Carbon monoxide hydrogenation over zirconia supported Ni and Co-Ni bimetallic catalysts

被引:20
作者
Das, PC
Pradhan, NC
Dalai, AK [1 ]
Bakshi, NN
机构
[1] Univ Saskatchewan, Dept Chem Engn, Catlaysis & Chem React Engn Labs, Saskatoon, SK S7N 5C5, Canada
[2] Indian Inst Technol, Dept Chem Engn, Kharagpur 721302, W Bengal, India
关键词
Fisher-Tropsch synthesis; CO hydrogenation; bimetallic catalyst; nickel; cobalt; zirconia support;
D O I
10.1007/s10562-004-7931-7
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
Zirconia supported nickel and cobalt-nickel bimetallic catalysts were prepared and characterized for various physico-chemical properties. The hydrogenation of carbon monoxide was studied over these catalysts in the pressure range of 101.3-1654 kPa, temperature range of 513-533 K, weight hourly space velocity range of 8-14 h(-1) and H2/CO mole ratio of 2. Catalysts containing both Co and Ni were found to give higher C(5+) hydrocarbons selectivity compared to that containing only Ni. A maximum C(5+) hydrocarbons selectivity of 55 wt% was obtained at 655 kPa pressure, 523 K and 9.6 h(-1) of WHSV with catalyst containing 4.03 wt% Co and 2.64 wt% Ni. The C(2) and C(3) olefin contents of the products decreased with increase in pressure. Improved deactivation behavior of the catalysts was observed when operated at high pressure.
引用
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页码:153 / 160
页数:8
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