Abstract
A mordenite membrane was prepared on the outer surface of a porous α-alumina tubular support by a secondary-growth method. Permeation tests for water/methanol/hydrogen mixtures were performed at 423 and 473 K. A mordenite membrane free from non-zeolitic pores allowed us selective permeation of steam and blocked the permeation of hydrogen and methanol. In order to elucidate the mechanism of such selective permeation behavior, adsorption, permeation, and structural properties of the mordenite membrane were discussed. As a result, it was considered that selective permeation of steam against hydrogen was based on its preferential adsorption of steam, while boundaries between mordenite crystals in the membrane may play a key role for inhibiting the permeation of methanol.
| Original language | English |
|---|---|
| Pages (from-to) | 870-877 |
| Number of pages | 8 |
| Journal | Journal of Chemical Engineering of Japan |
| Volume | 41 |
| Issue number | 9 |
| DOIs | |
| Publication status | Published - 2008 |
Fingerprint
Keywords
- Mordenite
- Separation
- Zeolite membrane
ASJC Scopus subject areas
- Chemical Engineering(all)
- Chemistry(all)
Cite this
Separation behavior of steam from hydrogen and methanol through mordenite membrane. / Sawamura, Ken Ichi; Shirai, Tsutomu; Ohsuna, Tetsu; Hagino, Takayuki; Takada, Mitsuko; Sekine, Yasushi; Kikuchi, Eiichi; Matsukata, Masahiko.
In: Journal of Chemical Engineering of Japan, Vol. 41, No. 9, 2008, p. 870-877.Research output: Contribution to journal › Article
}
TY - JOUR
T1 - Separation behavior of steam from hydrogen and methanol through mordenite membrane
AU - Sawamura, Ken Ichi
AU - Shirai, Tsutomu
AU - Ohsuna, Tetsu
AU - Hagino, Takayuki
AU - Takada, Mitsuko
AU - Sekine, Yasushi
AU - Kikuchi, Eiichi
AU - Matsukata, Masahiko
PY - 2008
Y1 - 2008
N2 - A mordenite membrane was prepared on the outer surface of a porous α-alumina tubular support by a secondary-growth method. Permeation tests for water/methanol/hydrogen mixtures were performed at 423 and 473 K. A mordenite membrane free from non-zeolitic pores allowed us selective permeation of steam and blocked the permeation of hydrogen and methanol. In order to elucidate the mechanism of such selective permeation behavior, adsorption, permeation, and structural properties of the mordenite membrane were discussed. As a result, it was considered that selective permeation of steam against hydrogen was based on its preferential adsorption of steam, while boundaries between mordenite crystals in the membrane may play a key role for inhibiting the permeation of methanol.
AB - A mordenite membrane was prepared on the outer surface of a porous α-alumina tubular support by a secondary-growth method. Permeation tests for water/methanol/hydrogen mixtures were performed at 423 and 473 K. A mordenite membrane free from non-zeolitic pores allowed us selective permeation of steam and blocked the permeation of hydrogen and methanol. In order to elucidate the mechanism of such selective permeation behavior, adsorption, permeation, and structural properties of the mordenite membrane were discussed. As a result, it was considered that selective permeation of steam against hydrogen was based on its preferential adsorption of steam, while boundaries between mordenite crystals in the membrane may play a key role for inhibiting the permeation of methanol.
KW - Mordenite
KW - Separation
KW - Zeolite membrane
UR - http://www.scopus.com/inward/record.url?scp=52649138417&partnerID=8YFLogxK
UR - http://www.scopus.com/inward/citedby.url?scp=52649138417&partnerID=8YFLogxK
U2 - 10.1252/jcej.07WE312
DO - 10.1252/jcej.07WE312
M3 - Article
VL - 41
SP - 870
EP - 877
JO - Journal of Chemical Engineering of Japan
JF - Journal of Chemical Engineering of Japan
SN - 0021-9592
IS - 9
ER -