SBR工艺处理垃圾渗滤液研究及应用现状

。。1、、、11。[1]771、5“”5。2、。COD1200～54412mg·L-1。3NH3-N。NH3-N1000～3000mg·L-1NH3-N。4。Fe、Zn、Cd、Cr、Hg、Mn、Pb、Ni。2、。1。。SBR100022。,SBR。SBR,,SBR。SBRX703.1A1000-3700(2009)02-019-062008-05-13“”—[e-mail]。COD/mg·L-1BOD5/BOD/mg·L-1NH3-N/NH4+-N/mg·L-1Pb/mg·L-1Cr/mg·L-11200～54412200～1900020～74000.069～1.530.01～2.61pHTP/mg·L-1TOC/mg·L-1SS/mg·L-1Hg/mg·L-15.5～8.50.6～71.91500～20000200～10000～0.032/mg·L-1/mg·L-1As/mg·L-1～2356～357033000～100000.1～0.51Table1Charactersoftypicallandfillleachate35220092TECHNOLOGYOFWATERTREATMENTVol.35No.2Feb.,200919。2。、、、、、AOPs、、Fenton、。。、。3。、。。。、、、、。。、。UASB、ABR、ASBR、、。、。。。、。SBR。3SBRSBRSBR。3.1SBR[2]SBR,COD500mg·L-1BOD5/COD0.14COD5.0kgCOD·mg-1·d-195%。[3]SBRCOD、BOD、NH3-N、TN86.1%、97.4%、94.5%81.3%COD、NH3-N、TN89.8%、97.6%、89.1%。3.1.1SBRASBR。Harmandali。pHHRTCOD64%～85%COD83%0.12VSS/gCOD。2.8kgTOC·mg-1·d-1TOC73.9%ASBR[4]。3.1.2SBR-SBRASBRSBR。[6]ASBR-SBRNH4+-NNH4+-N83.5%80.9%。NH4+-NSBR。ASBRCOD58.9%BOD566.0%SBRCOD67.9%BOD589.05%。3.2SBRSBRSBR+SBR。3.2.1、-SBR→pH→→SBR→→。90%。35220COD。[6]-SBR-COD、NH3-N91%、81%95%。AhmetUygurFikretKarg[7]--SBR-An/Ax/Ox/Ax/Ox21hCOD86%93%。3.2.2-SBR→→SBR→→。、。。[8]FBZBOD5、COD、82.1%、68.9%、53.8%。EvelyneGonze[9],63GJ·m-2BOD5/COD0.014COD70%。EwaNeczaj10]12μm5%～15%70%COD90%。3.2.3-SBR→→→SBR1→SBR2→PAFCSSBR2。。[11]COD1500～4500mg·L-1NH4+-N795～1550mg·L-1pH8.0～9.0SBR+COD300mg·L-1、20mg·L-1、20。[12]PAFCSSS84%92%SBRCOD、BOD88%、94%89%。3.2.4-SBR、。[13]SBRCOD90%、NH3-N99%、TN95%、99%0.001mg·L-1。3.2.5Fenton-SBR→→→SBR→。Fenton·OH、。[14]-SBR。COD85%99%。[15]-Fenton-SBRCOD、BOD80%、94%。4SBR4.1-SBR-→→→SBR→CaOpH→→SBRCaOpH。、。NH3-N。SBR。[16]-SBR-COD148.4mg·L-1、NH3-N12.2mg·L-1COD91.2%NH3-N90.4%。4.2-UBF-A-SBR→→→21→SBR→。、。、。[17]→UBF→A-SBRCOD、BOD5、NH3-NTN95%、99%、99.5%97%。COD10～15g·L-1、BOD53～5g·L-1。4.3-UASB--SBR→→UASB→→SBR→→。CODUASBUASBCOD。[18]UASB++SBRSBRBOD5SBRBOD5/COD。SBRCOD78.2%COD99.1%96.6%。[19]+UASB+SBRCOD5000～6000mg·L-1、NH3-N600～1400mg·L-1COD80%NH3-N95%。4.4UASBF-SBR→→UASBF→→SBR→→。UASBF。。COD1～1.5×104mg·L-1NH3-N800～1500mg·L-1SS2000～4000mg·L-1。COD94%～98%NH3-N＞99%[20]。5SBRSBR2SBRGB1688921997。6SBR6.1SBRNO3-。、pH、FA、、。FANO2--NDO2SBRTable2ExampleofSBRcombinationprocesstotreatlandfillleachate-SBR-150～200m3·d-1COD2000～2500mg·L-1800～1000mg·L-1+++SBRSBR100m324h。AlCl3COD2984mg·L-1NH3-N363.2mg·L-1COD242mg·L-1NH3-N21.2mg·L-1++SBR+COD0.5kg·m-3·d-130%～40%MLSS4000mg·L-1COD2～10mg·L-199%-UBF-SBRCOD600～5000mg·L-180～400mg·L-1SS30～280mg·L-1pH6.2～6.5COD78%NH3-N89%SS79%CANON600m3·d-11mg·L-1800mg·L-10.46kgNH+4·m-3·d-195%90%UASBF-SBRCOD(1～1.5)×104mg·L-1NH3-N800～1500mgSS2000～4000mg·L-1COD:94%～98%NH3-N99%+SBR+COD1780.3mg·L-1NH4+-N127.1mg·L-1BOD5713.5mg·L-1COD63.0%35222。