Fenton李德生, 谭 磊, 王宝山, 徐东辉(兰州交通大学环境与市政工程学院,甘肃兰州730070) : 研究了Fenton试剂法强化铁炭微电解工艺对高浓度难生化有机废水的预处理效果。结果表明,当原水COD在9000mg/L、铁炭微电解反应时间为100min、pH值为2.2时,铁炭微电解对原水COD的去除率45%;铁炭微电解出水再投加240mg/L的H2O2(30%)进行Fenton试剂法处理,常温下反应50min对原水COD的去除率可提高到75%以上。铁炭微电解+Fenton试剂联合工艺的除污效果好、运行稳定、成本低廉,适宜对高浓度难生化有机废水的预处理。 : 废水处理; 化工废水; 高浓度难生化有机废水; 铁炭微电解; Fenton试剂:X703.1 :C :1000-4602(2006)17-0081-04StudyonPretreatmentofHighConcentrationandRefractoryOrganicWastewaterbyFerric-CarbonMicro-electrolysisandFentonReagentLIDe-sheng, TANLei, WANGBao-shan, XUDong-hui(SchoolofEnvironmentalandMunicipalEngineering,LanzhouJiaotongUniversity,Lanzhou730070,China) Abstract: Thecombinedtechniquesofferric-carbonmicro-electrolysisandFentonreagentfortreatinghighconcentrationandrefractoryorganicwastewaterwerestudied.ResultsshowthatwhentheCODininfluentis9000mg/L,thereactiontimeforthemicro-electrolysisisapproximately100minandpHis2.2,theremovalrateofCODisabove45%.WhenthedosageofH2O2(30%)is240mg/Landthereactiontimeis50minutes,theremovalrateofCODisraisedtoabove75%inrawwastewaterbyFentonreagen.tFerric-carbonmicro-electrolysisandFentonreagenttechniquesarehighlyefficientinremovalofpollutants,stableinoperationandlowincost,thusaresuitablefortreatmentofhighconcen-trationandrefractoryorganicwastewater. Keywords: wastewatertreatment; chemicalindustrialwastewater; highconcentrationandre-fractoryorganicwastewater; ferric-carbonmicro-electrolysis; Fentonreagent :(ZS021-A25-021-G); “” ,、。、、[14],。,Fenton[5]。Fenton,。81第22卷 第17期2006年9月 中国给水排水CHINAWATERWASTEWATER Vo.l22No.17Sep.20061 试验方法1.1 。,,,、、、、,。1。1 Tab.1 WastewaterqualityCOD/(mgL-1)B/CpHSS/(mgL-1)6580~113500.181.5~1028~1581.2 1。1 Fig.1 Schematicdiagramofexperimentalset-up4m,400mm,4,1、2、3、4m,。,2.5∶1,、[6]。Fenton,××=2m×0.5m×0.6m,H2O2,,,,。1.3 COD:;BOD5:;pH:;SS:;Fe2+:。2 结果与讨论2.1 2.1.1 COD9850mg/L、pH2.5,2。2 Fig.2 InfluenceofreactiontimeonCODremovalbyferriccarbonmicro-electrolysis2,100min,COD,50%。,。100min。2.1.2 pHpH[7],,COD7280mg/L、100min,pH,3。3 pHFig.3 InfluenceofpHonCODremovalbyferriccarbonmicro-electrolysis3,pH,pHCOD,pH6COD20%。pH3。pHFe2+,pHFe2+。,Fe2+pH:pH2.5Fe2+≥100mg/L,pH=6Fe2+0.1mg/L。82第17期 中国给水排水 第22卷2.2 Fenton2.2.1 Fe2+Fe2+Fenton,Fenton。80mg/LH2O2(30%),Fe2+Fenton,4。4 Fe2+FentonFig.4 InfluenceofFe2+concentrationonCODremovalbyFentonreagent4,Fe2+150mg/L,Fe2+COD,Fe2+250mg/L,COD。Fe2+H2O2,H2O2Fe2+,Fe2+,Fe2+,,,[8]。Fe2+150~250mg/L。pHFe2+,pH2.2,COD50%,Fe2+180mg/L。2.2.2 H2O2Fenton[8、9],pH2.2pH5,pH。COD5140mg/L、50min,H2O2(30%)Fenton,5。5,H2O2,COD;240mg/L,COD。Fen-tonH2O2(30%)240mg/L。5 H2O2FentonFig.5 InfluenceofdosageofH2O2onCODremovalbyFentonreagent2.2.3 COD4580mg/L、H2O2(30%)240mg/L,,6。6 FentonFig.6 InfluenceofreactiontimeonCODremovalbyFentonreagent6,COD,50minCOD(70%),Fenton50min。2.2.4 ,30%H2O2240mg/L、50min,,7。7 FentonFig.7 InfluenceoftemperatureonCODremovalbyFentonreagent83第17期李德生,等:Fenton试剂强化铁炭微电解预处理高浓有机废水第22卷,。Fenton,,[10、11]。7,,COD,,(20℃)。2.3 +Fenton、,,15dCODFentonCOD,8。8 +FentonFig.8 EffectofCODremovalbycombinedprocessofferriccarbonmicro-electrolysisandFentonreagent8,Fenton,COD45%75%,B/C0.35。+Fen-ton、,。3 结论① pH2.2、100min,COD45%,Fe2+180mg/L,FentonFe2+。② Fenton,50min、H2O2(30%)240mg/L,COD60%。③ +Fenton,COD75%,。、,。:[1] ,,,.[J].,2001,17(12):66-68.[2] ,,.[J].,2003,29(2):68-70.[3] ,.[J].,2004,5(10):72-75.[4] JohnsonTL.Kineticsofhalogenatedorganiccompounddegradationbyironmetal[J].EnvironSciTechnol,1996,30:2634-2640.[5] Ghizlainekaichouh,OturanN,OturanMA.DegradationoftheherbicideimazapurbyFentonreactions[J].Envi-ronChemLett,2004,2:31-33.[6] ,.[J].,2003,19(10):58-60.[7] ,.[J].,2001,29(11):1294-1298.[8] DelaatJ,GallardH,AncelinS,etal.ComparativestudyofoxidationofatrazineandacetonebyH2O2/UV,Fe(Ⅲ)/UV,Fe(Ⅲ)/H2O2/UVandFe(Ⅱ)orFe(Ⅲ)/H2O2[J].Chemospere,1999,39(15):2693-2706.[9] ,.Fenton[J].,2005,24(3):27-29.[10] BoyeB,FarniaG,SandonaG.Removalofvegetaltan-ninsfromwastewaterbyelectroprecipitationcombinedwithelectrogeneratedFentonoxidation[J].JApplElec-trochem,2005,35:369-374.[11] ,,.Fenton[J].,2005,21(3):41-43.:(0931)4956163E-mail:Lids@mai.llzjtu.cn:2006-03-1784第17期 中国给水排水 第22卷