微通道内气-液弹状流动及传质特性研究进展 (Review on flow and mass transfer characteristics of gas-liquid slug flow in microchannels)

Q3 Chemistry
Chaoqun Yao, Jun Yue, Yuchao Zhao, Guangwen Chen, Q. Yuan
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引用次数: 2

摘要

气液段塞流(也称为泰勒流)是一种以细长气泡和液体段塞交替运动为特征的流型。微通道内气液段塞流操作具有易于控制、气泡和段塞尺寸均匀、缩短停留时间分布以及增强径向混合等优点,对增强气液反应具有重要意义。本文综述了微通道内气液段塞流流动和传质特性的基本概念和最新研究进展。总结了气泡的形成机理、相应的气泡和液体长度以及气泡形成过程中的传质。对于微通道主段有规律的段塞流,研究了气泡截面形状和液膜轮廓、槽内液体再循环和泄漏流动、气液传质系数以及物理和化学吸收过程中流动和传质之间的耦合现象等几个重要方面。最后,对该领域未来的研究方向进行了展望。
本文章由计算机程序翻译,如有差异,请以英文原文为准。
微通道内气-液弹状流动及传质特性研究进展 (Review on flow and mass transfer characteristics of gas-liquid slug flow in microchannels)
Gas-liquid slug flow (also termed as Taylor flow) is a flow pattern characterized by the alternate movement of elongated bubbles and liquid slugs. Gas-liquid slug flow operation in microchannels has been found important implications in the enhancement of gas-liquid reactions due to its advantages such as easy control, uniform bubble and slug size, narrowed residence time distribution as well as enhanced radial mixing. This review presents the basic conceptions and recent research progress on flow and mass transfer characteristics during the gas-liquid slug flow in microchannels. The gas bubble formation mechanisms, the corresponding bubble and liquid lengths, and mass transfer during bubble formation are summarized. For regular slug flow in the main section of microchannels, several important aspects are addressed including bubble cross-sectional shape and liquid film profile, internal liquid recirculation and leakage flow through the gutters, gas-liquid mass transfer coefficients and coupling phenomena between flow and mass transfer in physical and chemical absorption processes. Finally, an outlook is given for future research directions in this field.
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来源期刊
Huagong Xuebao/CIESC Journal
Huagong Xuebao/CIESC Journal Chemical Engineering-Chemical Engineering (all)
CiteScore
1.40
自引率
0.00%
发文量
15165
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