期刊文献+

界面聚合表面改性法制备高效抗污染油水分离复合膜 被引量:6

ANTIFOULING COMPOSITE MEMBRANES FOR OIL/WATER SEPARATION PREPARED BY SURFACE-MODIFICATION USING INTERFACIAL POLYMERIZATION
下载PDF
导出
摘要 A fouling-resistant ceramic-supported polymer composite membrane was developed for removal of oil-in-water (O/W) microemulsions. The composite membrane was featured with an asymmetric three-layer structure,i.e. ,a porous ceramic membrane substrate,a polyethersulfone (PES) ultrafiltration sub-layer,and a polyamide/polyvinyl alcohol (PVA) composite thin top-layer.The PES polymer was cast onto the tubular porous ceramic membrane with the sol-gel method,and the polyamide/PVA composite thin top-layer was fabricated with the interfacial polymerization method. The prepared composite membrane showed good performance for treating the O/W microemulsions with a mean diameter of 2.4 μm. At the operating pressure of 0.4 MPa,the hydraulic permeability remained steady at about 280 L·m -2 ·h -1 after a period of operation,the oil concentration in the filtrate was always less than 1.15 mg·L -1 ,and the oil rejection coefficient was higher than 99.1% from the beginning of the operation. A fouling-resistant ceramic-supported polymer composite membrane was developed for removal of oil-in-water (O/W) microemulsions. The composite membrane was featured with an asymmetric three-layer structure, i.e., a porous ceramic membrane substrate, a polyethersulfone (PES) ultrafiltration sublayer, and a polyamide/polyvinyl alcohol (PVA) composite thin top-layer. The PES polymer was cast onto the tubular porous ceramic membrane with the sol-gel method, and the polyamide/PVA composite thin top-layer was fabricated with the interfacial polymerization method. The prepared composite membrane showed good performance for treating the O/W microemulsions with a mean diameter of 2.4 /μm. At the operating pressure of 0.4 MPa, the hydraulic permeability remained steady at about 280 L&middotm-2&middoth-1 after a period of operation, the oil concentration in the filtrate was always less than 1.15 mg&middotL-1, and the oil rejection coefficient was higher than 99.1% from the beginning of the operation.
出处 《化工学报》 EI CAS CSCD 北大核心 2004年第4期664-667,共4页 CIESC Journal
基金 教育部跨世纪优秀人才基金 胜利石油管理局工程机械总厂资助项目~~
关键词 复合膜 抗污染 油水分离 微乳液 界面聚合 Microemulsions Polymerization Wastewater treatment
  • 相关文献

参考文献9

  • 1Cheryan M, Rajagopalan N. Membrane Processing of Oily Streams:Wastewater Treatment and Waste Reduction.J. Membr. Sci.,1998,151:13-28
  • 2Kim I C, Choi J G, Tak T M. Sulfonated Polyethersulfone by Heterogeneous Method and Its Membrane Performance.J. Appl. Polym. Sci.,1999,74:2046-2055
  • 3Tansel B, Regula J, Shalewitz R. Treatment of Fuel Oil and Crude Oil Contaminated Waters by Ultrafiltration Membranes.Desalination,1995,102:301-311
  • 4Kong J, Li K. Oil Removal from Oil-in-water Emulsions Using PVDF Membranes.Sep. Purif. Technol.,1999,16:83-93
  • 5Ma H, Bowman C N, Davis R H. Membrane Fouling Reduction by Back Pulsing and Surface Modification.J. Membr. Sci.,2000,173:191-200
  • 6Faibish R S, Cohen Y. Fouling-resistant Ceramic-supported Polymer Membranes for Ultrafiltration of Oil-in-water Microemulsions.J. Membr. Sci.,2001,185:129-143
  • 7Faibish R S, Cohen Y. Fouling and Rejection Behavior of Ceramic and Polymer-modified Ceramic Membranes for Ultrafiltration of Oil-in-water Emulsions and Microemulsions. Colloids and Surfaces A,2001,191:27-41
  • 8Shekar B C, Veeravazhuthi V, Sakthivel S, Mangalaraj D, Narayandass S K. Growth, Structure,Dielectric and AC Conduction Properties of Solution Grown PVA Films.Thin Solid Films,1999,348:122-129
  • 9Wang Jing(王静), Zhang Yushan(张雨山).Present State of the Application of the Ultrafiltration Membrane and Microfiltration Membrane to Wastewater Treatment and Its Development Trend.Industrial Water Treatment(工业水处理)

同被引文献109

引证文献6

二级引证文献24

相关作者

内容加载中请稍等...

相关机构

内容加载中请稍等...

相关主题

内容加载中请稍等...

浏览历史

内容加载中请稍等...
;
使用帮助 返回顶部