A comparison study on high-temperature water-gas shift reaction over Fe/Al/Cu and Fe/Al/Ni catalysts using simulated waste-derived synthesis gas

被引:26
作者
Jeong, Dae-Woon [1 ]
Jang, Won-Jun [1 ]
Shim, Jae-Oh [1 ]
Han, Won-Bi [1 ]
Jeon, Kyung-Won [1 ]
Seo, Yong-Chil [1 ]
Roh, Hyun-Seog [1 ]
Gu, Jae Hoi [2 ]
Lim, Yong Taek [2 ]
机构
[1] Yonsei Univ, Dept Environm Engn, Wonju 220710, Gangwon, South Korea
[2] Plant Engn Ctr, IAE, Suwon 443749, Gyeonggi, South Korea
基金
新加坡国家研究基金会;
关键词
High temperature water-gas shift; Waste-derived synthesis gas; Fe/Al/Cu; Reducibility; Magnetite; SIZED PT/CEO2 CATALYST; IRON-BASED CATALYSTS; GASIFICATION TECHNOLOGIES; MODIFIED FERRITES; H-2; PRODUCTION; COPPER; CH4; ENHANCEMENT; PERFORMANCE; ENERGY;
D O I
10.1007/s10163-014-0272-8
中图分类号
X [环境科学、安全科学];
学科分类号
08 ; 0830 ;
摘要
A comparative study on Fe/Al, Fe/Al/Cu, and Fe/Al/Ni catalysts in high-temperature water-gas shift reaction (HT-WGS) using simulated waste-derived synthesis gas has been carried out. The metal oxide (Cu and Ni) and aluminum incorporated Fe catalysts were designed to get highly active HT-WGS catalysts. Despite the high CO concentration in the simulated waste-derived synthesis gas, Fe/Al/Cu catalyst exhibited the highest CO conversion (84 %) and 100 % selectivity to CO2 at a very high gas hourly space velocity (GHSV) of 40,057 h(-1). The outstanding catalytic performance is mainly due to easier reducibility, the synergy effect of Cu and Al, and the stability of the magnetite.
引用
收藏
页码:650 / 656
页数:7
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