Combined H2O and CO2 reforming of CH4 over Ce-promoted Ni/Al2O3 catalyst for gas to liquid (GTL) process: Enhancement of Ni-CeO2 interaction

被引:56
|
作者
Koo, Kee Young [1 ]
Roh, Hyun-Seog [2 ]
Jung, Un Ho [1 ]
Yoon, Wang Lai [1 ]
机构
[1] KIER, Hydrogen Energy Res Ctr, Taejon 305343, South Korea
[2] Yonsei Univ, Dept Environm Engn, Wonju 220710, Gangwon Do, South Korea
关键词
Gas to liquid (GTL); Synthesis gas; Combined steam and carbon dioxide reforming of methane; Ni-CeO2 intimate contact; Coke resistance; NICKEL-CATALYSTS; METHANE; PERFORMANCE; STEAM;
D O I
10.1016/j.cattod.2011.07.027
中图分类号
O69 [应用化学];
学科分类号
081704 ;
摘要
The effect of Ni-Ce loading method on the catalytic activity and coke formation over Ce-promoted Ni/Al2O3 catalysts was investigated in combined steam and carbon dioxide reforming of methane (CSCRM) to produce synthesis gas with a H-2/CO ratio of 2 for gas to liquid (GTL) process. 12 wt%Ni-6 wt%Ce/Al2O3 catalysts prepared by a co-impregnation method exhibited higher catalytic performance and less coke formation than 12 wt%Ni/6 wt%Ce/Al2O3 and 6 wt%Ce/12 wt%Ni/Al2O3 catalysts prepared by a sequential impregnation method due to the improvement of Ni dispersion and high oxygen storage capacity resulting from the intimate contact between Ni and CeO2 on the surface of the catalyst. (C) 2011 Elsevier B.V. All rights reserved.
引用
收藏
页码:126 / 130
页数:5
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