Hydrogen separation in H2-H2O-HI gaseous mixture using the silica membrane prepared by chemical vapor deposition

被引:59
作者
Hwang, GJ
Onuki, K
Shimizu, S
Ohya, H
机构
[1] Japan Atom Energy Res Inst, Dept Adv Nucl Heat Technol, Tokai, Ibaraki 3191195, Japan
[2] Yokohama Natl Univ, Dept Mat Sci & Chem Engn, Hodogaya Gu, Yokohama, Kanagawa 2408501, Japan
关键词
inorganic membranes; silica-alumina membranes; chemical vapor deposition; gas separations; hydrogen permselectivity;
D O I
10.1016/S0376-7388(99)00125-8
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
Hydrogen separation in H-2-H2O-HI gaseous mixture using the silica membrane prepared by CVD was evaluated aiming at the application for hydrogen iodide decomposition in the thermochemical IS process. Porous alumina tubes having pore size of 100 nm (M1) and 10 nm (M2) were modified by chemical vapor deposition using tetraethoxysilane as the Si source. Single-component permeance to He, H-2, and N-2 was measured at 300-600 degrees C. Hydrogen permeance of the modified membranes at a permeation temperature of 600 degrees C was about 6 x 10(-9) mol/Pa m(2) s. H-2/N-2 selectivities at 600 degrees C were 5.2 and 160 for M1 and M2 membrane, respectively. Separation experiments of a H-2-H2O-HI mixture using the modified membranes were carried out at 300-600 degrees C. Hydrogen permeances were almost the same as the single-component permeances, whereas HI permeances were below 1 x 10(-11) mol/Pa m(2) s. The hydrogen permeances were not changed after one day exposure in a mixture of H-2-H2O-HI with a molar composition of 0.23:0.65:0.12 at 450 degrees C. (C) 1999 Elsevier Science B.V. All rights reserved.
引用
收藏
页码:83 / 90
页数:8
相关论文
共 16 条
[1]   DEPOSITION OF H-2-PERMSELECTIVE SIO2-FILMS [J].
GAVALAS, GR ;
MEGIRIS, CE ;
NAM, SW .
CHEMICAL ENGINEERING SCIENCE, 1989, 44 (09) :1829-1835
[2]   CHEMICAL-VAPOR-DEPOSITION OF HYDROGEN-PERMSELECTIVE SILICA FILMS ON POROUS-GLASS SUPPORTS FROM TETRAETHYLORTHOSILICATE [J].
HA, HY ;
NAM, SW ;
HONG, SA ;
LEE, WK .
JOURNAL OF MEMBRANE SCIENCE, 1993, 85 (03) :279-290
[3]   PREPARATION OF H-2 PERMSELECTIVE SILICA MEMBRANES BY ALTERNATING REACTANT VAPOR-DEPOSITION [J].
KIM, SJ ;
GAVALAS, GR .
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 1995, 34 (01) :168-176
[4]   SYNTHESIS OF H2-PERMSELECTIVE MEMBRANES BY MODIFIED CHEMICAL VAPOR-DEPOSITION - MICROSTRUCTURE AND PERMSELECTIVITY OF SIO2/C/VYCOR MEMBRANES [J].
MEGIRIS, CE ;
GLEZER, JHE .
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 1992, 31 (05) :1293-1299
[5]   Separation of hydrogen from an H-2-H2O-HBr system with an SiO2 membrane formed in macropores of an alpha-alumina support tube [J].
Morooka, S ;
Kim, SS ;
Yan, S ;
Kusakabe, K ;
Watanabe, M .
INTERNATIONAL JOURNAL OF HYDROGEN ENERGY, 1996, 21 (03) :183-188
[6]   Closed-cycle continuous hydrogen production test by thermochemical IS process [J].
Nakajima, H ;
Ikenoya, K ;
Onuki, K ;
Shimizu, S .
KAGAKU KOGAKU RONBUNSHU, 1998, 24 (02) :352-355
[7]  
Norman JH, 1981, GRI800105
[8]  
ONUKI K, 1997, P 8 INT TOP M NUCL R, P1803
[9]   TEST OF ONE-LOOP FLOW SCHEME FOR THE UT-3 THERMOCHEMICAL HYDROGEN-PRODUCTION PROCESS [J].
SAKURAI, M ;
AIHARA, M ;
MIYAKE, N ;
TSUTSUMI, A ;
YOSHIDA, K .
INTERNATIONAL JOURNAL OF HYDROGEN ENERGY, 1992, 17 (08) :587-592
[10]   Pore size control and gas permeation kinetics of silica membranes by pyrolysis of phenyl-substituted ethoxysilanes with cross-flow through a porous support wall [J].
Sea, BK ;
Kusakabe, K ;
Morooka, S .
JOURNAL OF MEMBRANE SCIENCE, 1997, 130 (1-2) :41-52