Fischer-Tropsch synthesis: Studies effect of reduction variables on the performance of Fe-Ni-Co catalyst

被引:18
|
作者
Azizi, Hamid Reza [1 ]
Mirzaei, Ali Akbar [1 ]
Kaykhaii, Massoud [1 ]
Mansouri, Mohsen [2 ]
机构
[1] Univ Sistan & Baluchestan, Fac Sci, Dept Chem, Zahedan 98135674, Iran
[2] Univ Sistan & Baluchestan, Fac Engn, Dept Chem Engn, Zahedan 98164161, Iran
关键词
Fe-Ni-Co catalyst; Co-precipitation; Reduction conditions; Fischer-Tropsch synthesis; PRODUCT DISTRIBUTIONS; CERIA ADDITION; IRON; TEMPERATURE; ACTIVATION; REDUCIBILITY; HYDROCARBONS; SELECTIVITY; KINETICS; BEHAVIOR;
D O I
10.1016/j.jngse.2014.04.003
中图分类号
TE [石油、天然气工业]; TK [能源与动力工程];
学科分类号
0807 ; 0820 ;
摘要
The effect of reduction temperature (200-450 degrees C) and various atmospheres on the performance of Fe-Ni-Co catalyst in a fixed bed reactor have been investigated. Catalysts were prepared by co-precipitation procedure and used for CO hydrogenation in Fischer-Tropsch synthesis (FTS). The catalyst which was reduced at 300 degrees C under H-2 atmosphere showed the best catalytic performance for higher CO conversion and low CH4 selectivity. The initial activity depends on the atmosphere used and is in the order of H-2 > CO > H-2: CO = 1. XRD, SEM/EDS, and BET characterization of precursor, calcinated and reduced catalysts showed that while by increasing reduction temperature; the pore volume increases and their pore size decreases. It was observed that the phase composition of catalysts reduced with H-2 is strongly dependent on the pretreatment conditions. (C) 2014 Elsevier B.V. All rights reserved.
引用
收藏
页码:484 / 491
页数:8
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