反渗透技术在垃圾渗滤液处理中的应用143f527427284b73f242501a

08/2012[1]CODCr0.010m500100000Da100500Da100Da[2][3]GB16889-2008ROreverseosmosisCOD98%99%[4-5]1977Chian[6]RO[7-8]ROROChan[5](VSEPRO-vibratoryshear-enhancedprocessingreverseosmosis)NENTpH0.09CODNH3–N96%98%8000mg/L2620mg/L200mg/L5mg/LRO2003500m380%pH66.599%Ca2+Ba2+Mg2+99.9%[-9]ROM.Šír[10]7.4m2300L/h203MPa:TDS99%TOC97%108/2012[1]CODCr0.010m500100000Da100500Da100Da[2][3]GB16889-2008ROreverseosmosisCOD98%99%[4-5]1977Chian[6]RO[7-8]ROROChan[5](VSEPRO-vibratoryshear-enhancedprocessingreverseosmosis)NENTpH0.09CODNH3–N96%98%8000mg/L2620mg/L200mg/L5mg/LRO2003500m380%pH66.599%Ca2+Ba2+Mg2+99.9%[-9]ROM.Šír[10]7.4m2300L/h203MPa:TDS99%TOC97%108/2012[11][12-13]ROCaSO4ROCaSO4CaSO4JianxinLi[14][15]DTROXSEM-EDX,SSiCaFeAlNghiem[16][17]DOMdissolvedorganicmatterROOhsungKwon[18]NFCOD1380mg/L1590mg/L10149mg/L90%pH2.42.63hpH11.611.8+EDTA97.8%RO08/2012[11][12-13]ROCaSO4ROCaSO4CaSO4JianxinLi[14][15]DTROXSEM-EDX,SSiCaFeAlNghiem[16][17]DOMdissolvedorganicmatterROOhsungKwon[18]NFCOD1380mg/L1590mg/L10149mg/L90%pH2.42.63hpH11.611.8+EDTA97.8%RO08/2012DTRORORORORenou[19]+ROTMPtransmembranepressureVRFvolumetricreductionfactorVRFVRFPiatkiewicz[20]-MF()-UF()-ROMFUFROMF5%10%UF25%35%RO90%NFROCaSO4NFNFROHPRO2.04.0MPaNFROHPRONF-RO-HPRO8.512kW•h/m3(95%)Bohclziewicz[21]+++++RO++RO[22]:EWGEROSECOD2074mg/L1685mg/L8500S/cm81mg/L183mg/L320S/cm100%TimoMaria[23]/90%-UASB+SBR+RO500m3/d600025/m3CMFROROCMFRO1722+ROUASB-MBR-DTROCOD38000mg/L50mg/LBOD20000mg/L10mg/LNH3-N2000mg/L10mg/LSS1000mg/L5mg/LHalilHasar[24]ROSRT3090%CODMBRROWon-YoungAhn[25]+MBR+RO50m3/dMBRRO[26]RO08/2012DTRORORORORenou[19]+ROTMPtransmembranepressureVRFvolumetricreductionfactorVRFVRFPiatkiewicz[20]-MF()-UF()-ROMFUFROMF5%10%UF25%35%RO90%NFROCaSO4NFNFROHPRO2.04.0MPaNFROHPRONF-RO-HPRO8.512kW•h/m3(95%)Bohclziewicz[21]+++++RO++RO[22]:EWGEROSECOD2074mg/L1685mg/L8500S/cm81mg/L183mg/L320S/cm100%TimoMaria[23]/90%-UASB+SBR+RO500m3/d600025/m3CMFROROCMFRO1722+ROUASB-MBR-DTROCOD38000mg/L50mg/LBOD20000mg/L10mg/LNH3HH-N2000mg/L10mg/LSS1000mg/L5mg/LHalilHasar[24]ROSRT3090%CODMBRROWon-YoungAhn[25]+MBR+RO50m3/dMBRRO[26]RO08/201253+CODCrBOD5NH3-NSS55mgL20mgL8mgL40mgL1mgLRO5080mS/cm[27]CODTDS[28](Fenton)[29](CCD)(RSM)FentonpHFeSO4•7H2O[H2O2]/[Fe2+]3CODpH3.75FeSO4•7H2O17.91mmol/L[H2O2]/[Fe2+]1.36,COD(72.25%)PrengleNakayamaHangoO3/H2O2[30]H2O2/O3CMFROROH2O2/O3CODH2O2O3HAFA:;[31]ROpHNH3-NCODNH3-NMBR+RO(Landfillgas,LFG),[32](Submergedcombustionevaporation,SCE)RO,RO51070RO[33]CODNH3-NCOD81.6%NH3-N70%COD81.56BOD82.5NH3-N607032.38mL/(L•d)RO08/201253