Catalytic Technology for Carbon Dioxide Reforming of Methane to Synthesis Gas

被引:513
作者
Fan, Mun-Sing [1 ]
Abdullah, Ahmad Zuhairi [1 ]
Bhatia, Subhash [1 ]
机构
[1] Univ Sains Malaysia, Sch Chem Engn, Nibong Tebal 14300, Pulau Pinang, Malaysia
关键词
fuels; heterogeneous catalysis; supported catalysts; sustainable chemistry; syngas production; DIELECTRIC-BARRIER DISCHARGE; PROMOTED NI/AL2O3 CATALYSTS; FLUIDIZED-BED REACTOR; SUPPORTED NI CATALYSTS; PRODUCE SYNTHESIS GAS; TO-SYNGAS CONVERSION; MGO SOLID-SOLUTION; LOW H-2/CO RATIO; PARTIAL OXIDATION; MEMBRANE REACTORS;
D O I
10.1002/cctc.200900025
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
The mitigation and utilization of greenhouse gases, such as carbon dioxide and methane, are among the most important challenges in the area of energy research. Dry reforming of CH4 (DRM), which uses both CO2 and CH4 as reactants, is a potential method to utilize the greenhouse gases in the atmosphere. Natural gas containing high concentrations of CO2 and CH4 could therefore be utilized for hydrogen and synthesis gas (syngas) production in the near future, without need for the removal of CO2 from the source gas. Thus, the DRM reaction is a suitable process to convert CH4 and CO2 to syngas, which is a raw material for liquid fuel production, through the Fischer-Tropsch process. Herein, the development of CO2 reforming for syngas production is reviewed, covering process chemistry; catalyst development, and process technologies as well as the potential future direction for this process.
引用
收藏
页码:192 / 208
页数:17
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