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Fenton-CODCr、,,,,,,。,,。Fenton,pHFeSO4Fe2+H2O2,Fe2+H2O2,:(2008ZX07314-001-09);(863)(2008AA06Z301):2011-08-01;:2011-08-31!!!!!!!!!!!!!!!!!!!!!!!!1,4,2,3,4,1(1.,300384;2.,300074;3.,100029;4.,100085):,Fenton-。Fenton、pH、H2O2、Fe2+、pH。Fenton60min,pH3.5,H2O2FeSO4·7H2O6.5mmol/L600mg/L,pH6.5,PAM0.9mg/L,CODCr、78.86%、96.64%98.65%,m(BOD5)/m(CODCr)0.180.5,。:Fenton;;;;:X703.1:A:%1009-2455(2011)05-0015-05PretreatmentofchemicalintegratedwastewaterbyFenton-flocculationprocessLUOJiu-peng1,4,HANFei2,JIANGQi3,TIANBing-hui4,SUNLi-ping1(1.DepartmentofEnvironmentalandMunicipalEngineering,TianjinInstituteofUrbanConstruction,Tianjin300384,China;2.NorthChinaMunicipalEngineeringDesignandResearchInstitute,Tianjin300074,China;3.NationalMajorScienceandTechnologyProgramManagementOfficeforWaterPollutionControlandTreatment,Beijing100029,China;4.ResearchCenterforEco-EnvironmentalSciences,ChineseAcademyofScience,Beijing100085,China)Abstract:Takingchemicalintegratedwastewaterastheresearchobject,anexperimentofFenton-flocculationprocesstreatingintegratedwastewaterfromachemicalparkwascarriedout.TheinfluencesofFentonreactiontime,initialpHvalue,dosageofH2O2andFe2+,initialpHvalueoftheflocculation,flocculantdosageandsomeotherfactorsonthetreatmenteffectwereinvestigated.Itcouldbeseenthat,whentheFentonreactiontimewas60min,theinitialpHvaluewas3.5,thedosageofH2O2andFeSO4·7H2Owere6.5mmol/Land600mg/Lrespectively,theinitialpHvalueoftheflocculationwas6.5,thePAMdosagewas0.9mg/L,theremovalratesofCODCr,turbidityandchromaintherawwaterreached78.86%、96.64%and98.65%respectively,them(BOD5)/m(CODCr)increasedfrom0.18toabove0.5,thebiodegradabilityofthewastewaterwassignificantlyimproved.Keywords:Fenton;flocculation;chemicalintegratedwastewater;pretreatment;biodegradabilityINDUSTRIALWATER&WASTEWATERVol.42No.5Oct.,2011·15·INDUSTRIALWATER&WASTEWATERVol.42No.5Oct.,20111Tab.1QualityofrawwaterpH/NTU/ρ(CODCr)/(mg·L-1)ρ(BOD5)/(mg·L-1)6.89~7.6858.40~71.10753.76~1707.52594.02~866.43113.20~150.961FentonCODCrFig.1ImpactofFentonreactiontimeonCODCrremoval20406080100120/minρ(CODCr)/(mg·L-1)300270240210180150CODCr/%757065605550,·OH,2.80V,F2(3.06V),CO2H2O,,[1-6]。,,。,,、,。Fenton2(),,,,。11.1,。、、、,80%。,。201011~12。,1。1.2(pH3.5、H2O26.5mmol/L、FeSO4·7H2O230mg/L、2.0mg/L):1L,H2SO4NaOHpH,FeSO4·7H2OH2O2,NaOHpH,,FentonCODCr。1.3pH:PHS-3CpH;:HACH2100AN;:XZ-S;:HZQ-F160A;CODCr:HACH;BOD5:;Zeta:MalvernZitasizer2000Zeta。22.1Fenton2.1.1CODCrCODCr1。1,20~40min,CODCr,40~60min,,60min,CODCr,,60min,Fenton。P.K.Malik[7],FentonFe2+,,,Fe2+,Fe3+Fenton,。