Hydrocracking of Fischer-Tropsch products. Optimization of diesel and naphtha cuts

被引：0
|
作者：
Teles, U. M. [1 ]
Fernandes, F. A. N. [1 ]
机构：
[1] Univ Fed Ceara, Dept Engn Quim, BR-60455760 Fortaleza, Ceara, Brazil
来源：
CHEMICAL AND BIOCHEMICAL ENGINEERING QUARTERLY | 2008年 / 22卷 / 02期
关键词：
hydrocracking; Fischer-Tropsch; optimization; diesel; naphtha;
D O I：
暂无
中图分类号：
Q81 [生物工程学（生物技术）]; Q93 [微生物学];
学科分类号：
071005 ; 0836 ; 090102 ; 100705 ;
摘要：
Hydrocracking of Fischer-Tropsch synthesis products consisting of a mixture of C-4-C-30 paraffins and olefins over a platinum/amorphous silica-alumina catalyst was analyzed and optimized. A mathematical model of a batch reactor used for hydrocarbon hydrocracking was developed and the process was studied from a modeling point of view based on the kinetics of a bifunctional catalyst. The influence of temperature on the product yield distribution was evaluated. Time and temperature optimization were performed to obtain the best operating conditions to increase the fractions of naphtha and diesel that can be produced by Fischer-Tropsch synthesis.
引用
收藏
页码：227 / 231
页数：5
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