A general pressure drop model based on liquid holdup of gas–liquid flow in micro-packed beds

The understanding of the gas−liquid flow characteristics in a micro-packed bed reactor is still immature, especially for many gas−organic working systems commonly used in industry. Accordingly, this study proposes a platform to investigate the gas–liquid flow characteristics in a micro-packed bed re...

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Bibliographic Details
Published inChinese journal of chemical engineering Vol. 76; no. 12; pp. 147 - 156
Main Authors Wang, Junjie, Sheng, Lin, Deng, Jiang, Luo, Guangsheng
Format Journal Article
LanguageEnglish
Published Elsevier B.V 01.12.2024
The State Key Laboratory of Chemical Engineering,Department of Chemical Engineering,Tsinghua University,Beijing 100084,China
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ISSN1004-9541
DOI10.1016/j.cjche.2024.07.022

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