Electrochemical Hydrogen Separation via Solid Acid Membranes

被引:14
|
作者
Papandrew, Alexander B. [1 ]
Wilson, David L., III [1 ]
Cantillo, Nelly M. [1 ]
Hawks, Samantha [1 ]
Atkinson, Robert W., III [1 ]
Goenaga, Gabriel A. [1 ]
Zawodzinski, Thomas A., Jr. [1 ,2 ,3 ]
机构
[1] Univ Tennessee, Dept Chem & Biomol Engn, Knoxville, TN 37996 USA
[2] Oak Ridge Natl Lab, Div Mat Sci & Technol, Oak Ridge, TN 37831 USA
[3] King Abdulaziz Univ, Dept Chem, Jeddah 21413, Saudi Arabia
关键词
ELECTROLYTE FUEL-CELL; EVOLUTION REACTIONS; PROTON CONDUCTORS; CARBON-MONOXIDE; CO; OXIDATION; STEAM; ELECTROOXIDATION; PERFORMANCE; REFORMATE;
D O I
10.1149/2.078405jes
中图分类号
O646 [电化学、电解、磁化学];
学科分类号
081704 ;
摘要
The inorganic proton conductor CsH2PO4 (CDP) was investigated as a proton exchange membrane for electrochemical hydrogen separation at temperatures from 230 degrees C to 250 degrees C. Carbon-supported Pt and Pd were synthesized via vapor deposition and evaluated as hydrogen oxidation catalysts in hydrogen pump electrodes. The hydrogen oxidation and evolution reactions were reversible on Pt in 100% H-2, and a cell current of 300 mA cm(-2) was produced at a 25 mV overpotential after correction for the membrane ohmic resistance. Anodes were also exposed to hydrogen-containing gas mixtures to simulate reformed fuels. In the case of a stream containing 7% CO (75% H-2, balance CO2), a 300 mA cm(-2) cell current required 45 mV electrode polarization, and in a stream containing 10% CO and 0.25% CH4 (43% H-2, balance N-2, CO2), 75 mV polarization was required to obtain the same current. The performance of carbon-supported Pd was virtually identical to that of Pt under each of these conditions. (C) 2014 The Electrochemical Society. All rights reserved.
引用
收藏
页码:F679 / F685
页数:7
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