Solubility-based gas separation with oligomer-modified inorganic membranes

被引:62
作者
Javaid, A
Hughey, MP
Varutbangkul, V
Ford, DM [1 ]
机构
[1] Texas A&M Univ, Dept Chem Engn, College Stn, TX 77843 USA
[2] Stanford Univ, Dept Chem Engn, Stanford, CA 94305 USA
基金
美国国家科学基金会;
关键词
ceramic membranes; gas and vapor permeation; gas separations; microporous and porous membranes; organic separations;
D O I
10.1016/S0376-7388(01)00341-6
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
The potential of hybrid organic-inorganic membranes for separating organic molecules from air, based on a solubility-selective mechanism, was evaluated. Alumina membranes with average pore sizes near 5 and 12 nm were surface-derivatized with various alkyl trichlorosilanes, and their permeances to nitrogen, methane, and propane gases were evaluated at feed pressures up to 2 bar. The permeation rates in the modified membranes generally decreased by two to three orders of magnitude compared with the untreated membranes, while the propane/nitrogen selectivity increased significantly. The membrane performance was correlated with the materials and synthesis conditions employed in the modification, which indicated an ability to control the hydrophobic character and free volume of the hybrids. The maximum propane/nitrogen selectivity observed was 32, which compares very favorably to the best results reported for purely polymeric membranes. This study demonstrates that the synthesis of hybrid membranes with tunable free volume and surface chemistry is feasible, and that such membranes may achieve high performance in solubility-based separations. (C) 2001 Elsevier Science B.V. All rights reserved.
引用
收藏
页码:141 / 150
页数:10
相关论文
共 26 条
[1]  
BAKER RW, 1987, J MEMBRANE SCI, V31, P259, DOI 10.1016/S0376-7388(00)82232-2
[2]   THE MOLECULAR MECHANISM OF RETENTION IN REVERSED-PHASE LIQUID-CHROMATOGRAPHY [J].
DORSEY, JG ;
DILL, KA .
CHEMICAL REVIEWS, 1989, 89 (02) :331-346
[3]  
Freeman B, 1997, TRENDS POLYM SCI, V5, P167
[4]   Recovery of volatile organic solvent compounds from air by ceramic membranes [J].
Huang, P ;
Xu, NP ;
Shi, J ;
Lin, YS .
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 1997, 36 (09) :3815-3820
[5]  
Karger J., 1992, Diffusion in zeolites and other microporous solids
[6]   MEMBRANE-BASED GAS SEPARATION [J].
KOROS, WJ ;
FLEMING, GK .
JOURNAL OF MEMBRANE SCIENCE, 1993, 83 (01) :1-80
[7]   Vapour permeation for the recovery of organic solvents from waste air streams: Separation capacities and process optimization [J].
Leemann, M ;
Eigenberger, G ;
STrathmann, H .
JOURNAL OF MEMBRANE SCIENCE, 1996, 113 (02) :313-322
[8]   Preparation and properties of surface modified ceramic membranes .2. Gas and liquid permeabilities of 5 nm alumina membranes modified by a monolayer of bound polydimethylsiloxane (PDMS) silicone oil [J].
Leger, C ;
Lira, HD ;
Paterson, R .
JOURNAL OF MEMBRANE SCIENCE, 1996, 120 (01) :135-146
[9]   Preparation and properties of surface modified ceramic membranes .3. Gas permeation of 5 nm alumina membranes modified by trichloro-octadecylsilane [J].
Leger, C ;
Lira, HD ;
Paterson, R .
JOURNAL OF MEMBRANE SCIENCE, 1996, 120 (02) :187-195
[10]   THE FORMATION OF CHEMICALLY MODIFIED GAMMA-ALUMINA MICROPOROUS MEMBRANES [J].
MILLER, JR ;
KOROS, WJ .
SEPARATION SCIENCE AND TECHNOLOGY, 1990, 25 (13-15) :1257-1280