,Fenton,[8-9]:·OH+·OH=H2O2(1)·OH+H2O2=H2O+HO2(2)·OH,,。Fenton60min。2.1.2pHCODCrpHCODCr2。2,pH2.02.5,CODCr·16·2pHCODCrFig.2ImpactofinitialpHvalueonCODCrremoval23456pHρ(CODCr)/(mg·L-1)300250200150100CODCr/%807570656055503H2O2CODCrFig.3ImpactofH2O2dosageonCODCrremoval051015202530H2O2/(mmol·L-1)ρ(CODCr)/(mg·L-1)240220200180160140CODCr/%7774716865624FeSO4·7H2OCODCrFig.4ImpactofFeSO4·7H2OdosageonCODCrremoval100200300400500600700800900FeSO4·7H2O/(mg·L-1)ρ(CODCr)/(mg·L-1)250230210190170150130CODCr/%8075706560,2.53.5,pH3.5CODCr,pH3.56.0,CODCr,5.06.0,pH6.0。,,CODCr,pH3.5,pHCODCr。,Fenton,Fe2+pH,,Fe2+H2O2·OH。pH·OH,Fe2+;pH,H+,Fe3++HO2=Fe2++O2+H+,Fe3+Fe2+[10],Fe2+Fe3+,Fenton。2.1.3H2O2CODCrH2O2CODCr3。3,H2O21.625mmol/L26mmol/L,H2O2,CODCr。H2O2Fenton,H2O2Fenton。H2O2,,·OH,,CODCr;H2O2,·OH,H2O2·OH[11-12],,。13mmol/L,CODCr75.22%,6.5mmol/L,CODCr73.51%,97.70%,H2O26.5mmol/L。2.1.4FeSO4·7H2OCODCrFeSO4·7H2OCODCr4。4,120~900mg/L,FeSO4·7H2O,CODCr、、。Fe2+·OH,Fe2+,H2O2[10]。Fe2+Fenton,Fe2+,Fe2++H2O2=Fe3++OH-+·OH·OH,·OH,[13];FeSO4·7H2O,Fe2+,·OH、,;Fe2+,H2O2,·OHFe3+,。600~720mg/L,CODCr,FeSO4·7H2O。2.2Fenton,pH,,,:Fenton-·17·INDUSTRIALWATER&WASTEWATERVol.42No.5Oct.,20115pHZetaFig.5ZetapotentialunderdifferentpHconditions6.06.57.07.58.0pHZeta/mV-4-5-6-7-8-96pHFig.6ImpactofflocculationpHvalueonturbidityremoval6.06.57.07.58.0pH/NTU1.21.00.80.60.40.20/%99.499.299.098.898.698.47pHCODCrFig.7ImpactofflocculationpHvalueonCODCrremoval6.06.57.07.58.0pHρ(CODCr)/(mg·L-1)320300280260240220200CODCr/%7875726966638Fig.8Impactofflocculantdosageonturbidityremoval0.30.60.91.21.51.8PAM/(mg·L-1)/NTU3.53.02.52.01.5/%97.597.096.596.095.595.094.59CODCrFig.9ImpactofflocculantdosageonCODCrremoval0.30.60.91.21.51.8PAM/(mg·L-1)ρ(CODCr)/(mg·L-1)350300250200150CODCr/%8580757065606.0、6.5、7.0、7.58.0,pHZeta5。5,pH6.08.0,Zeta,,,(PAM)。2.3pHpH6、7。6,pH6.08.0,pH,,pH6.0,99.31%,pH8.098.42%,,,0.8NTU。7,pH,CODCr。[14],ZetapH,pH,Zeta,,,pH,。,pH6.5。2.4PAMPAM8、9。8,PAM0.3~0.6mg/L,。,,。PAM0.6~1.2mg/L,,PAM,,,。·18·2、BOD5CODCrTab.2Chromavalue,massconcentrationofBOD5andCODCrofrawwaterandtreatedwater/ρ(BOD5)/(mg·L-1)ρ(CODCr)/(mg·L-1)m(BOD5)∶m(CODCr)1707.52147.60820.020.17923.1388.68173.350.512,,PAM1.8mg/L,97.33%,,、。96.49%。9,PAM,CODCr、、,PAM0.9mg/L。CODCr,0.9mg/L。2.5,、BOD5CODCr2。2,1707.5223.13,98.65%。BOD5147.6088.68mg/L,CODCr820.02173.35mg/L,m(BOD5)/m(CODCr)0.180.5,。3(1)Fenton:60min、pH3.5、H2O26.5mmol/LFeSO4·7H2O600mg/L。(2),PAM。pH6.5,PAM0.9mg/L,96.49%,。(3)Fenton-、CODCr,,96.64%、98.65%78.86%,m(BOD5)/m(CODCr)0.180.5,,,。:[1]WalterZT
本文标题:Fenton絮凝法预处理化工综合废水的研究罗九鹏
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