Fischer-Tropsch synthesis:: effect of small amounts of boron, ruthenium and rhenium on Co/TiO2 catalysts

被引:73
|
作者
Li, JL [1 ]
Jacobs, G [1 ]
Zhang, YQ [1 ]
Das, T [1 ]
Davis, BH [1 ]
机构
[1] Univ Kentucky, Ctr Appl Energy Res, Lexington, KY 40511 USA
关键词
cobalt; titania; boron; ruthenium; rhenium; Fischer-Tropsch synthesis; synthesis gas conversion; continuously stirred tank reactor;
D O I
10.1016/S0926-860X(01)00752-9
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 effect of the addition of small amounts of boron, ruthenium and rhenium on the Fischer-Tropsch (F-T) catalyst activity and selectivity of a 10 Wt.% Co/TiO2 catalyst has been investigated in a continuously stirred tank reactor (CSTR). A wide range of synthesis gas conversions has been obtained by varying space velocities over the catalysts. The addition of a small amount of boron (0.05 wt.%) onto Co/TiO2 does not change the activity of the catalyst at lower space times and slightly increases synthesis gas conversion at higher space times. The product selectivity is not significantly influenced by boron addition for all space velocities investigated. Ruthenium addition (0.20 wt.%) onto Co/TiO2 and CoB/TiO2 catalysts improves the catalyst activity and selectivity. At a space time of 0.5 h-g cat./NL, synthesis gas conversion increases from 50-54 to 68-71% range and methane selectivity decreases from 9.5 to 5.5% (molar carbon basis) for the promoted catalyst. Among the five promoted and non-promoted catalysts, the rhenium promoted Co/TiO2 catalyst (0.34 wt.% Re) exhibited the highest synthesis gas conversion, and at a space time of 0.5 h-g cat./NL, synthesis gas conversion was 73.4%. In comparison with the results obtained in a fixed bed reactor, the catalysts displayed a higher F-T catalytic activity in the CSTR. (C) 2002 Elsevier Science B.V. All rights reserved.
引用
收藏
页码:195 / 203
页数:9
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