A reaction-separation combined OCM process for high C-2 hydrocarbon yields
Jiang, Y; Yu, C; Li, W; Yan, J; Ji, Y; dePontes, M; Espinoza, RL; Nicolaides, CP; Scholtz, JH; Scurrell, MS
刊名NATURAL GAS CONVERSION IV
1997
卷号107页码:339-343
ISSN号0167-2991
文献子类Article
英文摘要The oxidative coupling of methane (OCM) has been investigated over doped CaTiO3 catalysts in a fixed-bed reactor with gas recycle and C-2 trapping. It has been demonstrated that both high selectivity to C-2 and CH4 conversion, thus a high C-2 yield, can be realized in such a recycle reactor which has several advantages for the consecutive reaction as the OCM reaction. The best C-2 yield obtained so far is 55%, which could be improved further by the optimization of reaction conditions.
WOS关键词METHANE ; ETHYLENE
WOS研究方向Chemistry ; Energy & Fuels ; Engineering
语种英语
出版者ELSEVIER SCIENCE BV
WOS记录号WOS:A1997BJ22F00050
内容类型期刊论文
源URL[http://cas-ir.dicp.ac.cn/handle/321008/168202]  
专题大连化学物理研究所_中国科学院大连化学物理研究所
通讯作者Jiang, Y
推荐引用方式
GB/T 7714
Jiang, Y,Yu, C,Li, W,et al. A reaction-separation combined OCM process for high C-2 hydrocarbon yields[J]. NATURAL GAS CONVERSION IV,1997,107:339-343.
APA Jiang, Y.,Yu, C.,Li, W.,Yan, J.,Ji, Y.,...&Scurrell, MS.(1997).A reaction-separation combined OCM process for high C-2 hydrocarbon yields.NATURAL GAS CONVERSION IV,107,339-343.
MLA Jiang, Y,et al."A reaction-separation combined OCM process for high C-2 hydrocarbon yields".NATURAL GAS CONVERSION IV 107(1997):339-343.
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