Heterogeneous catalysis in multi-stage fluidized bed reactors: From fundamental study to industrial application

被引:11
|
作者
Zhang, Chenxi [1 ]
Qian, Weizhong [1 ]
Wang, Yao [1 ]
Luo, Guohua [1 ]
Wei, Fei [1 ]
机构
[1] Tsinghua Univ, Beijing Key Lab Green React Engn & Technol, Dept Chem Engn, Beijing 100084, Peoples R China
来源
关键词
multi-stage fluidized bed reactors; back-mixing; phase separation; heterogeneous catalysis; PRESSURE-DROP; NO REDUCTION; GAS; AROMATICS; METHANOL; TIME; REGENERATION; CONVERSION; COLUMN; RANGE;
D O I
10.1002/cjce.23425
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
The multi-stage fluidized bed (MSFB) reactor with several stages connected in series prevents gas and solids back-mixing effectively and obtains the plug-flow reactor performance. Besides, different process steps can be accomplished in a single reactor by establishing different temperatures and/or concentrations in each stage. Therefore, multi-stage fluidized bed reactors are acknowledged as novel and flexible multi-phase flow reactors for heterogeneous catalytic processes, especially with the intermediates as the desired products. Typical process developments in the industry involve the methanol to aromatics (MTA), regeneration in fluid catalytic cracking (FCC), and hydrogenation of nitrobenzene to aniline. The purpose of this article is to provide a comprehensive review of the fundamental research as well as particular industrial applications on multi-stage fluidized bed reactors in the Fluidization Laboratory of Tsinghua University (FLOTU).
引用
收藏
页码:636 / 644
页数:9
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