期刊文献+

层层自组装界面聚合技术制备复合正渗透膜

Preparation of composite positive permeable membrane by layer-by-layer self-assembly interface polymerization technology
下载PDF
导出
摘要 以聚醚砜为膜材料,聚乙烯醇为亲水改性剂,聚多巴胺为交联剂,采用热致相分离法制备了负载聚多巴胺层的聚醚砜基膜;再以间苯二胺为水相单体,均苯三甲酰氯为油相单体,利用层层自组装界面聚合技术可制备复合正渗透膜。结果表明:将基膜依次在聚阳和聚阴离子电解质溶液中各反应15 min,然后浸泡于去离子水中5 min,所制备的复合正渗透膜的水通量最高(28.2 L/h),盐反通量较低(3.9 g/h),膜的过滤性能最好。 The polyethersulfone based membrane supported by polydopamine layer was prepared by thermally-induced phase separation technology with polyethersulfone as the membrane material,pol-yvinyl alcohol as the hydrophilic modifier,and polydopamine as the cross-linking agent.The com-posite positive permeable membrane could be ob-tained by layer-by-layer self-assembly interface polymerization technology with the m-phenylene as water phase monomer and the tribenzoyl chloride as oil phase monomer.The results showed that when the based membrane was successively reacted in the polycationic and polyanion electrolyte solution for 15 min,and then soaked in deionized water for 5 min,the prepared composite positive permeable membrane had the highest water flux(28.2 L/h)and a lower salt reverse flux(3.9 g/h),and the fil-tration performance of membrane was the best.
作者 姚彬 张玉荣 张文存 朱瑞龙 YAO Bin;ZHANG Yu-rong;ZHANG Wen-cun;ZHU Rui-long(Shaanxi Research Design Institute of Petroleum and Chemical Industry,Xi'an 710054,China)
出处 《石化技术与应用》 CAS 2020年第3期175-177,共3页 Petrochemical Technology & Application
基金 陕西省重点产业创新链资助项目(项目编号:2017 ZDCXL-GY-07-04)。
关键词 聚醚砜 热致相分离技术 层层自组装界面聚合技术 复合正渗透膜 polyethersulfone thermally-induced phase separation technology layer-by-layer self-assembly interface polymerization technology com-posite positive permeable membrane
  • 相关文献

参考文献2

二级参考文献36

  • 1Ghaffour N,Missimer T M,Amy G L.Technical reviewand evaluation of the economics of water desalination:cur-rent and future challenges for better water supply sustain-ability[J].Desalination,2013,309:197-207.
  • 2Lutchmiah K,Verliefde A R D,Roest K,et al.For-ward osmosis for application in wastewater treatment:A review[J].Wat Res,2014,58:179-197.
  • 3Zhao S,Zou L,Tang C Y,et al.Recent developmentsin forward osmosis:opportunities and challenges[J].JMembr Sci,2012,396:1-21.
  • 4Lee S,Boo C,Elimelech M,et al.Comparison of foulingbehavior in forward osmosis (FO)and reverse osmosis(RO)[J].J Membr Sci,2010,365(1/2):34-39.
  • 5Zhang X,Ning Z,Wang D K,et al.Processing munici-pal wastewaters by forward osmosis using CTA mem-brane[J].J Membr Sci,2014,468:269-275.
  • 6Cui Y,Ge Q,Liu X Y,et al.Novel forward osmosisprocess to effectively remove heavy metal ions[J].JMembr Sci,2014,467:188-194.
  • 7Mondal P,Tran A T K,Van der Bruggen B.Removalof As (V)from simulated groundwater using forwardosmosis:Effect of competing and coexisting solutes[J].Desalination,2014,348:33-38.
  • 8Cath T Y,Childress A E,Elimelech M.Forward os-mosis:principles,applications,and recent develop-ments[J].J Membr Sci,2006,281(1/2):70-87.
  • 9Wang K Y,Chung T S,Qin J J.Polybenzimidazole(PBI)nanofiltration hollow fiber membranes applied inforward osmosis process[J].J Membr Sci,2007,300(1/2):6-12.
  • 10Li X,Wang K Y,Helmer B,et al.Thin-film compos-ite membranes and formation mechanism of thin-filmlayers on hydrophilic cellulose acetate propionate sub-strates for forward osmosis processes[J].Ind EngChem Res,2012,51(30):10039-10050.

共引文献9

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