The Conversion of Syngas to Liquid Fuels in a Dual-Bed Single Reactor Process

被引：4
|
作者：
Corsaro, A. [1 ]
Wiltowski, T. [2 ]
Juchelova, D. [1 ,3 ]
机构：
[1] Tech Univ Ostrava, ENET Energy Units Utilizat Non Tradit Energy Sour, Ostrava 70833, Czech Republic
[2] So Illinois Univ, Dept Mech Engn & Energy Proc, Carbondale, IL 62901 USA
[3] Tech Univ Ostrava, Fac Mech Engn, Dept Energy, Ostrava 70833, Czech Republic
来源：
PETROLEUM SCIENCE AND TECHNOLOGY | 2014年 / 32卷 / 22期
关键词：
cobalt; HZSM-5; dual-bed; liquid fuels; single reactor; Fischer-Tropsch synthesis; FISCHER-TROPSCH SYNTHESIS; HYDROCARBONS; PERFORMANCE; CATALYSTS; HYDROCRACKING; ZEOLITE;
D O I：
10.1080/10916466.2014.901350
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 effects of HZSM-5 temperature and weight hourly space velocity (WHSV) on conversion of syngas to liquid fuels were investigated in a single reactor process. The temperature of FT catalyst was constant (463K), whereas the temperature of HZSM-5 varied (523, 573, 623K). The value of WHSV ranged between 16 and 24h(-1). HZSM-5 addition suppressed the formation of CH4 and remarkably enhanced the formation of iso-C-5-C-12 paraffins. An increase of HZSM-5 temperature resulted in an enhancement of gaseous hydrocarbons, C18+ paraffins, and olefins. The optimal HZSM-5 temperature and WHSV were identified as 523K and 16h(-1), respectively.
引用
收藏
页码：2722 / 2729
页数：8
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