Hydrogen permeability of 2.5 μm palladium-silver membranes deposited on ceramic supports

被引:63
作者
Pizzi, Diego [1 ]
Worth, Ryan [1 ]
Baschetti, Marco Giacinti [1 ]
Sarti, Giulio C. [1 ]
Noda, Ken-ichi [2 ]
机构
[1] Univ Bologna, Alma Mat Studiorum, Dipartimento Ingn Chim Mineraria & Tecnol Ambient, I-40131 Bologna, Italy
[2] NGK Insulators Ltd, Mizuho Ku, Nagoya, Aichi 4678530, Japan
关键词
Hydrogen permeation; Palladium-silver membrane; Ceramic support; Concentration polarization;
D O I
10.1016/j.memsci.2008.08.020
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
The permeability of hydrogen selective Pd-based membranes was tested in different experimental conditions. The membranes were obtained by depositing palladium-silver films onto ceramic porous supports, with film composition of about 20 wt% of silver and thicknesses of about 2.5 mu m. Their permeance was measured at 400 C at total trans-membrane pressures between 0.2 and 6 bar, using pure feeds of H-2 and N-2, as well as H-2/N-2 and H-2/CO mixtures; the temperature dependence of permeability was investigated using pure H2 feeds at 300, 400 and 500 degrees C. The membranes exhibit a very attractive behavior, maintaining a virtually infinite selectivity throughout the testing, with permeance values among the highest values reported in literature for similar membranes. Permeation of pure hydrogen accurately follows Sieverts' law and confirms the presence of a chemisorption-dissociation-diffusion mechanism, characterised by the transport of atomic hydrogen through the Pd-Ag layer as the limiting step. In the case of H-2/N-2 mixtures, the high membrane permeance originates also significant concentration polarization phenomena resulting in apparent deviations from Sieverts' behavior; the presence of CO in the feed may reduce hydrogen permeability even by 75%, although this effect is shown to be fully reversible after a subsequent air treatment at 400 degrees C. The temperature dependence of the membrane permeability is of Arrhenius type, with an activation energy of about 17 kJ/mol, that is, close to what is reported for Pd-Ag membranes following Sieverts' behavior. (c) 2008 Elsevier B.V. All rights reserved.
引用
收藏
页码:446 / 453
页数:8
相关论文
共 43 条
[1]   Hydrogen permeation through surface modified Pd and PdAg membranes [J].
Amandusson, H ;
Ekedahl, LG ;
Dannetun, H .
JOURNAL OF MEMBRANE SCIENCE, 2001, 193 (01) :35-47
[2]   The effect of CO and O2 on hydrogen permeation through a palladium membrane [J].
Amandusson, H ;
Ekedahl, LG ;
Dannetun, H .
APPLIED SURFACE SCIENCE, 2000, 153 (04) :259-267
[3]   CATALYSIS WITH PERMSELECTIVE INORGANIC MEMBRANES [J].
ARMOR, JN .
APPLIED CATALYSIS, 1989, 49 (01) :1-25
[4]   The partial oxidation of methane to syngas in a palladium membrane reactor:: simulation and experimental studies [J].
Basile, A ;
Paturzo, L ;
Laganà, F .
CATALYSIS TODAY, 2001, 67 (1-3) :65-75
[5]  
Bird R B., 2002, Transportphenomena
[6]   High-temperature membranes in power generation with CO2 capture [J].
Bredesen, R ;
Jordal, K ;
Bolland, O .
CHEMICAL ENGINEERING AND PROCESSING-PROCESS INTENSIFICATION, 2004, 43 (09) :1129-1158
[7]   Palladium membranes prepared by r.f. magnetron sputtering for hydrogen purification [J].
Checchetto, R ;
Bazzanella, N ;
Patton, B ;
Miotello, A .
SURFACE & COATINGS TECHNOLOGY, 2004, 177 :73-79
[8]   Performance of alumina, zeolite, palladium, Pd-Ag alloy membranes for hydrogen separation from Towngas mixture [J].
Cheng, YS ;
Peña, MA ;
Fierro, JL ;
Hui, DCW ;
Yeung, KL .
JOURNAL OF MEMBRANE SCIENCE, 2002, 204 (1-2) :329-340
[9]   Palladium-silver composite membranes by electroless plating technique [J].
Cheng, YS ;
Yeung, KL .
JOURNAL OF MEMBRANE SCIENCE, 1999, 158 (1-2) :127-141
[10]   Catalysis in membrane reformers: a high-performance catalytic system for hydrogen production from methane [J].
Ferreira-Aparicio, P ;
Benito, M ;
Kouachi, K ;
Menad, S .
JOURNAL OF CATALYSIS, 2005, 231 (02) :331-343