Transport properties of alumina-supported MFI membranes made by secondary (seeded) growth

被引:162
作者
Xomeritakis, G [1 ]
Nair, S [1 ]
Tsapatsis, M [1 ]
机构
[1] Univ Massachusetts, Dept Chem Engn, Goessmann Lab 159, Amherst, MA 01003 USA
基金
美国国家科学基金会;
关键词
inorganic membrane; zeolite membrane; zeolite MFI; gas and vapor permeation; xylene separation;
D O I
10.1016/S1387-1811(99)00300-5
中图分类号
O69 [应用化学];
学科分类号
081704 ;
摘要
Zeolite MFI membranes with thicknesses in the range of 1-40 mu m have been prepared by hydrothermal growth of colloidal silicalite-l seed crystals of particle sizes similar to 100 nm deposited on the surface of alpha-Al2O3 porous support disks. These membranes exhibit attractive separation characteristics as judged by permeation measurements with butane and xylene isomers. At 22 degrees C, the permeation flux of n-butane and the n-butane/isobutane ratio from 50 kPa/50 kPa binary mixtures vary in the range of 1.0-4.0 mmol m(-2) s(-1) and 30-70, respectively. The n-butane flux exhibited a dependence on temperature and feed partial pressure consistent with activated diffusion of an adsorbed phase obeying Langmuir isotherm but was rather insensitive to the membrane thickness. For the best membranes, the single-component p-xylene flux and the p-xylene/o-xylene flux ratio at 100 degrees C was in the range of 10-30 mu mol m(-2) s(-1) and 30-130, respectively. The permeation flux of o-xylene increases dramatically in the presence of p-xylene resulting in a substantial loss in para/ortho selectivity (maximum of similar to 5), an effect that may be attributed to the flexibility of the MFI framework in the presence of molecules with a close fit to its framework. At 100 degrees C para/ortho selectivities (>20) are observed when the p-xylene feed partial pressure is below 0.05 kPa. (C) 2000 Elsevier Science B.V. All rights reserved.
引用
收藏
页码:61 / 73
页数:13
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