微通道内气液两相Taylor流传质行为的体积-流体多相流系统数值研究

IF 3.4 Q1 ENGINEERING, MECHANICAL 国际机械系统动力学学报(英文) Pub Date : 2022-09-28 DOI:10.1002/msd2.12049
Qiuwen Zhong, Zhen Jiao, Wenhui Nie, Yan Li, Ning Gu
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引用次数: 1

摘要

微通道反应器是近年来发展起来的一种创新的微反应系统,是目前最常用的微反应技术。本文通过耦合流体体积模型和物质输运模型,研究了微通道中气液两相泰勒流的传质行为。测定并详细讨论了气体溶质的浓度分布和体积传质系数。仿真结果表明,双循环流动影响了液段塞内的浓度分布。在气泡表面观察到最高值,并沿着气泡的垂直方向迅速下降。气泡速度的增加导致了更明显的下降趋势。气泡的气液界面更新速率随着气泡速度的增加而加快,导致气泡表面各区域的平均传质速率随着气泡速度的增加而增加。结果还表明,液膜面积对气泡传质行为的影响最大,因为液膜在气泡中的传质比例和平均传质速率都最大。
本文章由计算机程序翻译,如有差异,请以英文原文为准。

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Numerical investigation of mass transfer behavior of a gas–liquid two-phase Taylor flow in a microchannel by a volume-of-fluid multiphase flow system

The microchannel reactor is the most commonly used microreaction technology, an innovative reaction system developed in recent years. This study investigates the mass transfer behavior of a gas–liquid two-phase Taylor flow in a microchannel by coupling the volume-of-fluid model and the species transport model. The concentration distribution and the volumetric mass transfer coefficient of the gas solute are determined and discussed in detail. The simulation results reveal that the double-circulation flow influences the concentration distribution in the liquid slug. The highest value is observed at the bubble's surface and decreases rapidly along the vertical direction of the bubble. The increase of bubble velocity leads to a more apparent decreasing trend. The gas–liquid interface renewal rate of the bubble is accelerated with increasing bubble velocity, resulting in an increase in the average mass transfer rate in all regions of the bubble surface with an increase in bubble velocity. The results also indicate that the liquid film area contributes the most to the mass transfer behavior due to the most significant proportion and average mass transfer rate of the liquid film among the bubble.

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