Fischer-Tropsch synthesis on Co/ZnO catalyst-Effect of pretreatment procedure

被引:37
|
作者
Pan, Zhendong [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/ZnO catalyst; Hydrogen and carbon monoxide activation; Catalyst characterization; IMPREGNATED COBALT CATALYSTS; CARBON-MONOXIDE; HYDROCARBON SYNTHESIS; REDUCTION; SUPPORT; HYDROGEN; CO; DEACTIVATION; CO/AL2O3; ALUMINA;
D O I
10.1016/j.apcata.2011.07.012
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 catalyst pretreatment, using hydrogen or carbon monoxide, on the activity and selectivity of cobalt on ZnO catalyst (10 wt% Co/ZnO) during Fischer-Tropsch synthesis was studied in a fixed bed reactor. Catalyst reduced with hydrogen had higher activity and higher olefin content, and produced less methane than the CO activated catalyst. Catalysts were characterized by means of Brunauer-Emmett-Teller (BET), X-ray diffraction (XRD), temperature programmed reduction (TPR), and hydrogen chemisorption (H-2-TPD) with pulse re-oxidation. Reduction of Co3O4 occurs in two stages during H-2-TPR and CO-TPR. In the latter case CoO, metallic cobalt, cobalt carbides (CoxC; x = 2 or 3) and carbon (from CO disproportionation) are formed during the reduction process. The existence of Co-0 along with CoO and CoxC, indicates a possibility of two reaction paths for formation of CoxC from CoO: the direct path (CoO -> CoxC) and a series reaction via Co-0 (i.e. CoO -> Co-0 CoxC). (C) 2011 Elsevier B.V. All rights reserved.
引用
收藏
页码:74 / 80
页数:7
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