Process intensification in gas/liquid/solid reaction in trickle bed reactors: A review

被引:13
作者
Tan, Jing [1 ]
Ji, Ya-Ni [1 ]
Deng, Wen-Sheng [1 ]
Su, Yue-Feng [2 ]
机构
[1] Beijing Inst Technol, Sch Chem & Chem Engn, Beijing 100081, Peoples R China
[2] Beijing Inst Technol, Sch Mat Sci & Engn, Beijing Key Lab Environm Sci & Engn, Beijing 100081, Peoples R China
基金
中国国家自然科学基金;
关键词
Trickle bed reactor; Process intensification; Gas; liquid; solid catalytic reaction; Petroleum industry; ORGANIC SULFUR-COMPOUNDS; POROUS-MEDIA MODEL; SELECTIVE HYDROGENATION; CATALYTIC-HYDROGENATION; PACKED-BED; OXIDATIVE DESULFURIZATION; MASS-TRANSFER; 2-PHASE FLOW; HIGHLY EFFICIENT; LIQUID HOLDUP;
D O I
10.1016/j.petsci.2021.07.007
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
As an important form of reactors for gas/liquid/solid catalytic reaction, trickle bed reactors (TBRs) are widely applied in petroleum industry, biochemical, fine chemical and pharmaceutical industries because of their flexibility, simplicity of operation and high throughput. However, TBRs also show inefficient production and hot pots caused by non-uniform fluid distribution and incomplete wetting of the catalyst, which limit their further application in chemical industry. Also, process intensification in TBRs is necessary as the decrease in quality of processed crude oil, caused by increased exploitation depths, and more restrictive environmental regulations and emission standards for industry, caused by increased environment protection consciousness. In recent years, lots of strategies for process intensification in TBRs have been proposed to improve reaction performance to meet the current and future demands of chemical industry from the environmental and economic perspective. This article summarizes the recent progress in techniques for intensifying gas/liquid/solid reaction in TBRs and application of intensified TBRs in petroleum industry. (c) 2021 The Authors. Publishing services by Elsevier B.V. on behalf of KeAi Communications Co. Ltd. This is an open access article under the CC BY-NC-ND license (http://creativecommons.org/licenses/by-nc-nd/ 4.0/).
引用
收藏
页码:1203 / 1218
页数:16
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