Hydrogen permeation measurements of Pd and Pd-Cu membranes using dynamic pressure difference method

被引:29
作者
Chen, Wei-Hsin [1 ]
Hsu, Po-Chih [1 ]
机构
[1] Natl Univ Tainan, Dept Greenergy, Tainan 700, Taiwan
关键词
Palladium (Pd) and palladium-copper; (Pd-Cu) membranes; Permeance and permeability; Dynamic pressure difference method; Optimal pressure exponent; Activation energy; POROUS STAINLESS-STEEL; COMPOSITE MEMBRANES; PALLADIUM MEMBRANE; SEPARATION; METHANE; GENERATION; FLUX; THIN; DEHYDROGENATION; FABRICATION;
D O I
10.1016/j.ijhydene.2011.04.141
中图分类号
O64 [物理化学(理论化学)、化学物理学];
学科分类号
070305 [高分子化学与物理];
摘要
Hydrogen permeation across membranes is measured using a dynamic pressure difference method. In the method, a transient system for continuously monitoring hydrogen flux of a membrane is conducted. Three different membranes, consisting of two pure palladium (Pd) membranes with different thicknesses and one palladium-copper (Pd-Cu) membrane supported by porous stainless steel (PSS) tubes, are taken into account. Three different operating temperatures of 320, 350 and 380 degrees C as well as two different initial pressure differences of 5 and 10 atm are considered to evaluate the effects of the operating parameters upon the hydrogen permeation. The results suggest that a threshold of pressure difference is always exhibited at the end of the permeation process, regardless of which membrane is tested. The hydrogen permeation rate can be predicted well for the pressure exponent in the range of 0.1-1.0; however, the optimal pressure exponent is located between 0.5 and 0.8. The theoretical analysis indicates that the characteristic time of hydrogen permeation in the present system ranges from 245 to 460 s and the entire permeation period is longer than the characteristic time by an order of magnitude. In regard to the effect of membrane temperature on the permeation, the activation energies of the three membranes range from 11 to 18 kJ mol(-1). Copyright (C) 2011, Hydrogen Energy Publications, LLC. Published by Elsevier Ltd. All rights reserved.
引用
收藏
页码:9355 / 9366
页数:12
相关论文
共 35 条
[1]
Hydrogen membrane separation techniques [J].
Adhikari, S ;
Fernando, S .
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 2006, 45 (03) :875-881
[2]
Hydrogen Production Using Pd-based Membrane Reactors for Fuel Cells [J].
Basile, Angelo .
TOPICS IN CATALYSIS, 2008, 51 (1-4) :107-122
[3]
Characterization of Pd-Ag membranes after exposure to hydrogen flux at high temperatures [J].
Bosko, Maria L. ;
Yepes, David ;
Irusta, Silvia ;
Eloy, Pierre ;
Ruiz, Patricio ;
Lombardo, Eduardo A. ;
Cornaglia, Laura M. .
JOURNAL OF MEMBRANE SCIENCE, 2007, 306 (1-2) :56-65
[4]
The effect of H2S on the performance of Pd and Pd/Au composite membrane [J].
Chen, Chao-Huang ;
Ma, Yi Hua .
JOURNAL OF MEMBRANE SCIENCE, 2010, 362 (1-2) :535-544
[5]
Hydrogen generation from a catalytic water gas shift reaction under microwave irradiation [J].
Chen, Wei-Hsin ;
Jheng, Jian-Guo ;
Yu, A. B. .
INTERNATIONAL JOURNAL OF HYDROGEN ENERGY, 2008, 33 (18) :4789-4797
[6]
Hydrogen permeation dynamics across a palladium membrane in a varying pressure environment [J].
Chen, Wei-Hsin ;
Hsu, Po-Chih ;
Lin, Bo-Jhih .
INTERNATIONAL JOURNAL OF HYDROGEN ENERGY, 2010, 35 (11) :5410-5418
[7]
Effect of microwave double absorption on hydrogen generation from methanol steam reforming [J].
Chen, Wei-Hsin ;
Lin, Bo-Jhih .
INTERNATIONAL JOURNAL OF HYDROGEN ENERGY, 2010, 35 (05) :1987-1997
[8]
Modeling of transient hydrogen permeation process across a palladium membrane [J].
Chen, Wei-Hsin ;
Chiu, I-Han .
APPLIED ENERGY, 2010, 87 (03) :1023-1032
[9]
Hysteresis and reaction characterization of methane catalytic partial oxidation on rhodium catalyst [J].
Chen, Wei-Hsin ;
Chiu, Tin-Wei ;
Hung, Chen-I ;
Lin, Mu-Rong .
JOURNAL OF POWER SOURCES, 2009, 194 (01) :467-477
[10]
Transient dynamic of hydrogen permeation through a palladium membrane [J].
Chen, Wei-Hsin ;
Chiu, I. -Han .
INTERNATIONAL JOURNAL OF HYDROGEN ENERGY, 2009, 34 (05) :2440-2448