Modeling of Fischer-Tropsch products hydrocracking

被引:44
作者
Pellegrini, L [1 ]
Locatelli, S
Rasella, S
Bonomi, S
Calemma, V
机构
[1] Politecn Milan, Dept Chem Mat & Chem Engn, I-20133 Milan, Italy
[2] EniTecnol, Milan, Italy
关键词
hydrocracking; kinetics; multiphase reactors; catalysis; adsorption; modeling;
D O I
10.1016/j.ces.2004.08.027
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
The hydrocracking behavior of a C-4-C-70 mixture of n-paraffins on a platinum/amorphous silica-alumina catalyst has been analyzed. The influence on the system behavior of operating conditions, i.e. pressure, temperature, H-2/feed ratio and stream velocity, has been investigated by means of experimental data from a bench scale reactor, the last aim being the derivation of a proper model for the reaction system. Because of the high number of species involved, a model which takes into account pseudocomponents (lumped model) corresponding to the cuts of interest for the refinery has been considered. The obtained results show good agreement with experimental data. (C) 2004 Elsevier Ltd. All rights reserved.
引用
收藏
页码:4781 / 4787
页数:7
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