COx free hydrogen by methane decomposition over activated carbons

被引:52
作者
Ashok, J. [1 ]
Kumar, S. Naveen [1 ]
Venugopal, A. [1 ]
Kumari, V. Durga [1 ]
Tripathi, S. [2 ]
Subrahmanyam, M. [1 ]
机构
[1] Indian Inst Chem Technol, Hyderabad 500007, Andhra Pradesh, India
[2] Indian Inst Petr, Dehra Dun 248005, Uttar Pradesh, India
关键词
methane decomposition; hydrogen production; activated carbons;
D O I
10.1016/j.catcom.2007.05.046
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
Catalytic characteristics of carbon catalysts for methane decomposition were examined in a fixed bed, quartz-tube continuous flow reactor. The reactions were carried out under atmospheric pressure at 800-900 degrees C. The kinetics of methane decomposition over carbon catalysts and surface changes before and after the reaction were investigated. In all the kinds of carbon catalysts tested, no discernible trend was observed between the initial activity and the surface area. Highest initial methane conversion rate of 1.27 mmols/min g-cat, and sustainability factor (R-1/R-0) of 0.40 for a high surface area carbon catalyst yielded carbon of 890 mg/g-cat at 900 degrees C. The activation energies are in the range from 170 to 175 kJ mol(-1). The physicochemical properties like surface area, pore size distribution, SEM and carbon content generated from the methane decomposition for the used and fresh catalysts are presented in this work. (c) 2007 Elsevier B.V. All rights reserved.
引用
收藏
页码:164 / 169
页数:6
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