您好,欢迎访问三七文档
当前位置:首页 > 商业/管理/HR > 公司方案 > Fenton氧化深度处理石化废水厂二级出水研究
36720157ENVIRONMENTALSCIENCEVol.36No.7Jul.2015Fenton1222*12111.7300702.100012FentonCOD.COD64.8mg·L-1PO3-4-P0.79mg·L-1H2O230%0.4mL·L-1FeSO4·7H2O0.8g·L-1PAM0.9mg·L-130minCOD24.3%COD50mg·L-1PO3-4-P95.5%1×10380.4%Fenton95.6%.Fenton、.GC-MS11727.Fenton.FentonX703.1X742A0250-3301201507-2597-07DOI10.13227/j.hjkx.2015.07.0362014-08-242015-02-092012ZX07201-005512084841989~E-mailxiaoxiaomu02@163.com*E-mailzhouyuexi@263.netTreatmentofPetrochemicalTreatmentPlantSecondaryEffluentbyFentonOxidationWANGYi12WUChang-yong2ZHOUYue-xi2*ZHANGXue12DONGBo1CHENXue-min11.SchoolofEnvironmentalandMunicipalEngineeringLanzhouJiaotongUniversityLanzhou730070China2.ResearchCenterofWaterPollutionControlTechnologyChineseResearchAcademyofEnvironmentalSciencesBeijing100012ChinaAbstractFentonoxidationwasappliedtotreatthepetrochemicaltreatmentplantsecondaryeffluentbythecontinuousflowconfiguration.TheeffectofFentonagentdosageontheCODandphosphorusremovalandthevariationofthedissolvedorganicmattercharacteristicsduringthetreatmentprocesswereinvestigated.TheresultsshowedtheaverageCODandPO3-4-Pconcentrationswere64.8mg·L-1and0.79mg·L-1respectively.WhenthedosageofH2O230%FeSO4·7H2OandPAMwere0.4mL·L-10.8g·L-1and0.9mg·L-1andtheresidencetimewas30mintheaverageremovalrateofCODandPO3-4-Pwere24.3%and95.5%respectively.TheeffluentCODwaslowerthan50mg·L-1.Thepercentageofdissolvedorganicmatterswithmolecularweightlessthan1×103was80.4%intherawwastewaterhoweverthepercentageincreasedto95.6%whentreatedbyFentonoxidation.Three-dimensionalfluorescenceanalysisshowedthattheFentonoxidationcaneffectivelyremoveproteinandphenols.GC-MSresultsshowedthattherewereabout117kindsoforganicmattersdetectedinthesecondaryeffluentwhilethenumberreducedto27afteroxidationbyFenton.Theorganicscontainingunsaturatedbondhadabetterremovalthanthoseofothertypesoforganics.Fentonoxidationcanbeusedintheadvancedtreatmentofpetrochemicalsecondaryeffluent.KeywordssecondaryeffluentofpetrochemicalwastewateradvancedtreatmentFentonoxidationmolecularweightdistributionorganicmatter.2.1×1010t3%~5%.40%1...19981《》GB8978-1996COD<100mg·L-1.CODBOD55.0mg·L-1234.COD36.Fenton、、、、CO2H2O.FentonFe2+、Fe3+.Fenton、、.FentonFenton、5~8.FentonpH9.pHFentonCODFenton.11.11、FentonFeSO4·7H2O.Fenton43.2L41H2O230%4PAM.14.4LFenton.1.1Table1WastewaterqualityusedinthisstudypHCOD/mg·L-1BOD5/mg·L-1PO3-4-P/mg·L-1TP/mg·L-16.9~7.860~1204.38~2.050.60~1.081.04~1.627.5377.323.140.791.321Fig.1Schematicdiagramoftheexperiment10~12CODH2O230%、FeSO4PAMCOD、UV254、PO3-4-P.1.21.2.1GC-MS13-Agilent7890NIST.HP-5MS