Dry Reforming of Hydrocarbon Feedstocks

被引:100
作者
Shah, Yatish T. [1 ]
Gardner, Todd H. [2 ]
机构
[1] Norfolk State Univ, Dept Engn, Norfolk, VA 23505 USA
[2] US DOE, Natl Energy Technol Lab, Morgantown, WV USA
来源
CATALYSIS REVIEWS-SCIENCE AND ENGINEERING | 2014年 / 56卷 / 04期
关键词
Carbon dioxide; Methane; Hydrogen production; Hydrocarbon; Dry reforming; Catalyst; Syngas; GHG; Nickel; Solid oxide; Metal carbide; Deactivation; SUPPORTED RHODIUM CATALYSTS; NI-BASED CATALYSTS; CARBON-DIOXIDE; SYNTHESIS GAS; PARTIAL OXIDATION; MOLYBDENUM CARBIDE; SUPERCRITICAL WATER; HYDROGEN-PRODUCTION; NICKEL-CATALYSTS; NI/ALPHA-AL2O3; CATALYST;
D O I
10.1080/01614940.2014.946848
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
Developments in catalyst technology for the dry reforming of hydrocarbon feedstocks are reviewed for methane, higher hydrocarbons and alcohols. Thermodynamics, mechanisms and the kinetics of dry reforming are also reviewed. The literature on Ni catalysts, bi-metallic Ni catalysts and the role of promoters on Ni catalysts is critically evaluated. The use of noble and transitional metal catalysts for dry reforming is discussed. The application of solid oxide and metal carbide catalysts to dry reforming is also evaluated. Finally, various mechanisms for catalyst deactivation are assessed. This review also examines the various process related issues associated with dry reforming such as its application and heat optimization. Novel approaches such as supercritical dry reforming and microwave assisted dry reforming are briefly expanded upon.
引用
收藏
页码:476 / 536
页数:61
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