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当前位置:首页 > 商业/管理/HR > 企业文化 > 磁纳米类芬顿法与芬顿法处理焦化废水的对比研究杨乐
121231211.1500902.2142053.056038Fe3O4、Fe3O4-H2O2。Fe3O4COD67.9%97.8%COD68.04%98.48%。。Fe3O4X703C1000-4602201701-0084-05E-mailguohaijuan@163.comComparativeStudyonMagneticNanoparticlesFenton-likeMethodandFentonMethodforCokingWastewaterTreatmentYANGLe12YANGJi-xian1GUOHai-juan23MAFang12QIUShan11.StateKeyLaboratoryofUrbanWaterResourceandEnvironmentHarbinInstituteofTechnologyHarbin150090China2.YixingEnvironmentalProtectionResearchInstituteHarbinInstituteofTechnologyYixing214205China3.CollegeofEnergyandEnvironmentalEngineeringHebeiUniversityofEngineeringHandan056038ChinaAbstractTosolvetheproblemsthatthebiochemicaleffluentfromtraditionalprocessesinthetreatmentofcokingwastewatercouldnotmeetthestandardanditwashardforadvancedtreatmentthebiochemicaleffluentofcokingwastewaterwasdegradedusingFe3O4magneticnanoparticlesFenton-likemethodandFentonmethodrespectivelyandFe3O4-H2O2wasreusedbecauseitcouldberecycledbymagneticseparation.Theoptimumreactionconditionswereobtainedthroughsinglefactoranalysismeth-od.UnderthisconditionFe3O4wasreusedandthesystemwasoperatedstably.TheremovalratesofCODandvolatilephenolwereabove67.9%and97.8%respectively.AftertheparameteroptimizationthetraditionalFentonmethodcouldremoveCODandvolatilephenolby68.04%and98.48%respec-tively.Bothofthemethodscouldtreatcokingwastewaterstablyandeffectively.Aftertheeconomicanal-ysistheFenton-likemethodhasgreatpotentialincost-savingbecauseofitsspecialrepeatabilityandwi-derapplicationprospectsthanthetraditionalFentonmethod.·48·33120171CHINAWATER&WASTEWATERVol.33No.1Jan.2017KeywordsFe3O4Fentoncokingwastewaterrepeatability、12。34。Fe3O4-H2O2pHFe3O4Fe2+H2O2·OH5~7Fe3O4Fe3O4。。11.1Fe3O4Fe3O4Fe3O4MNPsFeCl3·6H2OFeCl2·4H2O2.0mol/LHClFe3+∶Fe2+=2∶150mL1.0mol/LNH3·H2O10min40mm×40mm×20mmFe3O4MNPs5min。。X1。1Fe3O4MNPsXRDFig.1XRDparternsofFe3O4MNPs12θ=30.4°、35.7°、43.4°、53.8°、57.5°、62.8°Fe3O4Fe3O4。1.2FeCl3·6H2O、FeCl2·4H2O、FeSO4·7H2O、、、。pH9.3、COD157.7mg/L、28.3mg/L。1.3Fe3O4MNPs-H2O2pHFe3O4MNPsH2O2。。pHFeSO4·7H2OH2O2。NaOHpH。COD4-。COD60℃60minH2O2。22.10.5g/L、H2O230%1.0mL/L、120minpHCOD2。2pHFig.2EffectofpHonpollutantsremovalbyFenton-likemethod2pH2.5CODCOD·58·.watergasheat.com33175%98%。pH·OHpHH+·OH·OHH2O2H2OO289。pH=2.5、0.5g/L、120minH2O230%0.1、0.2、0.5、1.0、1.5、2.0mL/LCOD3。H2O2≥1.0mL/LCODH2O2COD。H2O2·OH·OHH2O2COD。3H2O2Fig.3EffectofH2O2dosagesonpollutantsremovalbyFenton-likemethodpH=2.5、H2O230%1.0mL/L、120min0.1、0.2、0.5、1.0、1.5、2.0g/LCOD4。4Fe3O4MNPsFig.4EffectofFe3O4MNPsdosagesonpollutantsremovalbyFenton-likemethod4≥1.0g/LCOD。·OH10Fe3O4。