CARBON-DIOXIDE REFORMING OF METHANE WITH SUPPORTED RHODIUM

被引:489
作者
RICHARDSON, JT
PARIPATYADAR, SA
机构
[1] Department of Chemical Engineering, University of Houston, Houston
来源
APPLIED CATALYSIS | 1990年 / 61卷 / 02期
关键词
adsorption; carbon dioxide; coke formation; hydrogen); kinetics; methane reforming; rhodium/alumina; selectivity (carbon monoxide; solar systems;
D O I
10.1016/S0166-9834(00)82152-1
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
Rhodium supported on γ-Al2O3 was an effective catalyst for reforming methane with carbon dioxide at low ratios of CO2/CH4. Unlike other metals tested, no carbon deposited on the catalyst in the temperature range 600-800°C. Kinetic experiments on a 0.5 wt.-% Rh/Al2O3 catalyst gave rate equations for the reforming and shift reactions. A model was constructed for conversion in a pellet by incorporating both the reverse reaction and the effect of external and internal diffusion. This model, when tested with the data from a pellet string reactor, gave very good agreement with conversions and product distributions. External diffusion was negligible but internal effectiveness factors were about 0.3 or more. The model was expanded to a large-scale packed bed with appropriate heat transfer parameters. Adjustable factors were determined by matching measured temperature profiles from pilot unit experiments. The catalyst later performed successfully in a solar receiver/reactor and shows potential for conventional processing. © 1990.
引用
收藏
页码:293 / 309
页数:17
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