Selective permeation and separation of steam from water–methanol–hydrogen gas mixtures through mordenite membrane
Separation properties of a mordenite membrane for water–methanol–hydrogen mixtures were studied in the temperature range from 423 to 523 K under pressurized conditions. The mordenite membrane was prepared on the outer surface of a porous alumina tubular support by a secondary-growth method. It was f...
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Published in | Catalysis today Vol. 132; no. 1; pp. 182 - 187 |
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Main Authors | , , , , , |
Format | Journal Article Conference Proceeding |
Language | English |
Published |
Amsterdam
Elsevier B.V
01.03.2008
Elsevier Science |
Subjects | |
Online Access | Get full text |
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Summary: | Separation properties of a mordenite membrane for water–methanol–hydrogen mixtures were studied in the temperature range from 423 to 523
K under pressurized conditions. The mordenite membrane was prepared on the outer surface of a porous alumina tubular support by a secondary-growth method. It was found that water was selectively permeated through the membrane. The separation factor of water/hydrogen and water/methanol were 49–156 and 73–101, respectively. Even when only hydrogen was fed at 0.5
MPa, its permeance was as low as 10
−9
mol
m
−2
s
−1
Pa
−1 up to 493
K, possibly suggesting that water pre-adsorbed in the micropores of mordenite hindered the permeation of hydrogen. The hydrogen permeance dramatically increased to 6.5
×
10
−7
mol
m
−2
s
−1
Pa
−1 at 503
K and reached to 1.4
×
10
−6
mol
m
−2
s
−1
Pa
−1 at 523
K because of the formation of cracks in the membrane. However, the membrane was thermally stabilized in the presence of steam and/or methanol. |
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ISSN: | 0920-5861 1873-4308 |
DOI: | 10.1016/j.cattod.2007.12.005 |