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当前位置:首页 > 商业/管理/HR > 管理学资料 > Fenton氧化活性炭吸附协同深度处理抗生素制药废水研究祁佩时
Vol.27,No.6,2008,、,,COD、、、pH[1,2]。,,,,。Fenton2060,FentonHO·,2.8eV,[3]。Fenton[4,5],Fenton,Fenton/。Fenton/,,,。1.1Fenton-1,1,1,2(1.,150090;2.,150090)Fenton-。、pH、H2O2、Fe2+、,COD。:30℃,pH5,H2O2(30%)300mg/L,FeSO4·7H2O80mg/L,120min,50mg/LFenton,COD68.5%,。Fenton-:X703.1:A:1009-0177(2008)06-0038-04StudyonAdvancedTreatmentofPharmaceuticalWastewaterContainingAntibioticbyFentonOxidationCooperatedwithActiveCarbonAdsorptionQIPei-shi1,WANGNa2,LIUYun-zhi1,MAChao2(1.StateKeyLaboratoryofUrbanWaterResourcesandEnvironment,HarbinInstituteofTechnology,Harbin150090,China;2.HeiLongJiangUrbanPlanningSurveyingDesignandResearchInstitute,Harbin150090,China)AbstractThetreatmentofthesecondeffluentofpharmaceuticalwastewatercontainingantibioticbyFentonoxidationcooperatedwithactivecarbonadsorptionisstudied.ThefactorshavingeffectsonCODremovalofpharmaceuticalwastewaterbyFentonoxidationcooperatedwithactivecarbonadsorption,suchastemperature,pH,H2O2(30%)dosage,FeSO4·7H2Odosage,reactiontime,activecarbondosageandthewayofputtinginarediscussed.Intheoptimisticconditions68.5%ofCODremovalisachievedatT=30℃,pH=4,H2O2(30%)=300mg/L,FeSO4·7H2O=80mg/L,t=120min,massconcentrationofactivecarbonputatthesametimeofFentonoxidationwas50mg/L,thetreatedwaterreachedthefirst-gradenationaldischargestandard.KeywordspharmaceuticalwastewaterantibioticFentonoxidationcooperatedwithactivecarbonadsorptionprocessadvancedtreatment[]2008-03-28[](1955-),,,,,,,,。:13904639918,0451-86282317;E-mail:qipeishi@163.com。[],:13895793474;E-mail:wangna-202@163.com。2008,27(6):38-41WaterPurificationTechnology38--DOI:10.15890/j.cnki.jsjs.2008.06.007WATERPURIFICATIONTECHNOLOGYVol.27,No.6,2008December25th,2008,,(35℃)—,1。1.2:pHS-25,,。:30%H2O2,FeSO4·7H2O,,95%~98%,NaOH。1.31.3.1Fenton[6]200mL,pH,,FeSO4·7H2O,30%H2O2,,NaOHpH8~9,COD。1.3.2,1~2mm,2~3mm。,,24h,,24h,,,。Fenton,COD,:(1)Fenton150mL,,,COD。(2)200mL,,,150mL,FentonFentonCOD。(3)150mL,,FentonFenton,COD。1.4COD,BOD5,pH。2.1Fenton,、pH、、Fe2+、H2O2[7]。2、3。50℃,pH5,90min,Fe2+80mg/L,H2O2300mg/L。pHFe2+H2O2。pH,pH,。