510006ABRHABRHRT、HABR。HABRHRT11~12h0.3HABRCOD、47%56%。EXPERIMENTSTUDYONTHETREATMENTOFPRINTINGANDDYEINGWASTEWATERBYHYBRIDANAEROBICBAFFLEDREACTORHuangRuiminLiuXinHuangChunmeiZhouHaibinCollegeofEnvironmentalScienceandEngineeringSouthChinaUniversityofTechnologyGuangzhou510640ChinaAbstractInthisworktheprintinganddyeingwastewaterwastreatedbyapilot-scaleHABRwhichwasmodifiedfromgeneralABRbyaddingcombinedpackingintheupperpartofeachcompartmentandaddinginertcarrieratthebottomofthereactor.Thestart-upcharacteristicsofthereactortheeffectofHRTandsludgereturnratioonthetreatmentofprintinganddyeingwastewaterbyHABRandtherunningcharacteristicsofeachcompartmentwereresearched.TheresultsshowthattheHABRhasahigherefficiencyintreatingprintinganddyeingwastewaterwithhigherCODandcolorremovalrate.whilethehydraulicretentiontimeHRTweretakenfor12~13hoursandthesludgereturnratiowas0.3theaverageCODandcolorremovalratestendstoreach47%and56%respectivelyandtheanaerobicbacteriaineachcompartmentdevelopedgoodbasedontheiravailablesubstratesandspecificenvironmentalconditions.Keywordsanaerobicbaffledreactorprintinganddyeingwastewatercombinedpackinginertcarrier0、、。ABRStanfordMcCarty12080、、SMPA2。HABR。11.1、1。1pHρCOD/mg·L-1ρBOD5/mg·L-1ρSS/mg·L-1/ρS2-/mg·L-18.5~9.5500~600150~180200~300600~80020~3011201012286DOI:10.13205/j.hjgc.2010.06.0131.2ABR。ABRPVCPE4000mm×500mm×3300mm6000L51~513∶1。45°。1∶1∶0.87∶0.87∶0.62。3。1。11.3CODpHpHB-3pHSSVSSDOJPB-6073。1.41.4.1ABRABR、14-56。ABRABRCOD。7ABR。ABR1。1/30.5~1mm。。HABR。1.4.2HABRHRT、。ABR。28~35℃。22.1HABR1/2VSS18g/LVSS/TSS0.56。。600mg/LmCOD∶mN∶mP=200∶5∶1。5d。1h。ABR。10d8-9HABRABR。∶400L/h120150180240300400L/h50h15h。CODCOD2。212010122862COD2HABRABRCOD40dHABRCOD75dHRT25hHABRCOD48%HRTHRTCOD75d。HABR0.5~3mm1、22~3mm。ABR60dCOD30%。2.2HRTHRTABR。HRTHABRABR7d3。HABRABRCOD12hHABRCOD45%ABRCOD28%。HABRHRT12h50%。。。3HRTABRHABRHABRCODCOD。HABRHRT11~12h。HABRABRABR。2.3HABRHABRHABR31201012286。12hHABRCOD4。4HABR4HABR0.3COD。2.4HABR。HRTHABRpHCOD、HABR5。5HRTpH5pH10pH。HRT12hpH。HRT=6hpH。COD6。COD。HRTHABRHABR。6HRTCOD31。2HABRCOD11~12hCOD45%4120101228655%HABRHRT11~12h。3HABR。HRT12h0.3COD47%56%。4HABR。1BachmanNABeardVLMcCartyPL.PerformancecharacteristicsoftheanaerobicbaffledreactorJ.WatRes198519199-106.2LettingaG.AdvancedanaerobicwastewatertreatmentinthenearfutureJ.WaterSciandTechnol199435105-12.3.M..2002.4.J.199915718-20.5.J.20052592297-2303.6BarberWPStuckevDC.TheuseoftheanaerobicbaffledreactorABRforwastewatertreatmentareviewJ.WatRes19993371559-1578.7WilliamPBStuckeyPC.NitrogenremovalinamodifiedanaerobicbaffledreactorABRdenitrificationJ.WaterRes20003492413-2422.8BarberWPStuckeyDC.Start-upstrategiesforanaerobicbaffledreactorstreatingasyntheticsucrosefeedC∥Procofthe8thInternationalConferenceonAnaerobicDigestion.SendaiJapan199732-39.9.ABRJ.200833596-99.10.ABRJ.200627102024-2027.510730111213E-mailliulin750@163.com2009-11-20櫅櫅櫅櫅櫅櫅櫅櫅櫅櫅櫅櫅櫅櫅櫅櫅櫅櫅櫅櫅櫅櫅櫅櫅櫅櫅櫅櫅櫅櫅櫅櫅櫅櫅櫅櫅櫅櫅櫅櫅櫅櫅櫅櫅櫅櫅櫅櫅櫅櫅3。DO1.5~2mg/L、DO3.5mg/L。SS。30d、。2。1.D.2003.2.、D.2009.3.J.200427639-41.4.-J.20063446-48.5.-J.20023662-64.6.—D.200615-18.7.J.2005311167-70.8.-J.20052329-11.9.--J.200430753-55.10.J.20092718-10.130026E-mailhuangjg@jlu.edu.cn2010-03-2951201012286