Progress in catalytic naphtha reforming process: A review

被引:207
作者
Rahimpour, Mohammad Reza [1 ,2 ]
Jafari, Mitra [1 ]
Iranshahi, Davood [1 ]
机构
[1] Shiraz Univ, Dept Chem Engn, Sch Chem & Petr Engn, Shiraz 71345, Iran
[2] Univ Calif Davis, Dept Chem Engn & Mat Sci, Davis, CA 95616 USA
关键词
Catalytic naphtha reforming; Catalyst; Kinetic model; Deactivation model; Reactor configuration; BED REACTOR CONCEPT; PT-SN CATALYSTS; HYDROGEN-PRODUCTION; RADIAL-FLOW; COKE FORMATION; OPTIMIZATION APPROACH; ENDOTHERMIC REACTIONS; MEMBRANE REACTOR; KINETIC-MODEL; OCTANE NUMBER;
D O I
10.1016/j.apenergy.2013.03.080
中图分类号
TE [石油、天然气工业]; TK [能源与动力工程];
学科分类号
0807 ; 0820 ;
摘要
Catalytic naphtha reforming process is a vital process for refineries due to the production of high-octane components, which is intensely demanded in our modern life. The significance of this industrial process induced researchers to investigate different aspects of catalytic naphtha reforming process intensively. Some of the investigators try to improve this process by representing more effective catalysts, while others try to elucidate its kinetic and deactivation mechanisms and design more efficient reactor setups. The amount of these established papers is so much that may confuse some of the researchers who want to find collective information about catalytic naphtha reforming process. In the present paper, the published studies from 1949 until now are categorized into three main groups including finding suitable catalyst, revealing appropriate kinetic and deactivation model, and suggesting efficient reactor configuration and mode of operation. These studies are reviewed separately, and a suitable reference is provided for those who want to have access to generalized information about catalytic naphtha reforming process. Finally, various suggestions for revamping the catalytic naphtha reforming process have been proposed as a guideline for further investigations. (c) 2013 Elsevier Ltd. All rights reserved.
引用
收藏
页码:79 / 93
页数:15
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