+CODCrBOD5NH3-NSS55mgL20mgL8mgL40mgL1mgLRO5080mS/cm[27]CODTDS[28](Fenton)[29](CCD)(RSM)FentonpHFeSO4•7H2O[H2O2]/[Fe2+]3CODpH3.75FeSO4•7H2HHO17.91mmol/L[H2HHO2]/[Fe2+]1.36,COD(72.25%)PrengleNakayamaHangoO3/H2O2[30]H2O2/O3CMFROROH2O2/O3CODH2O2O3HAFA:;[31]ROpHNH3-NCODNH3-NMBR+RO(Landfillgas,LFG),[32](Submergedcombustionevaporation,SCE)RO,RO51070RO[33]CODNH3-NCOD81.6%NH3-N70%COD81.56BOD82.5NH3HH-N607032.38mL/(L•d)RO08/2012RO1WeiLi,TaoHua,QixingZhou,ShuguangZhang,FengxiangLi.Treatmentofstabilizedlandfillleachatebythecombinedprocessofcoagulation/flocculationandpowderactivatedcarbonadsorption.Desalination,2010,264:56622BjarneNicolaisen.Developmentsinmembranetechnologyforwatertreatment.Desalination,2002,153:355360.3M.Ince,E.Senturk,G.OnkalEngin,B.Keskinler.Furthertreatmentoflandfillleachatebynanofiltrationandmicrofiltration–PAChybridprocess.Desalination,2010,255:52604ThomasA.Peters.Purificationoflandfillleachatewithreverseosmosisandnanofiltration.Desalination,1998,119:2892935GilbertY.S.Chan,JieChang,TonniAgustionoKurniawan,Cheng-XinFu,HongJiang,YingJe.Removalofnon-biodegradablecompoundsfromstabilizedleachateusingVSEPROmembranefiltration.Desalination,2007,202:3103176E.S.K.Chian.Stabilityoforganicmatterinlandfillleachates.WaterResearch,1977,11(2):2252327T.Bilstad,M.V.Madland,Leachateminimizationbyreverseosmosis.WaterScience&Technology,1992,25(3):1171208KristinaLinde,Ann-sofiJönsson,RolandWimmerstedt.Treatmentofthreetypesoflandfillleachatewithreverseosmosis.Desalination,1995,101:21309,,.DT-RO.2005,318414510M.Šír,M.Podhola,T.Patoka,Z.Honzajková,P.Kocurek,M.Kubal,M.Kuraš.Theeffectofhumicacidsonthereverseosmosistreatmentofhazardouslandfillleachate.HazardousMaterials,2011,08(079):1511VignesaeranS.,VigneswaranB.andBenAimR.Applicationofmicrofiltrationforwaterandwastewatertreatment.EnvironmentalSanitationReviews,1991,31(1):172112K.Košuti,B.Kunst.ROandNFmembranefoulingandcleaningandporesizedistributionvariations.Desalination,2002,150:11312013RaffaeleMolinari,PietroArgurio,LeonardoRomeo.Studiesoninteractionsbetweenmembranes(ROandNF)andpollutants(SiO2,NO3-,Mn+andhumicacid)inwater.Desalination,2001,138:27128114JianxinLi,L.J.Koenb,D.K.Hallbauer,L.Lorenzen,R.D.Sanderson.Interpretationofcalciumsulfatedepositiononreverseosmosismembranesusingultrasonicmeasurementsandasimplifiedmodel.Desalination200518622724115..2007Vol.1,No.7101105.16KhaL.Tu,AllanR.Chivas,LongD.Nghiem.Effectsofmembranefoulingandscalingonboronrejectionbynanofiltrationandreverseosmosismembranes.Desalination201127926927717,,,..,2009,10(3):1783