The effects of polymer chain rigidification, zeolite pore size and pore blockage on polyethersulfone (PES)-zeolite A mixed matrix membranes

被引:314
作者
Li, Y
Chung, TS
Cao, C
Kulprathipanja, S
机构
[1] Natl Univ Singapore, Dept Chem & Biomol Engn, Singapore 119260, Singapore
[2] U0P LLC, Des Plaines, IL 60017 USA
关键词
mixed matrix membrane; gas separation performance; polymer chain rigidification; partial pore blockage; Maxwell model;
D O I
10.1016/j.memsci.2005.03.019
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
The polyethersulfone (PES)-zeolite 3A, 4A and 5A mixed matrix membranes (MMMs) were fabricated with a modified solution-casting procedure at high temperatures close to the glass transition temperatures (T-g) of polymer materials. The effects of membrane preparation methodology, zeolite loading and pore size of zeolite on the gas separation performance of these mixed matrix membranes were studied. SEM results show the interface between polymer and zeolite in MMMs experiencing natural cooling is better (i.e., less defective) than that in MMMs experiencing immediate quenching. The increment of glass transition temperature (T-g) of MMMs with zeolite loading confirms the polymer chain rigidification induced by zeolite. The experimental results indicate that a higher zeolite loading results in a decrease in gas permeability and an increase in gas pair selectivity. The unmodified Maxwell model fails to correctly predict the permeability decrease induced by polymer chain rigidification near the zeolite surface and the partial pore blockage of zeolites by the polymer chains. A new modified Maxwell model is therefore proposed. It takes the combined effects of chain rigidification and partial pore blockage of zeolites into calculation. The new model shows much consistent permeability and selectivity predication with experimental data. Surprisingly, an increase in zeolite pore size from 3 to 5 A generally not only increase gas permeability, but also gas pair selectivity. The O-2/N-2 selectivity of PES-zeolite 3A and PES-zeolite 4A membranes is very similar, while the O-2/N-2 Selectivity of PES-zeolite 5A membranes is much higher. This implies the blockage may narrow a part of zeolite 5A pores to approximately 4 angstrom, which can discriminate the gas pair of O-2 and N-2 and narrow a part of zeolites 3A and 4A pores to smaller sizes. It is concluded that the partial pore blockage of zeolites by the polymer chains has equivalent or more influence on the separation properties of mixed matrix membranes compared with that of the polymer chain rigidification. (c) 2005 Elsevier B.V. All rights reserved.
引用
收藏
页码:45 / 55
页数:11
相关论文
共 29 条
[1]   Scaling of differentiation in networks: Nervous systems, organisms, ant colonies, ecosystems, businesses, universities, cities, electronic circuits, and legos [J].
Changizi, MA ;
McDannald, MA ;
Widders, D .
JOURNAL OF THEORETICAL BIOLOGY, 2002, 218 (02) :215-237
[2]   GAS PERMEATION IN POLYETHERSULFONE [J].
CHIOU, JS ;
MAEDA, Y ;
PAUL, DR .
JOURNAL OF APPLIED POLYMER SCIENCE, 1987, 33 (05) :1823-1828
[3]  
Dolveck J.Y., 1992, MATER SCI FORUM, V105-110, P1549
[4]   ADSORBENT FILLED MEMBRANES FOR GAS SEPARATION .1. IMPROVEMENT OF THE GAS SEPARATION PROPERTIES OF POLYMERIC MEMBRANES BY INCORPORATION OF MICROPOROUS ADSORBENTS [J].
DUVAL, JM ;
FOLKERS, B ;
MULDER, MHV ;
DESGRANDCHAMPS, G ;
SMOLDERS, CA .
JOURNAL OF MEMBRANE SCIENCE, 1993, 80 (1-3) :189-198
[5]   PREPARATION OF ZEOLITE FILLED GLASSY POLYMER MEMBRANES [J].
DUVAL, JM ;
KEMPERMAN, AJB ;
FOLKERS, B ;
MULDER, MHV ;
DESGRANDCHAMPS, G ;
SMOLDERS, CA .
JOURNAL OF APPLIED POLYMER SCIENCE, 1994, 54 (04) :409-418
[6]   A NEW MULTIPLET-CLUSTER MODEL FOR THE MORPHOLOGY OF RANDOM IONOMERS [J].
EISENBERG, A ;
HIRD, B ;
MOORE, RB .
MACROMOLECULES, 1990, 23 (18) :4098-4107
[7]  
ERDEMSENATALAR A, 2001, P 13 INT ZEOL C MONT
[8]   MOLECULAR-SIEVING EFFECT OF THE ZEOLITE-FILLED SILICONE-RUBBER MEMBRANES IN GAS PERMEATION [J].
JIA, MD ;
PEINEMANN, KV ;
BEHLING, RD .
JOURNAL OF MEMBRANE SCIENCE, 1991, 57 (2-3) :289-296
[9]  
JIANG LY, UNPUB PREPARATION CH
[10]  
KAZUO H, 1987, Patent No. 62019206