Effect of the operation parameters on the Fischer-Tropsch synthesis in fluidized bed reactors

被引:16
|
作者
Zhang, Xiaolai [1 ]
Qian, Weixin [1 ]
Zhang, Haitao [1 ]
Sun, Qiwen [2 ]
Ying, Weiyong [1 ]
机构
[1] East China Univ Sci & Technol, Engn Res Ctr Large Scale Reactor Engn & Technol, State Key Lab Chem Engn, Minist Educ, Shanghai 200237, Peoples R China
[2] State Key Lab Coal Liquefact & Coal Chem Technol, Shanghai 201203, Peoples R China
关键词
Fluidized bed; Fischer-Tropsch synthesis; CFD; HYDROGEN-PERMSELECTIVE MEMBRANE; COLUMN SLURRY REACTOR; GTL TECHNOLOGY; KINETIC-THEORY; FAST PYROLYSIS; MICROCHANNEL REACTOR; GENETIC ALGORITHM; TUBE DIAMETER; GRANULAR FLOW; HEAT-TRANSFER;
D O I
10.1016/j.cjche.2017.05.012
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
For the Fischer-Tropsch synthesis (FTS), this paper presents a numerical investigation in a 3D fluidized bed reactor. The effect of the operation parameters such as bed temperature, superficial gas velocities, particle size and bed heights is discussed. A 3D-CFD model coupled with FTS chemical kinetics was set up. The computational results are compared with experimental data in terms of the components production rates, etc. The analysis shows that the bed heights, the bed temperature, the superficial gas velocities and particle sizes affect the C5+ selectivity and the reaction rates. Product yields are dependent on the operating conditions especially the temperature. (C) 2017 The Chemical Industry and Engineering Society of China, and Chemical Industry Press. All rights reserved.
引用
收藏
页码:245 / 251
页数:7
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