2.2COD2.2.1CODAH2O2/(mg·L-1)BFe2+/(mg·L-1)C/℃D/minEpH60202040118040306033006040805420805010072Tab.2Factorleveloforthogonalexperiment3Tab.3ResultsoforthogonalexperimentABCDECOD/%111111218.010.3212222193.720.3313333174.728.1414444168.630.6521234234.03.7622143210.713.3723412162.133.3824321165.232.0931342155.536.01032431163.532.71133124242.00.41234213186.623.21341423147.539.31442314240.80.91543241175.227.91644132232.34.4-----243-K1j/%89.389.328.467.7102.9--K2j/%82.367.275.192.074.0--K3j/%92.389.797.068.9103.9--K4j/%72.590.2135.9107.835.6--Max(K)92.390.2135.9107.8103.9--R19.823.060.840.168.3--A3B4C4D4E3--1Tab.1WaterqualityofbiologicallytreatedpharmaceuticalwastewaterpHCOD/(mg·L-1)BOD5/(mg·L-1)/℃6.8~7.5200~26025~3528~3339--Vol.27,No.6,2008pH5,90min,FeSO4·7H2O80mg/L,30%H2O2300mg/L,COD1。1,70℃,COD;70℃,COD。,,。,。Fenton,,;H2O2O2H2O。1,70℃COD65%,,30℃。2.2.2pHCOD30℃,90min,FeSO4·7H2O80mg/L,30%H2O2300mg/L,pHCOD2。2,pH,pH3~5,,COD;pH5,pH,Fenton,pH,H2O2,;pH3,Fenton,pH,H2O2Fe2+·OH,。pH4COD,52%,pH5COD48%,pH4,pH54,pH,,pH5。2.2.3COD30℃,pH5,FeSO4·7H2O80mg/L,30%H2O2300mg/L,COD3。3,COD,120min;120min,,。120min,COD50%。120min。2.2.4Fe2+COD30℃,120min,pH5,30%H2O2300mg/L,FeSO4·7H2OCOD4。4Fe2+COD,CODFe2+,Fe2+80mg/L,COD,,Fe2+H2O2Fe3+,FeSO4·7H2O80mg/L。2.2.5H2O2COD30℃,pH5,1CODFig.1EffectoftemperatureonCODremovalefficiency2pHCODFig.2EffectofpHvalveonCODremovalefficiency3CODFig.3EffectoftimeonCODremovalefficiency,,,.Fenton-40--WATERPURIFICATIONTECHNOLOGYVol.27,No.6,2008December25th,2008120min,FeSO4·7H2O80mg/L,H2O2COD5。5,CODH2O2。H2O2300mg/L,COD。300mg/LH2O2,COD55%,COD100mg/L,《》(GB8978-1996),。2.3CODpH5,30℃,120min,FeSO4·7H2O80mg/L,H2O2300mg/L,,COD6。6,COD。Fenton,,,50mg/L,COD68.5%,。,2-3。Fenton/,。:30℃,120min,pH5,FeSO4·7H2O80mg/L,30%H2O2300mg/L,50mg/L,《》(GB8978-1996)。,,,,。[1]Kümmerer,K.Drugsintheenvironment:emissionofdrugs,diagnosticaidsanddisinfectantsintowastewaterbyhospitalsinrelationtothesourcesofreview[J].Chemosphere,2001,45(6-7):957-969.[2]Kümmerer,K.Biodegradabilityofsomeantibiotics,eliminationofthegenotoxicityandaffectionofwastewaterbacteriainasimpletest[J].Chemosphere,2000,40(7):701-710.[3],,.Fenton[J].,2008,29(5):1271-1275.[4],,.Fenton[J].,2008,31(3):88-90.[5]AhmadiM,VahabzadehF,BonakdarpourB,etal.ApplicationofthecentralcompositedesignandresponsesurfacemethodologytotheadvancedtreatmentofoliveoilprocessingwastewaterusingFenton’speroxidation[J].Hazard.Mater,2005,123(1-3):187-195.[6],,.Fenton-[J].,2003,42(3):440-443.[7]ZuchengWu,MinghuaZ.Synergeticeffectsofanodic-cathodicelectrocatalysisforphenoldegradationinthepresenceofiron(II)[J].Chemophere,2002,48,:1089-1096.4Fe2+CODFig.4EffectofFe2+onCODremovalefficiency6CODFig.6EffectofactivecarbondosageonCODremovalefficiencyindifferentways5H2O2CODFig.5EffectofhydrogenperoxidedosageonCODremovalefficiency41--
本文标题:Fenton氧化活性炭吸附协同深度处理抗生素制药废水研究祁佩时
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