Properties and separation performance of Ge-ZSM-5 membranes

被引:108
作者
Li, S [1 ]
Tuan, VA [1 ]
Falconer, JL [1 ]
Noble, RD [1 ]
机构
[1] Univ Colorado, Dept Chem Engn, Eng Ctr ECCH 111, Boulder, CO 80309 USA
关键词
inorganic membranes; ZSM-5; zeolite; gas permeation; organic separation; pervaporation;
D O I
10.1016/S1387-1811(02)00612-1
中图分类号
O69 [应用化学];
学科分类号
081704 ;
摘要
Germanium-substituted ZSM-5 zeolite membranes with various Si/Ge ratios were synthesized by in situ crystallization on porous tubular stainless steel and alpha-Al2O3 supports. For a Si/Ge ratio in the synthesis gel,of 25, the Si/Ge ratio in the membrane was 41-82, depending on the support. When the Si/Ge ratio was 5, extra framework compounds that contained Ge formed. The fraction of permeation through non-zeolite pores increased as the Si/Ge ratio decreased. The Ge-ZSM-5 membranes were effective for separating acetone from water by pervaporation. The highest acetone/ water selectivity of 330 (at 323 K) and the highest total flux of 0.95 kg/m(2) h (at 333 K) were obtained for a membrane with a Si/Ge ratio of 41. This membrane selectively removed alcohols, ketones, carboxylic acids, esters, and propionaldehyde from 5 wt.% aqueous solutions because the organics preferentially adsorbed. The C-3 organics showed higher organic/water selectivities than C-2 or C-4 organics with the same functional group. The organic/water separation selectivity increased as the liquid-phase fugacity of the organic in the feed increased. (C) 2002 Published by Elsevier Science Inc.
引用
收藏
页码:137 / 154
页数:18
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