Accumulation of liquid hydrocarbons in catalyst pores during cobalt-catalyzed Fischer-Tropsch synthesis

被引:27
|
作者
Poehlmann, F. [1 ]
Kern, C. [1 ]
Roessler, S. [1 ]
Jess, A. [1 ]
机构
[1] Univ Bayreuth, Chair Chem Engn, Ctr Energy Technol, Univ Str 30, D-95440 Bayreuth, Germany
关键词
VAPORIZATION ENTHALPIES; VAPOR-PRESSURES; T=298.15 K; N-ALKANES; DIFFUSION; KINETICS; SELECTIVITY; PREDICTION;
D O I
10.1039/c6cy00941g
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
In the literature, it is widely claimed that during the initial period of Fischer-Tropsch synthesis liquid higher hydrocarbons fill catalyst pores completely, at least at temperatures of less than 250 degrees C at a typical pressure of about 2 MPa. This leads to diffusional restrictions in the porous network for particles with a size appropriate for industrial fixed-bed operation (>1 mm), whereby catalyst effectiveness and product selectivity are strongly affected. However, under industrially relevant reaction conditions, our experimental and theoretical investigations on the interplay of reaction and diffusion in cobalt catalyst particles reveal that the pores are only partly filled with liquid higher hydrocarbons even at a very long time on stream of months or more for a chain growth probability of below about 0.8. Experiments were conducted in a magnetic suspension balance using particles of so called "technical" size (in the regime of 1-3 mm, relevant for industrial application), and a mathematical model was developed describing quite accurately the formation, vaporization and accumulation of liquid products and their C-number distribution in the porous particle.
引用
收藏
页码:6593 / 6604
页数:12
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