ALR、pH、、NO2--N。FAFA。6.2SND、COD/NH4+-N。SNDNO2-、。SBR[21]。6.3NH3NO2-NO3-NH3-NNOx--NN2。。SBR。Dongene[22]SHARON-Anammox1000～1500mg·L-1SBR80%NH4+-N。Siegrist[23]SBR70%。6.4CANONCANONANAMMOX。CANON。CANON50%50%。CANON62.5%。1mg·L-1800mg·L-10.46kgNH+4-N·m-3·dSBRCANON95%90%。7。。。、。。SBR。[1].[J].1996,18(4):41-43.[2],,,.SBR[J].,2005,6(2):30-35.[3],,,.SBR[J].:,2006,21(4):120-125.[4],.-、、[M].:,2004:359-360.[5],,.CANON[J].2004,30(8):24-29.[6],,,.-SBR-[J].,2000,22(3)21-29.[7]AhmetUygur,FikretKarg.Biologicalnutrientremovalfrompre-treatedlandfillleachateinasequencingbatchreactor[J].JournalofEnvironmentalManagement,2004,71:9-14.[8],,.+SBR[J].,2002,15(3):16-17.[9]EvelyneGonze,NadineCommenges,YvesGonthier,etal.Highfrequencyultrasoundasapre-orapost-oxidationforpapermillwastewatersandlandfillleachatetreatment[J].ChemicalEngineeringJournal,2003,92(1-3):215-225.[10]EwaNeczaj,EwaOkoniewska,MalgorzataKacprzak.Treatmentoflandfillleachatebysequencingbatchreacto[J].Desalination,185(2005)357-362.[11],,.SBR-PAC23[32],.-SMBR[J].,2005,31(23):9-12.[33],,,.[J].,2004,30(7):46-49.[34],,,.[J].,2005,28(5):66-68.[35],,,.[J].,2005,24(5):87-89.[36],.[J].,2001,27(4):41-44.PRESENTSTATUSOFPROCESSINGCONDITIONSOFMEMBRANEBIOREACTORINDYEINGWASTEWATERTREATMENTDAIXing-guo1,WULi-guang2,ZHANGLin1,CHENHuan-lin1,GAOCong-jie1,3（1.CollegeofMaterialsScience&ChemicalEngineering,ZhejiangUniversity,Hangzhou310027,China;2.CollegeofEnvironmentalScienceandEngineering,ZhejiangGongshangUniversity,Hangzhou310035,China;3.TheDevelopmentCenterofWaterTreatmentTechnology,Hangzhou310012,China）Abstract:Membranebioreactor(MBR)isanewtechnologyofwastewatertreatmentwhichhasbeendevelopedinrecentyears.Itisefficientindyeingwastewatertreatment.TheapplicationofMBRindyeingwastewatertreatmentwasreviewedinthispaper.Theprocessingconditionsofmembranebioreactorindyeingwastewatertreatmentandtheirinfluencesonthequalityofeffusionandmembranefoulingweresummarizedanddiscussed.Final-ly,thefuturedevelopmentofMBRfordyeingwastewatertreatmentwasalsoprospected.Keywords:membranebioreactor;dyeingwastewater;processingconditions;membranefouling[J].:,2002,28(4):435-439.[12],,,.-SBR[J].,2006,22(5):92-98.[13].SBR[J].:,19(3):217-224.[14],HuangCP.Fenton[J].,2001,17:1-3.[15],.-Fenton-SBR[J].,2002,16(4):19-20.[16],./SBR/[J].,2004,30,(3):176-178.[17],,.[J].,2007,33(1):23-26.[18],,.[J].,2007,28(1)70-73.[19],,.SBR[J].2006(11)90-91.[20],,.UASBF-SBR[J].20