PDMDAACMBBR组合工艺处理印染废水邓书平

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PDMDAAC-MBBR邓书平,牟淑杰(辽宁石油化工大学职业技术学院,辽宁抚顺113001) :(PDMDAAC)-(MBBR),、(HRT)、PDMDAAC、CODNH3-N。,60%(),24h,PDMDAAC0.8g/L,、CODNH3-N97%、92%90%。CODCrNH3-N50mg/L15mg/L,GB4287—1992《》。:染整;废水处理;絮凝剂;生物膜反应器:TS199   :B   :1000-4017(2009)06-0036-03CombinedprocessofPDMDAACandMBBRforwastewatertreatmentDENGShu-ping,MOUShu-jie(VocationalandTechnicalCollege,LiaoningUniversityofPetroleumChemicalTechnology,Fushun113001,China)Abstract:Thecombinedprocessofpolydimethyldiallylammoniumchloride(PDMDAAC)andmovingbedbiofilmreactor(MB-BR)wasappliedtothetreatmentofdyeingeffluents,theinfluencesoffillingproportionofcarrier,hydraulicretentiontime(HRT),thedosageofPDMDAAC,CODvalueandNH3-Nconcentrationoffeedingwateronthetreatmentefficiencywerein-vestigated.Theresultsshowedthatundertheconditionsoffillingproportionofcarrier60%(volumeratio),HRTinsinglereac-tor24h,thedosageofPDMDAAC0.8g/L,MBBRcouldoperatedverysteadilyandgoodefficiencycouldbeachievedwiththeremovalofcolor,CODandNH3-Nat97%,92%and90%respectively.Thedischargedwatercouldmeetthefirstclasscriteriaspecifiedindischargedstandardofwaterpollutantsfordyeingandfinishingoftextlleindustry(GB4287—1992)withCODandNH3-Nlessthan50mg/Land15mg/Lrespectively.Keywords:dyeingandfinishing;wastewatertreatment;flocculant;biofilmreactor0 前言,COD,,。,、。[1](MBBR)。、1,,,。,(PDMDAAC)、,。,MBBRPDMDAAC,,。1 试验1.1 :2008-11-13:(1973-),,,,,、。E-mail:dengshuping981@163.com。  1。MBBR,30cm×30cm×40cm,36L。。1 MBBR1.2 [2],MBBR,。MBBR,。,。(0.92~0.97g/cm3),,200~500m2/m3。,、,,、。1.3 pH、CODCr,36 (2009No.6) [3],(GB/T11903—1989)。,1。1 pHCODCr/(mg/L)BOD5/(mg/L)/(mg/L)/8~10281~59759~12587~1632371.4 ,5021mg/L。,MBBR,。,。,、,,7d,。,1~2cm,。CODCr,NH3-N,。2 结果与讨论237,CODCr462mg/L,CODCr。2.1 MBBR(HRT)24h,CODCr[4],2。2 CODCr2,,,CODCr。60%,CODCr88%86%;,。,,,。60%,,。60%,,,。,60%。2.2 HRT(HRT),HRTCODCr[5],3。3 HRTCODCr3,HRT,CODCr;HRT24h,CODCr,2%。,HRT24h。2.3 PDMDAACHRT24h,PDMDAACCODCr,4。4 PDMDAACCODCr4,PDMDAAC0.8g/L,,CODCr;,CODCr。,PDMDAAC0.8g/L。,4,MBBRPDMDAAC,88%97%,CODCr86%92%,。2.4 MBBRCODCrHRT24h,PDMDAAC0.8g/L,MBBRCODCr[6],5。5 CODCrCODCr37 PDMDAAC-MBBR组合工艺处理印染废水 (2009No.6)5,MBBR,CODCr280mg/L600mg/L,CODCr92%,97%,20,MBBR。,;,,,。2.5 MBBRNH3-N,。《》NH3-N(15mg/L)。HRT24h,PDMDAAC0.8g/L,NH3-NMBBRNH3-N,6。6 NH3-NNH3-N6,,NH3-N,NH3-N。NH3-N90%,15mg/L。3 结论(1)PDMDAAC。HRT24h,CODCr280~600mg/L,60%(),、CODCrNH3-N97%、92%90%。(2)CODCrNH3-NMBBR,20,CODCrNH3-N50mg/L15mg/L,《》(GB4287—1992)(40,CODCr100mg/L,NH3-N15mg/L)。(3)、,。,MBBR、、、,,。:[1] ,.、[J].,2003,29(4):13-15.[2]  ,,,.[J].,2003,19(2):56-57.[3] 《》.(3)[M].:,1997:102-356.[4]  ,,,.[J].,2007,32(S1):243-246.[5]  ,, .[J].,2002,20(1):19-21.[6] .[J].,2004,24(2):12-15.(△上接第28页)4,,;,。。。3 结论(1),,K/S,,。(2),,,。(3):CeO2/Pr6O11(1∶1)1.5%(owf),pH3,10mL/L,40min。:[1] ,, ,.[J].,2006,28(6):13-16.[2] ,,.[J].,1995(1):34-35.[3] ,,.[J].,2003(3):23-25.38 (2009No.6) 

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