Development of a powerful CO2 methanation process using a structured Ni/CeO2 catalyst

被引:101
|
作者
Ratchahat, Sakhon [1 ]
Sudoh, Masao [1 ]
Suzuki, Yuji [2 ]
Kawasaki, Wataru [2 ]
Watanabe, Ryo [2 ]
Fukuhara, Choji [2 ]
机构
[1] Amano Inst Technol, Kita Ku, 7955-98 Hosoe Cho Kiga, Hamamatsu, Shizuoka 4311305, Japan
[2] Shizuoka Univ, Grad Sch Engn, Dept Appl Chem & Biochem Engn, Naka Ku, 3-5-1 Johoku, Hamamatsu, Shizuoka 4328561, Japan
关键词
CO2; methanation; Ni/CeO2; Structured catalyst; Honeycomb; SYNTHETIC NATURAL-GAS; MASS-TRANSFER; TEMPERATURE; REACTOR; SIZE;
D O I
10.1016/j.jcou.2018.01.004
中图分类号
O6 [化学];
学科分类号
0703 ;
摘要
The purpose of this study is to develop a powerful CO2 methanation process using a variety of structured Ni/CeO2 catalysts. Various configurations of metallic honeycomb-type catalysts, which are plain, stacked, segment, and multi-stacked were constructed and tested under various reaction conditions; i.e. inlet temperature, feed flow rate and CO2 partial pressure. Effects of the developed configurations including stack and gap distance were examined. The random-flow channels of stacked type and the gap distance of segment type could improve the catalytic activity, resulting in high CO2 conversion. Under industrial-like high feed rate condition and pure feed gas component, a moderate hot spot over the multi-stacked catalyst was observed and reported for the first time. The moderate hot spot reboosted the conversion to a high level even at high feed flow rate condition of 3000 mL/min (contact time of 235 ms). As a result, high CO2 conversion > 90%, high CH4 selectivity > 99.5%, and high stability with dropped conversion < 0.6%, could be maintained over 76 h test at setting temperature of 300 degrees C, flow rate of 3000 mL/min and feed ratio of p(CO2)/p(H2) = 0.12/0.88. The stability of the Ni/CeO2 catalyst under the moderate hot spot condition was revealed by BET, SEM and XRD analyses.
引用
收藏
页码:210 / 219
页数:10
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