,.3 3.1   ,、,、[6].  [6],32d,COD470.3mg/L255.5mg/L,COD83.691.1,BOD5.3.2   ———,[5].3.2.1 投加无机絮凝剂或高聚物  [7]UASB,,7d、4.  TsuyoshiImai[8],(waterabsorbingpolymer)(VFA)UASB,:750mg/L,70d,,.  YuH.Q.[9]UASB,(Al3+300mg/L),UASB1,UASB10.  RandallA.Wirtz[10](ASBR),,ASBR75.  S.Uyanik[11]·264·  2004 10 4 (KymeneSLK-2)(ABR).,ABRABR,3,.3.2.2 投加细微颗粒物  [12]UASB,3~61.3.2.3 投加金属离子  YuH.Q.[13][14]UASB,:(ECP),,,.4    (1),、、、、pH,.  (2)、,.  (3),、,、.  (4).:[1] ,UASB[J],2000,18(2):17-20.[2] ,,,.[M]:,2003.[3] RITTAHK,JUKKAAR.Performanceofanon-siteUASBreactortreatingleachateatlowtemperature[J].WaterResearch,1998,32(3):537-546.[4]  ,,.UASB[J].,2002,18(8):13-15.[5] LIUY,XUHL,YANGSF,etal.Mechanismsandmodelsforanaerobicgranulationinupflowanaerobicsludgeblanketreactor[J].WaterResearch,2003,37:661-673.[6] ,,,.[J].,2003,30(3):56-59.[7] ,UASB[J],1996,(3):12-14.[8] ZMAIT,UKITAM,LIUJ,etal.AdvancedstartupofUASBreactorsbyaddingofwaterabsorbingpolymer[J].Wat.Sci.Tech.,1997,36(6~7):399-407.[9] YUHQ,FANGHHP,TAYJH,etal.Enhancedsludgegranulationinupflowanaerobicsludgeblanket(UASB)reactorsbyaluminumchloride[J].Chemosphere,2001,44:31-36.[10] WIRTZRA,DAGUERR.Laboratorystudiesonenhancementofgranulationintheanaerobicsequencingbatchreactor[J].Wat.Sci.Tech.,1997,36(4):279-286.[11] UYANIKS,SALLISPJ,ANDERSONGK.Theeffectofpolymeradditionongranulationinananaerobicbaffledreactor(ABR)[J].WaterResearch,2002,36:933-943.[12]  .UASB[J].,1996,12(5):16-19.[13] YUHQ,TAYJH,FANGHHP.RolesofcalciuminsludgegranulationduringUASBreactorstart-up[J].Wat.Res.,2001,35(4):1052-1061.[14] ,,.UASB[J].,2002,18(6):26-28.(下转第291页)·265·   :FEAforclampfittingsofGuangzhousubwaysBIJi-hong,LIUGang,LIULi-na,LIUFeng-tao(SchoolofConstructionEngineering,TianjinUniversity,Tianjin300072,China)Abstract:AccordingtotheprincipleofFEA,severalkindsofoverheadlineclampfittingsunderdifferentloadinelectrificationrailwayareanalyzedbyusingofANSYSprogram,andmaterialnonlinearandstatenonlinearareconsidered.Fromthecalculatingresult,someusefulconclusionsareconcluded,andreasonalizedsuggestionsareproposedintheperiodsofdesign,constructionandapplication.Keywords:finiteelementanalysis(FEA);ANSYS;materialnonlinear;statenonlinear(上接第265页)TechnologyadvanceonanaerobicgranularsludgeculturetotreatrefractorybiodegradableorganiccontaminantLIUYa-wei,ZHANGChun-qing,CHIYong-zhi(DepartmentofMunicipalandEnvironmentalEngineering,TIUC,Tianjin,300384,China)Abstract:Toquickenthestart-upspeedoftheanaerobicreactorwithoutcarrier,suchasUASB(upflowanaerobicsludgeblanket),whichwasusedtotreattherefractorybiodegradablewastewater,factorstoaffectthegranularsludgeculturewerereviewed.Furthermore,totreattherefractorybiodegradablewastewatermoreeffectivelyandquickly,theoptimalbacteriaisadvicedtobeusedintheUASBreactor,sotheanaerobicreactorcouldtreatrefractorybiodegradableorganiccontaminantintherefractorybiodegradablewastewatermoreefficientlyandrapidly.Keywords:anaerobicreactor;granularsludge;effectfactor;predominantbacteria·291·   :

1 / 4
下载文档,编辑使用

©2015-2020 m.777doc.com 三七文档.

备案号:鲁ICP备2024069028号-1 客服联系 QQ:2149211541

×
保存成功