期刊
CHEMICAL ENGINEERING & TECHNOLOGY
卷 35, 期 2, 页码 369-378出版社
WILEY-V C H VERLAG GMBH
DOI: 10.1002/ceat.201100615
关键词
Cobalt catalyst; Fischer-Tropsch synthesis; Fixed-bed reactor; Reactor modeling
Simulation of a single tube of a wall-cooled multitubular Fischer-Tropsch (FT) reactor with a cobalt catalyst indicates that the reactor performance is improved by enlarging the catalyst particle diameter. This aspect is studied for variation of the particle size for a fixed tube diameter and vice versa. For a syngas conversion per pass of about 30?% as target and a typical industrially used single-tube diameter of 40?mm, a particle size of >?3?mm is appropriate with regard to a high production rate of higher hydrocarbons. For a particle diameter of
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