High-flux palladium-silver alloy membranes fabricated by microsystem technology

被引:21
作者
Gielens, FC
Tong, HD
van Rijn, CJM
Vorstman, MAG
Keurentjes, JTF
机构
[1] Eindhoven Univ Technol, Dept Chem Engn & Chem, Proc Dev Grp, NL-5600 MB Eindhoven, Netherlands
[2] Univ Twente, MESA, NL-7500 AE Enschede, Netherlands
[3] Univ Twente, Inst Res, NL-7500 AE Enschede, Netherlands
[4] Aquamarijn Micro Filtrat BV, NL-7255 DB Hengelo, Netherlands
关键词
hydrogen permeation; palladium alloys; microsieve; micro-membrane; micro-reactor;
D O I
10.1016/S0011-9164(02)00637-9
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
In this study, hydrogen selective membranes have been fabricated using microsystem technology. A 750 nm dense layer of Pd (77 wt%) and Ag (23 wt%) is deposited on a non-porous 1 mm thick silicon nitride layer by cosputtering of a Pd and a Ag target. After sputtering, openings of 5 gm are made in the silicon nitride layer to create a clear passage to the Pd/Ag surface. As a result of the production method, these membranes are pinhole free and have a low resistance to mass transfer in the gas phase, as virtually no support layer is present. The membranes have been tested in a gas permeation system to determine the hydrogen permeability as a function of temperature, gas flow rate, and feed composition. In addition, the hydrogen selectivity over helium has been determined, which appears to be above 1500. At 0.2 bar partial hydrogen pressure in the feed, the hydrogen permeability of the membranes has been found to range from 0.02 to 0.95 mol.H-2/m(2)xs at 350 and 450degreesC, respectively. It is expected that by improving the hydrodynamics and increasing the operation temperature, substantially higher fluxes will be attainable.
引用
收藏
页码:417 / 423
页数:7
相关论文
共 19 条
[1]   Catalytic dehydrogenation of propane in hydrogen permselective membrane reactors [J].
Collins, JP ;
Schwartz, RW ;
Sehgal, R ;
Ward, TL ;
Brinker, CJ ;
Hagen, GP ;
Udovich, CA .
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 1996, 35 (12) :4398-4405
[2]   Membrane reactors for hydrogenation and dehydrogenation processes based on supported palladium [J].
Dittmeyer, R ;
Höllein, V ;
Daub, K .
JOURNAL OF MOLECULAR CATALYSIS A-CHEMICAL, 2001, 173 (1-2) :135-184
[3]  
Franz AJ, 2000, MICROREACTION TECHNOLOGY: INDUSTRIAL PROSPECTS, P267
[4]   Reaction assisted hydrogen transport during catalytic dehydrogenation in a membrane reactor [J].
Gobina, E ;
Hughes, R .
APPLIED CATALYSIS A-GENERAL, 1996, 137 (01) :119-127
[5]   The effect of direction of hydrogen permeation on the rate through a composite palladium membrane [J].
Goto, S ;
Assabumrungrat, S ;
Tagawa, T ;
Praserthdam, P .
JOURNAL OF MEMBRANE SCIENCE, 2000, 175 (01) :19-24
[6]   SURFACE-COMPOSITION OF PD-AG ALLOYS [J].
KUIJERS, FJ ;
PONEC, V .
JOURNAL OF CATALYSIS, 1979, 60 (01) :100-109
[7]   Fabrication of dense palladium composite membranes for hydrogen separation [J].
Li, AW ;
Liang, WQ ;
Hughes, R .
CATALYSIS TODAY, 2000, 56 (1-3) :45-51
[8]   Composition control and hydrogen permeation characteristics of sputter deposited palladium-silver membranes [J].
McCool, B ;
Xomeritakis, G ;
Lin, YS .
JOURNAL OF MEMBRANE SCIENCE, 1999, 161 (1-2) :67-76
[9]   A study on the palladium/nickel composite membrane by vacuum electrodeposition [J].
Nam, SE ;
Lee, KH .
JOURNAL OF MEMBRANE SCIENCE, 2000, 170 (01) :91-99
[10]   Thin dense Pd membranes supported on α-Al2O3 hollow fibers [J].
Pan, XL ;
Xiong, GX ;
Sheng, SS ;
Stroh, N ;
Brunner, H .
CHEMICAL COMMUNICATIONS, 2001, (24) :2536-2537