pH=2.5、Fe3O4MNPs1.0g/L、H2O230%1.0mL/LCOD73.11%、99.84%。2.2FeSO4·7H2O2.0g/L、H2O230%1.0mL/L、30minpHCOD5。5pHFig.5EffectofpHonpollutantsremovalbyFentonmethod5pH2~4COD。pHpH。pH=3、H2O230%1.0mL/L、30minFeSO4·7H2O0.5、1.0、1.5、2.0、2.5、3.0g/LCOD。FeSO4·7H2OCODFeSO4·7H2O1.0g/LCOD68.04%、98.48%。pH=3、FeSO4·7H2O1.0g/L、30minH2O230%0.1、0.2、0.5、1.0、1.5、2.0mL/LCOD。H2O21.0mL/LCOD51.7、0.43mg/L。pH=3、FeSO4·7H2O1.0g/L、H2O230%1.0mL/L·68·331.watergasheat.comCODCOD68.04%、98.48%。2.3Fe3O4MNPs-H2O2pH=2.5、Fe3O4MNPs1.0g/L、H2O230%1.0mL/L120min。COD4COD46.11、0.41mg/L。。2.4pH=2.5、Fe3O4MNPs1.0g/L、H2O230%1.0mL/L10%Fe3O4MNPs6。6Fig.6RemovalefficiencyofpollutantsbyFenton-likemethodwithcontinuousandstableoperationCOD67.9%97.8%COD40~50mg/L0.24~0.62mg/L。2.5。FeSO4·7H2OH2O21.5/m3Fe3O4H2O2H2O21/m3Fe3O4FeCl3·6H2O、FeCl2·4H2O、HCl、NH3·H2O5000/t90%1.5/m3。pH。。、。3①pH=2.5、Fe3O4MNPs1.0g/L、H2O230%1.0mL/LCODFe3O4MNPs4COD67.9%97.8%。②pH=3、FeSO4·7H2O1.0g/L、H2O230%1.0mL/LCOD。③。1ZhaoWTHuangXLeeDJ.Enhancedtreatmentofcokeplantwastewaterusingananaerobic-anoxic-oxicmembranebioreactorsystemJ.SepPurifTechnol2009662279-286.2WeiXXZhangZYFanQLetal.Theeffectoftreat-mentstagesonthecokingwastewaterhazardouscom-poundsandtheirtoxicityJ.JHazardMater2012239/2404135-141.3.FentonJ.201026·78·.watergasheat.com331393-95.4.Fenton—D.2014.5.Fe3O4-FentonD.2014.6XuLJWangJL.Fenton-likedegradationof24-di-chlorophenolusingFe3O4magneticnanoparticlesJ.ApplCatalBEnviron2012123/12430117-126.7HuangRXFangZQYanXMetal.Heterogeneoussono-FentoncatalyticdegradationofbisphenolAbyFe3O4magneticnanoparticlesunderneutralconditionJ.ChemEngJ201219714242-249.8.FentonJ.200629628-33.9ZhangJBZhuangJGaoLZetal.Decomposingphe-nolbythehiddentalentofferromagneticnanoparticlesJ.Chemosphere20087391524-1528.10XueXFHannaKAbdelmoulaMetal.AdsorptionandoxidationofPCPonthesurfaceofmagnetiteKineticex-perimentsandspectroscopicinvestigationsJ.ApplCatalBEnviron2009893/4432-440.1992-Fe3O4。E-mailyanglehit@126.com櫆櫆櫆櫆櫆櫆櫆櫆櫆櫆櫆櫆櫆櫆櫆櫆櫆櫆櫆櫆櫆櫆櫆櫆櫆櫆櫆櫆櫆櫆櫆櫆櫆櫆櫆櫆櫆櫆櫆櫆櫆櫆櫆櫆櫆櫆2016-04-1883tion201228778-81.2ZhaoSZouLTangCYetal.RecentdevelopmentsinforwardosmosisOpportunitiesandchallengesJ.JMembrSci201239641-21.3.J.2010261438-41.4.CTAJ.201433217-24.5.D.2011.6.D.2013.7SuJCChungTSHelmerBJetal.Enhanceddouble-skinnedFOmembraneswithinnerdenselayerforwastewatertreatmentandmacromoleculerecycleusingsucroseasdrawsoluteJ.JMembrSci2012396492-100.8GaoYBWangYNLiWYetal.CharacterizationofinternalandexternalconcentrationpolarizationsduringforwardosmosisprocessesJ.Desalination2014338165-73.9ParidaVNgHY.ForwardosmosisorganicfoulingEffectsoforg
本文标题:磁纳米类芬顿法与芬顿法处理焦化废水的对比研究杨乐
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