Hydrogen Production by Water Gas Shift Reaction Over Pd-K Impregnated Co Oxide Catalyst

被引:14
作者
Yamamuro, Keisuke [1 ]
Tamura, Sakurako [1 ]
Watanabe, Ryo [1 ,2 ]
Sekine, Yasushi [1 ]
机构
[1] Waseda Univ, Dept Appl Chem, Shinjuku Ku, Tokyo 1698555, Japan
[2] Shizuoka Univ, Dept Mat Sci & Chem Engn, Naka Ward, Hamamatsu, Shizuoka, Japan
关键词
Water gas shift reaction; Co catalyst; Promotion effect of potassium; Hydrogen production; COBALT MANGANESE OXIDE; POTASSIUM; METHANATION; SULFUR; RUTILE;
D O I
10.1007/s10562-013-0974-x
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
Effects of K and Pd loading on Co3O4 catalyst for the water gas shift (WGS) reaction were investigated. Pd/K/Co3O4 catalyst showed high and stable activity and high selectivity to WGS. Regarding loading amounts of Pd and K, the latter is important for WGS activity and selectivity. XRD, XAFS, and TPR measurements confirmed potassium loading benefits. Supported Pd promoted oxidation of CO with lattice oxygen. The synergetic effect of these functions of K and Pd protected high catalyst activity and stability.
引用
收藏
页码:339 / 344
页数:6
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