淀粉废水处理方法研究进展张连凯

21320086POLLUTIONCONTROLTECHNOLOGYVol.21,No.3Jun.,20081,　1,　2,　　1,　1(1.中国环境管理干部学院,河北秦皇岛　066004;　2.青岛银河环保股份有限公司,山东青岛　266071)　:,、、、,。:;;:X703.1　　　:AResearchProgressonStarchWastewaterTreatmentProcessesZHANGLian-kai1,　ZHANGRen-zhi1,　SONGShu-rui2,　YANGHui1,　ZHANGYi-ting1(1.EnvironmentalManagementCollegeofChina,Qinhuangdao,Hebei066004,China;2.QingdaoGalaxyEnvironmentalProtectionInc.Qingdao,Shandong266071,China)Abstract:Inthisacticle,severaltreatmenttechnologiesofstarchwastewaterweresummaried.Itincluedanerobicprocess,aer-obicprocess,biologicalpond,chemicalflocculationandphotosyntheticbacteriaprocess.Advantagesanddisadvantagesofthoseprocesseswerealsoanalysed.Keywords:starchwastewater;highconcentratedorganicwastewater;treatmentprocess:2008-02-28;:2008-03-25:(1981—),,,,。　　,、、、、。,CODcr5000～50000mg/L,BOD53000～30000mg/L,SS1000～5000mg/L。,,。,、、。1　,,,。,、、、。[1](UpflowAnero-bicSludgeBlanket,UASB),,,UASBCOD14.190g/L,COD90%,6.81g/(L·d),3.20L/(L·d)。[2]UASB,,COD10kg/(m3·d),COD90%。[3]UASB,,COD4000～8000mg/L,COD4～5kg/(m3·d),90%。[4]UASB-SBR,,,,,COD100mg/L。、、、[5]UASB、、,COD7～12kg/(m3·d),COD90%。[6](AnaerobicBaffledReactor,ABR),。(35±0.5)℃,CODcr12～·62　　　·.21338kg/(m3·d)、HRT12～24h,CODcr72%～96%。[7],,(VerticalBaffledAnaerobicSludgeBed,VBASB),--,。(AnaerobicSequencingBatchReactor,ASBR),Dague[8]SBR。ASBR,、、。[9],ASBR(CODcr6～8g/L),,。24h,35℃,CODcr0.6～1g/L,ASBR,。(ExpandGranuleSludgeBed,EGSB),,UASB,2.5～6.0m/h,UASB0.5～2.5m/h[10]。,EGSB,“”,,,,[11]。[12](ExpandGranuleSludgeBed,EGSB),,EGSB,CODcr3500～6500mg/L,EGSB85%。,,,,,,。。、pH、,、,。2　,、、,。,,,,[13]。Jin[14],45L,3.5L,10%,35℃、pH4.014h,95%,COD95%,2.07～2.39g/L。,,。、[15]SBR,:SBR。1.0g/L、CODcr1115mg/L,SBR;,6.0g/L、CODcr6690mg/L,97.3%,CODcr94%,,。CODcr,CODcr。[16]SBR,COD3.5～4.0g/L,8～12h,COD94%～96.7%,COD150mg/L,。、、。SBR,SBR,,,。[17],-,,,,,,。,,,,,,,,,、,。3　,。2050,20086.·63　　　·。,,、、[18-20]。[21],--。,,1～2d,,7d,,7d,,,、,,,。,、,,、。[20]、[22],-,,COD90%。,,,,,。、,。4　,(),,,,[23]。,,。[24],(1%)0.2mL/L,90min,CODcr96.2%。[25]-N--D-(),pH3.5,CaO、0.1%、0.3%、0.6%KMnO4,,,,CODcr68%。[26],FNF(、),,,,BOD573.9%,CODcrSS80%。、[27],(MBF),,1L10%CaCl25mL,MBF20mL,pH9,600、400、140、7030r/min20s、20s、20s、2min3min,,96.4%。,、、、、,,,,。,,。5　70,(PhotosyntheticBacteria,PSB)。,,,,,,。,、。,、[28,29]。[30],、、、,,,207,,72h,CODcr99.5%。[31],L2,,,CODcr95.7%,。,、、,、,。,,,,,。·64　　　·.2136　　,,。,,。,。,,,,,。[][1]　　,.UASB[J].,2002,23(6):774-777.[2]　,,　.UASB[J].,2002,22(1):28-31.[3]　　,,.UASB[J].,1996,9(4):10-12.[4]　,.UASB-SBR[J].,2002,23(4):21-24.[5]　AnnMarieEilersen,MogensHenze,LeneKloft.EffectofVola-tileFattyAcidsandTrimethylamineonDenitrificationinActiva-tedSludge[J].WatRes,1999,5:1259-1266.[6]　,.[J].,2002,21(3):139-142.[7]　,,.[J].,1997,22(3):33-35.[8]　IoannisShizas,DavidMBagley.ImprovingAnaerobicSequen-cingBatchReactorPerformancebyModifyingOperationalPa-rameters[J].WatRes,2002,36(1):363-367.[9]　,.[J].,2002,25(2):100-103.[10]　WuWei-Min,MahendraKJain.EffectofStorageonthePer-formanceofMethanogenicGranules[J].WatRes,1995,29(6):1445-1452.[11]　,,　,.[J].,2004,6(1):31-33.[12]　,　.EGSB[J].,2005,23(1):17-19.[13]　.[M].:,2003.[14]　JinB,VanLHJ,PatelB,etal.ProductionofFungalProteinandGlucoamalasebyRhizopusOligosporusfromStarchProcess-ing[J].WastewaterProcessBiochemistry,1999,34:59-65.[15]　,.SBR[J].(),2004,43(3):376.[16]　　,,.SBR[J].,2000,17(1):19-23.[17]　,　,.[J].,2000,24(2):55-56.[18]　Belingua,Seyfieldcf.AnaerobixAerobicTreatmentofPotato-Starchwastewater[J].WaterScienceandTechnology,1993,28(2):165-176.[19]　　.[J].,1999,36(4):26-27.[20]　.[J].,1993,3:38-39.[21]　,.[J].,1996,22(2):24-26.[22]　　.[J].,1994,13(4):70-71.[23]　,,　.[J].(),2002,23(2):230.[24]　,.[J].,1996,18(2):28-30.[25]　,.[J].,1990,12(3):22-23.[26]　,,.[J].,1991,9(6):415-418.[27]　　,,,.[J].,2004,17(2):47-50.[28]　,,.[J].,2005,23(1):29-35.[29]　NahjimaF,KamikoN,YamamotoK.OrganicWastewaterTreatmentWithoutGreenhouseGasEmissionbyPhotosyntheticBacteria[J].WarSciTech,1997,35(8):258-291.[30]　　,,　.3[J].,1994,24(3):235-240.[31]　,,.[J].,1995,16(3):39-40.·动态与简讯·,GPRS,,,,,40,、,,、、,,,,,。