Matrimid®/MgO mixed matrix membranes for pervaporation

被引:81
作者
Jiang, Lan Ying [1 ]
Chung, Tai-Shung [1 ]
Rajagopalan, Raj [1 ]
机构
[1] Natl Univ Singapore, Dept Chem & Biomol Engn, Singapore 119260, Singapore
关键词
mixed matrix membrane (MMM); magnesium oxide (MgO); pervaporation; dehydration; iso-propanol; WATER-ISOPROPANOL MIXTURES; CO-POLYIMIDE MEMBRANES; COMPOSITE MEMBRANES; SODIUM ALGINATE; ALCOHOL MIXTURES; SEPARATION; ZEOLITE; DEHYDRATION; CHITOSAN; ULTRAFILTRATION;
D O I
10.1002/aic.11198
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
For the first time, porous Magnesium oxide (MgO) particles have been applied to generate mixed matrix membranes (MMM) for the dehydration of iso-propanol by pervaporation. A modified membrane fabrication procedure has been developed to prepare membranes with higher separation efficiency. FESEM and DSC characterizations confirm that the MMMs produced have intimate polymer/particle interface; the nano-size crystallites on MgO surface may interfere with the polymer chain packing and induce chains rigidification upon the particle surface. It is observed that Matrimid (R)/ MgO MMMs generally have higher selectivity, but lower permeability relative to the neat Matrimid (R) dense membrane. The highest selectivity is obtained with MMM containing 15 wt. % MgO. The selective sorption and diffusion of water in the MgO particles, and the polymer/particle interface properties combine to lead to the earlier phenomena. The investigation on the effect of feed water composition on the pervaporation performance reveals that the addition of MgO can show the selectivity-enhancing effects if the feed water concentration is lower than 30 wt. %. In the dehydration of isopropanol aqueous solution with 10 wt. % water, the selectivity of the MMMs is around 2,000, which is more than twice of 900 of neat polymeric membrane. This makes MMMs extremely suitable for breaking the azeotrops of water/iso-propanol. Gas permeation tests are also conducted using O-2 and N-2 to determine the microscopic structure of the MMMs, and to investigate the relationship between pervaporation and gas separation performance. (c) 2007 American Institute of Chemical Engineers.
引用
收藏
页码:1745 / 1757
页数:13
相关论文
共 46 条
[41]   Structure of N-alkyl chitosan membranes on water-permselectivity for aqueous ethanol solutions [J].
Uragami, T ;
Kato, S ;
Miyata, T .
JOURNAL OF MEMBRANE SCIENCE, 1997, 124 (02) :203-211
[42]   A novel composite chitosan membrane for the separation of alcohol-water mixtures [J].
Wang, XP ;
Shen, ZQ ;
Zhang, FY ;
Zhang, YF .
JOURNAL OF MEMBRANE SCIENCE, 1996, 119 (02) :191-198
[43]  
WIJAMS JG, 2003, J MEMBRANE SCI, V220, P1
[44]  
WIJAMS JG, 1993, J MEMBRANE SCI, V79, P101
[45]   PREPARATION OF ASYMMETRIC POLYIMIDE MEMBRANE FOR WATER-ETHANOL SEPARATION IN PERVAPORATIN BY THE PHASE INVERSION PROCESS [J].
YANAGISHITA, H ;
MAEJIMA, C ;
KITAMOTO, D ;
NAKANE, T .
JOURNAL OF MEMBRANE SCIENCE, 1994, 86 (03) :231-240
[46]   Zeolite-filled polyimide membrane containing 2,4,6-triaminopyrimidine [J].
Yong, HH ;
Park, NC ;
Kang, YS ;
Won, J ;
Kim, WN .
JOURNAL OF MEMBRANE SCIENCE, 2001, 188 (02) :151-163