Electroless plating synthesis, characterization and permeation properties of Pd-Cu membranes supported on ZrO2 modified porous stainless steel

被引:100
作者
Gao, HY
Lin, JYS [1 ]
Li, YD
Zhang, BQ
机构
[1] Tianjin Univ, Sch Chem Engn, Dept Catalysis Sci & Technol, Tianjin 300072, Peoples R China
[2] Univ Cincinnati, Dept Chem & Mat Engn, Cincinnati, OH 45221 USA
[3] Arizona State Univ, Dept Chem & Mat Engn, Tempe, AZ 85287 USA
[4] Hebei Polytech Univ, Sch Chem & Biol Technol, Dept Appl Chem, Tangshan 063009, Peoples R China
基金
中国国家自然科学基金;
关键词
Pd-Cu alloy composite membrane; porous stainless steel; zirconia; hydrogen permeation; membrane preparation;
D O I
10.1016/j.memsci.2005.04.050
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
Thin Pd-Cu membranes were prepared by electroless plating technique on porous stainless steel (PSS) disks coated with a mesoporous palladium impregnated zirconia intermediate layer. This intermediate layer provides seeds for electroless plating growth of Pd-Cu film during synthesis and serves as an inter-metallic diffusion barrier that improves membrane stability for practical application. XPS analyses showed that the average surface compositions of the two membranes were respectively Pd84CU16 and Pd46Cu54 (at.%). XRD analyses indicated that deposited Pd84CU16 alloy film contained only alpha-fcc (face-centred cubic) phase structure whereas Pd46Cu54 alloy film contained a mixture of alpha-fcc and beta-bcc phases. The 10 mu m thick Pd46Cu54/ZrO2-PSS membrane exhibited an infinite separation factor for H-2 over N-2, with H-2 permeance of 1.1 x 10(-7) mol/m(2) s Pa at 753 K. The activation energies for hydrogen permeation and hydrogen pressure exponents are respectively 14.5 kJ/mol and 0.6 for Pd84Cu16/ZrO2-PSS membrane and 15.4 kJ/mol and I for Pd46Cu54/ZrO2-PSS composite membrane. The different permeation properties for the two membranes are discussed in terms of different permeation mechanisms associated with membrane thickness, structure, surface composition and morphology. (c) 2005 Elsevier B.V. All rights reserved.
引用
收藏
页码:142 / 152
页数:11
相关论文
共 64 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]  
*ASM, 1973, MET HDB, V8, P296
[3]   INVESTIGATIONS OF THE SELECTIVE-POPULATION OF HYDROGEN SUBSURFACE SITES ON PD(110) USING HE DIFFRACTION AND THERMAL-DESORPTION SPECTROSCOPY [J].
BAUMBERGER, M ;
STOCKER, W ;
RIEDER, KH .
APPLIED PHYSICS A-MATERIALS SCIENCE & PROCESSING, 1986, 41 (02) :151-156
[4]  
BRIGGS D, 1983, PRACTICAL SURFACE AN, P495
[5]   Nanostructured palladium-iron membranes for hydrogen separation and membrane hydrogenation reactions [J].
Bryden, KJ ;
Ying, JY .
JOURNAL OF MEMBRANE SCIENCE, 2002, 203 (1-2) :29-42
[6]   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
[7]   Effects of electroless plating chemistry on the synthesis of palladium membranes [J].
Cheng, YS ;
Yeung, KL .
JOURNAL OF MEMBRANE SCIENCE, 2001, 182 (1-2) :195-203
[8]   ADSORPTION OF HYDROGEN ON PALLADIUM SINGLE-CRYSTAL SURFACES [J].
CONRAD, H ;
ERTL, G ;
LATTA, EE .
SURFACE SCIENCE, 1974, 41 (02) :435-446
[9]   PROCESSING INDUSTRIAL GAS STREAMS AT HIGH PRESSURES ... DIFFUSION OF HYDROGEN THROUGH PALLADIUM MEMBRANES [J].
DEROSSET, AJ .
INDUSTRIAL AND ENGINEERING CHEMISTRY, 1960, 52 (06) :525-528
[10]   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