Abstract
Process improvements in silica membrane fabrication, especially the use of clean-room techniques, resulted in silica membranes without detectable mesoscopic defects, resulting in significantly improved transport properties. Supported membranes calcined at 400°C were 30 nanometers in thickness, showed a H 2 permeance at 200°C of 2 × 10 −6 moles per square meter per second per Pascal (mol m −2 s −1 Pa −1 ), and had a CH 4 permeance more than 500 times smaller. Molecules larger than CH 4 were completely blocked. Silica membranes calcined at 600°C showed no detectable CH 4 flux, with a H 2 permeance of 5 × 10 −7 (mol m −2 s −1 Pa −1 ) at 200°C. These results signify an important step toward the industrial application of these membranes such as purification of H 2 and natural gas as well as the selective removal of CO 2 .
References
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Dates
Type | When |
---|---|
Created | 23 years, 1 month ago (July 27, 2002, 5:42 a.m.) |
Deposited | 1 year, 7 months ago (Jan. 13, 2024, 1:06 a.m.) |
Indexed | 1 month ago (July 28, 2025, 5:31 p.m.) |
Issued | 27 years, 5 months ago (March 13, 1998) |
Published | 27 years, 5 months ago (March 13, 1998) |
Published Print | 27 years, 5 months ago (March 13, 1998) |
@article{de_Vos_1998, title={High-Selectivity, High-Flux Silica Membranes for Gas Separation}, volume={279}, ISSN={1095-9203}, url={http://dx.doi.org/10.1126/science.279.5357.1710}, DOI={10.1126/science.279.5357.1710}, number={5357}, journal={Science}, publisher={American Association for the Advancement of Science (AAAS)}, author={de Vos, Renate M. and Verweij, Henk}, year={1998}, month=mar, pages={1710–1711} }