Hydrogen production via partial oxidation of methane with plasma-assisted catalysis

被引:47
|
作者
Chao, Yu [1 ,2 ]
Huang, Ching-Tsuen [2 ]
Lee, How-Ming [2 ]
Chang, Moo-Been [1 ]
机构
[1] Natl Cent Univ, Grad Inst Environm Engn, Chungli 32001, Taiwan
[2] Inst Nucl Energy Res, Lungtan 32546, Taiwan
关键词
methane reforming; reformer; hydrogen; partial oxidation; plasma-assisted catalysis (PAC);
D O I
10.1016/j.ijhydene.2007.09.024
中图分类号
O64 [物理化学(理论化学)、化学物理学];
学科分类号
070304 ; 081704 ;
摘要
This study demonstrates an economic reforming process that combines arc plasma with catalyst in series for hydrogen production. Hydrogen was generated by means of partial oxidation of methane. Granular Ni catalysts were packed in the post plasma zone. No extra-energy was needed to sustain the temperature of catalyst bed; the elevated temperature was maintained both by the hot gases from plasma region and by the heat of reforming reaction itself. A promising energy efficiency of 1.21 MJ/kg-H-2, being together with high hydrogen yield (89.9%) and high methane conversion (90.2%), was experimentally achieved. The energy efficiency is estimated to be 20% higher compared with a gas turbine system with methane as the fuel. In addition, thermodynamic analysis for partial oxidation of methane was conducted. Experimental data agreed well with the thermodynamic results, indicating that high thermal efficiency can be achieved with the plasma-assisted catalysis process. (C) 2007 International Association for Hydrogen Energy. Published by Elsevier Ltd. All rights reserved.
引用
收藏
页码:664 / 671
页数:8
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