Fischer-Tropsch synthesis: effect of ammonia impurities in syngas feed over a cobalt/alumina catalyst

被引:33
|
作者
Pendyala, Venkat Ramana Rao [1 ]
Gnanamani, Muthu Kumaran [1 ]
Jacobs, Gary [1 ]
Ma, Wenping [1 ]
Shafer, Wilson D. [1 ]
Davis, Burtron H. [1 ]
机构
[1] Univ Kentucky, Ctr Appl Energy Res, Lexington, KY 40511 USA
关键词
Fischer-Tropsch synthesis; Cobalt/alumina catalyst; Ammonia; Product selectivity; HYDROCARBON SYNTHESIS; PATHWAYS;
D O I
10.1016/j.apcata.2013.07.060
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
The effect of co-fed ammonia in syngas on the performance of a traditional cobalt catalyst (platinum promoted cobalt/alumina) was investigated during Fischer-Tropsch synthesis (FTS) using a continuously stirred tank reactor (CSTR). The addition of 1, 10,100, and 1200 ppmw (concentration of ammonia with respect to the syngas feed) of ammonia resulted in significant irreversible deactivation of the catalyst under identical reaction conditions. The percentage of deactivation was almost constant (+/- 5%) at all the concentrations (1-1200 ppmw) of ammonia exposure. The addition of ammonia (either NH3 gas or aqueous NH4OH) particularly at higher concentrations exhibits lower methane selectivity compared to ammonia-free synthesis conditions. This enhancement in C-5+ hydrocarbon formation may be attributed to the selective poisoning of metallic cobalt sites by addition of ammonia. (C) 2013 Elsevier B.V. All rights reserved.
引用
收藏
页码:38 / 43
页数:6
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