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On the fouling mechanism of polysulfone ultrafiltration membrane in the treatment of coal gasification wastewater
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文摘
Membrane fouling has been investigated by using a polysulfone ultrafiltration membrane with the molecular weight cutoff of 20 kDa to treat crushed coal pressurized gasification wastewater. Under the conditions of different feed pressures, the permeate flux declines and rejection coefficients of pollutants referring to three parameters (total organic carbon (TOC), chroma and turbidity) were studied. The membrane fouling mechanism was simulated with three classical membrane fouling models. The membrane image and pollutants were analyzed by scanning electron microscopy and gas chromatography-mass spectrography (GC-MS). The results indicate that the permeate flux decreases with volume reduction factor before reaching a constant value. The rejection coefficients were also measured: fTOC = 70.5%, fC = 84.9% and fT = 91%. Further analysis shows that the higher the feed pressure is, the sooner the permeate flux reaches constant value and the more sharply the permeate flux declines. Constant flux indicates a nonlinear growth with feed pressure (PF): when PF equals 1.2 bar, the mark for the critical flux, slight membrane fouling occurs; when PF exceeds 1.2 bar, cake layer pollution aggravates. Also the rejection coefficients of global pollutant increases slightly with PF, suggesting the possibility of cake compression when PF exceeds 1.2 bar. Through regression analysis, the fouling of polysulfone ultrafiltration membrane could be fitted very well by cake filtration model. The membrane pollutants were identified as phthalate esters and long-chain alkenes by GC-MS, and a certain amount of inorganic pollutants by X-ray photoelectron spectroscopy.Keywordsmembrane foulingultrafiltration membranecoal gasification wastewaterrejection coefficientReferences1.Li H Q, Han H J, Du M A, Wang W. Removal of phenols, thiocyanate and ammonium from coal gasification wastewater using moving bed biofilm reactor. 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Treatment of coal gasification of wastewater by a two continuous UASB system with step-feed for COD and phenols removal. Bioresource Technology, 2011, 102(9): 5454–5460CrossRefGoogle ScholarCopyright information© Higher Education Press and Springer-Verlag Berlin Heidelberg 2016Authors and AffiliationsXue Zou12Jin Li1Email author1.School of Civil EngineeringBeijing Jiaotong UniversityBeijingChina2.College of Architectural EngineeringNorth China University of TechnologyBeijingChina About this article CrossMark Publisher Name Higher Education Press Print ISSN 2095-0179 Online ISSN 2095-0187 About this journal Reprints and Permissions Article actions Export citation .RIS Papers Reference Manager RefWorks Zotero .ENW EndNote .BIB BibTeX JabRef Mendeley Share article Email Facebook Twitter LinkedIn Cookies We use cookies to improve your experience with our site. More information Accept Over 10 million scientific documents at your fingertips

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