Fischer-Tropsch Synthesis on Co/Al2O3 Catalyst: Effect of Pretreatment Procedure

被引:14
|
作者
Pan, Zhendong [1 ]
Parvari, Matin [1 ]
Bukur, Dragomir B. [1 ,2 ]
机构
[1] Texas A&M Univ Qatar, Chem Engn Program, Doha, Qatar
[2] Texas A&M Univ, Artie McFerrin Dept Chem Engn, College Stn, TX 77843 USA
关键词
Fischer-Tropsch synthesis; Co/Al2O3; catalyst; Temperature-programmed hydrogenation and oxidation; Carbon species differentiation; Bulk cobalt phases; COBALT CATALYSTS; CO/SIO2; CATALYST; CARBON; DEACTIVATION; PERFORMANCE; IRON;
D O I
10.1007/s11244-013-0203-2
中图分类号
O69 [应用化学];
学科分类号
081704 ;
摘要
The effect of pretreatment procedure on catalytic performance during Fischer-Tropsch synthesis (FTS) of unpromoted cobalt on alumina (15 %Co/Al2O3) catalyst was studied in a fixed-bed reactor. Pure carbon monoxide or a mixture of hydrogen and carbon monoxide were used as reducing agents prior to FTS. Pretreatments with pure CO result in low activity and high selectivity to methane and gaseous hydrocarbons in comparison to standard hydrogen reduction. The use of synthesis gas (H-2/CO = 2/1) as a reducing agent resulted in high initial activity and high selectivity to gaseous hydrocarbons. Pretreatment procedure that utilized synthesis gas after the CO reduction resulted in low activity but high selectivity to high molecular weight hydrocarbons. Catalyst performance is strongly affected by the presence of cobalt carbides, cobalt oxide and/or various types of carbon species on the surface as determined by X-ray diffraction and temperature-programmed hydrogenation and oxidation characterization techniques.
引用
收藏
页码:470 / 478
页数:9
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