Preparation and characterization of palladium-plated, porous glass for hydrogen enrichment

被引:30
作者
Altinisik, O [1 ]
Dogan, M [1 ]
Dogu, G [1 ]
机构
[1] Gazi Univ, Dept Chem Engn, TR-06570 Ankara, Turkey
关键词
hydrogen; composite membrane; palladium; electroless plating;
D O I
10.1016/j.cattod.2005.06.012
中图分类号
O69 [应用化学];
学科分类号
081704 [应用化学];
摘要
In this study, cylindrical porous glass tablets were plated by palladium using electroless plating technique. Hypophosphite and Co(II) complexes were used as reducing agents in the prepared plating baths. Experiments were carried out in an especially designed glass vessel in which helium gas was continuously bubbled through the solution to create uniform concentration and to remove hydrogen gas from the surface for the case of hypophosphite-based procedure. XRF analysis of the upper layer of the composite membrane prepared by the hypophosphite-based bath showed a Pd/Si ratio of 4.6. SEM photographs indicated impregnation of Pd into the substrate upto 200 mu m. However, the thickness of the dense Pd layer was only about 15 mu m. SEM photographs and XRF results showed that hypophosphite-based bath was much more successful than the Co(II) complex-bath in Pd plating. Permeation experiments carried out at different temperatures showed that the contribution of surface diffusion to the permeation was significant at low temperatures and solution-diffusion mechanism was not important in the 40-200 degrees C temperature range for these membranes. The selectivity ratio for H-2/N-2 was found to be about 7 at 200 degrees C. (c) 2005 Elsevier B.V. All rights reserved.
引用
收藏
页码:641 / 646
页数:6
相关论文
共 15 条
[1]
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
[2]
Dynamics of flow and diffusion of adsorbing gases in Al2O3 and Pd-Al2O3 pellets [J].
Dogan, M ;
Dogu, G .
AICHE JOURNAL, 2003, 49 (12) :3188-3198
[3]
Hydrogen diffusivity enhancement in alumina pellets due to impregnated palladium [J].
Dogan, M ;
Dogu, G .
CHEMICAL ENGINEERING COMMUNICATIONS, 2003, 190 (5-8) :662-676
[4]
DOGAN M, 2003, 3 E MED CHEM ENG C P
[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]
Permeation of hydrogen through palladium/alumina composite membranes [J].
Huang, TC ;
Wei, MC ;
Chen, HI .
SEPARATION SCIENCE AND TECHNOLOGY, 2001, 36 (02) :199-222
[7]
Application of electroless deposited thin-film palladium composite membrane in hydrogen separation [J].
Ilias, S ;
Su, N ;
UdoAka, UI ;
King, FG .
SEPARATION SCIENCE AND TECHNOLOGY, 1997, 32 (1-4) :487-504
[8]
Fabrication of dense palladium composite membranes for hydrogen separation [J].
Li, AW ;
Liang, WQ ;
Hughes, R .
CATALYSIS TODAY, 2000, 56 (1-3) :45-51
[9]
A new preparation technique for Pd alumina membranes with enhanced high-temperature stability [J].
Paglieri, SN ;
Foo, KY ;
Way, JD ;
Collins, JP ;
Harper-Nixon, DL .
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 1999, 38 (05) :1925-1936
[10]
Catalytic dehydrogenation of hydrocarbons in palladium composite membrane reactors [J].
Quicker, P ;
Höllein, V ;
Dittmeyer, R .
CATALYSIS TODAY, 2000, 56 (1-3) :21-34