| 离子液体复合膜用于渗透汽化分离乙醇水溶液 |
| 作者：李雪茹1，吕权1，殷海燕1，张晶1，樊文玲2，李磊1 |
| 单位： 1.南京大学化学化工学院化工系，江苏南京 210093；2. 南京中医药大学 药学院，江苏南京 210029 |
| 关键词： 离子液体 支撑液膜 共混膜 渗透汽化 分离性能 |
| DOI号： |
| 分类号： TQ028.8 |
| 出版年,卷(期):页码： 2012,32(3):39-43 |
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摘要： |
| 本文将离子液体[bmim]PF6引入制膜过程，制备了PDMS膜以及离子液体支撑液膜和PDMS-IL共混膜。本文用所制的膜进行渗透汽化实验分离乙醇水溶液，研究料液温度、浓度和真空度等对膜渗透通量和分离因子的影响，并比较了三种膜的分离效果。实验结果表明，在分离乙醇水溶液时，PDMS-IL共混膜的综合分离效果优于普通的PDMS膜，而离子液体支撑液膜分离性能不理想。此外膜渗透通量都随料液温度、浓度的增大而增大，随透过侧压力的增大而减小；分离因子随料液温度、浓度和透过侧压力的增大而减小。 |
| Ionic liquid(IL)[bmim]PF6 was introduced into membrane preparation process to form supported ionic liquid membrane(SILM) and PDMS-IL composite membrane. Pervaporation performance of the prepared membranes were measured and compared thoroughly in the process of ethanol removal from water. The effects of feed temperature, feed concentration and permeation pressure on pervaporation performance were investigated systematically. The experimental results showed that PDMS-IL composite membranes exhibited superior separation performance to common PDMS membrane, while unfortunately that of SILM was not satisfactory. Besides, permeation ?uxes of the membranes all increased with increasing temperature and concentration, whereas they decreased with ascending permeation pressure. Furthermore, separation factors descended with climbing temperature, concentration and permeation pressure. |
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基金项目： |
| 国家自然科学基金青年基金项目（No. 30801552） |
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作者简介： |
| 李雪茹(1987-），女，硕士研究生，主要研究方向为膜分离，籍贯河南。联系人 李磊,博士,副教授,主要从事膜分离技术研究。电话025-83596665;E-mail ll-nju@163.com；地址 江苏省南京市汉口路22号南京大学化工系 |
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参考文献： |
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