4.4 Article

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

期刊

CANADIAN JOURNAL OF CHEMICAL ENGINEERING
卷 97, 期 3, 页码 636-644

出版社

WILEY
DOI: 10.1002/cjce.23425

关键词

multi-stage fluidized bed reactors; back-mixing; phase separation; heterogeneous catalysis

资金

  1. National Key Research and Development Program of China [2018YFB0604801]

向作者/读者索取更多资源

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).

作者

我是这篇论文的作者
点击您的名字以认领此论文并将其添加到您的个人资料中。

评论

主要评分

4.4
评分不足

次要评分

新颖性
-
重要性
-
科学严谨性
-
评价这篇论文

推荐

暂无数据
暂无数据