60m×250μm×0.25μm40℃3min5℃·min-1300℃3min58min1.0mL·min-1>99.999%5∶189527Fenton260℃.230℃150℃EI70eV29~350m/z0.5min.1.2.2Models8400Millipore400mL4.18×10-3m20.1MPa.0.45μm100×103、30×103、10×103、5×103、3×103、1×103Millipore.TOCTOCTOC.1.2.30.45μmEx200~500nmEm200~500nm5nm0.5s12000nm·min-1700V.1.2.4CODPO3-4-PUV254752TOCTOC-VCPH/CPN.22.12.1.1H2O2COD、UV254、PO3-4-PL6443H2O230%0.2、0.3、0.4、0.5mL·L-1FeSO4·7H2O0.4、0.6、0.80.10g·L-1PAM0.6、0.9、1.21.5mg·L-1.30min.COD、.、、、、UV254.UV254TOC、CODUV2541415.Fenton·OHUV254.2H2O2H2O2·OHCOD、UV254H2O2.H2O2·OH·OH16~18.H2O2Fe2+Fe3+H2O2·OH.FentonH2O2H2O2FentonH2O2COD.H2O20.4mL·L-1UV254COD.COD1.33VFenton2.8VCOD·OH.PO3-4-P85%~90%2H2O2PO3-4-P.2H2O2COD、UV254、PO3-4-PFig.2EffectsofH2O2dosageontheCODUV254andPO3-4-Premoval2.1.2FeSO4COD、UV254、PO3-4-PCOD、PO3-4-PFeSO4·7H2O0.8g·L-13.FentonFe2+、Fe3+.Fe2+、Fe3+.FentonFe2+、Fe3+9952361920.FeSO4·7H2O-Fe2+、Fe3+20.UV254FeSO4·7H2OFeSO4·7H2OFe2+·OH、、、.3FeSO4COD、UV254、PO3-4-PFig.3EffectsofFeSO4dosageontheCODUV254andPO3-4-Premoval2.1.3PAMCOD、UV254、PO3-4-PFentonPAM.Fe2+、Fe3+PAM、Fe.COD、PO3-4-PPAMPAM0.9mg·L-1COD.PAMPAM19.PAMCODPAMCOD.UV25465%~75%PAMUV2544.2.1.4H2O24PAMCOD、UV254、PO3-4-PFig.4EffectsofPAMdosageontheCODUV254andPO3-4-Premoval30%0.4mL·L-1FeSO4·7H2O0.8g·L-1PAM0.9mg·L-130min.COD64.8mg·L-1COD48.7mg·L-1COD24.3%UV2540.534UV2540.171UV25468.0%PO3-4-P0.78mg·L-1PO3-4-P0.04mg·L-1PO3-4-P95.5%3.4%.UV254COD·OH、.《》GB8978-1996A.H2O230%1400·t-1FeSO4·7H2O300·t-1PAM6000·t-11.9·t-1.2.2Fenton51×10321221×103.FentonCC、NN、CO、、CO2H2O.51×10380.4%1×10395.6%00627FentonFenton·OH、.5FentonFenton5FentonTOCFig.5MolecularweightdistributionandTOCvariationofwastewatertreatedbyFentonoxidation.2.3、65Flu1Flu2Flu3、Flu4Flu523~25./Ex/EmFI2.Flu1Flu2Fenton.Flu3.FentonCC、NN.Fenton.6FentonFig.6ContourmapofwastewaterbeforeandafterthetreatmentbyFentonoxidation2Table2PositionandintensityoffluorescenceinwastewatersamplesFlu1Flu2Flu3Flu4Flu5Ex/Em230/345275/345236/400236/407313/401FI/AU1414.0409.2302.5307.8232.42.4500mLGC-MS.7、Fenton.MS11780%、、.Fenton27..6.55nm2.51nm.Fenton95%3.1062367FentonGC-MSFig.7GC-MSspectrogramofthewastewaterbeforeandafterFentonoxidation3FentonTable3NumbersandtypesoforganicsinpetrochemicalsecondaryeffluentandtreatedwastewaterbyFentonoxidation//%//%265.1288.215.601010.50413.412.210.525.9、11.9023.013.731H2O230%0.4mL·L-1FeSO4·7H2O0.8g·L-1PAM0.9mg·L-130minFenton.COD24.3%UV25468.0%PO3-4-P95.5%.COD48.7mg·L-1PO3-4-P0.04mg·L-1《》GB8978-1996A.2Fenton1×1031×103Fenton.3、、Fenton、.4GC-MSFentonCC、NN、CO、.1.M.2011.35.2.J.20136493392-3395.3.
本文标题:Fenton氧化深度处理石化废水厂二级出水研究
链接地址:https://www.777doc.com/doc-6536954 .html