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Formation characteristics of Taylor bubbles in a microchannel with a converging shape mixing junction

机译:Formation characteristics of Taylor bubbles in a microchannel with a converging shape mixing junction

摘要

The bubble formation in a square microchannel with a converging shape mixing junction has been investigated under gas-liquid Taylor flow using a high-speed camera. A typical bubble formation process was found to consist of two steps including the expansion and rupture steps. The bubble length could be approximated as the product of the rupture time and two-phase mixture velocity. Significant influence of liquid viscosity and two-phase mixture velocity on the bubble length was observed, although a linear dependence of the bubble length on gas-liquid flow ratio is present for a given two-phase mixture velocity or liquid viscosity. This indicates that shear stress plays an important role in determining the bubble length in the current microfluidic device even at low Capillary numbers where the squeezing regime is expected to predominate. An empirical correlation expressing the bubble length as a function of gas-liquid flow ratio, liquid viscosity and two-phase mixture velocity was developed to describe the experimental results. The bubble frequency was found to reach a maximum as gas-liquid flow ratio is increased from 0.5 to 1. The cross-sectional shape of Taylor bubble was close to be square at low capillary numbers, which is in agreement with the literature results. (C) 2013 Elsevier B.V. All rights reserved.
机译:使用高速相机在气液泰勒流下研究了具有收敛形状混合结的方形微通道中的气泡形成。发现典型的气泡形成过程包括两个步骤,包括膨胀和破裂步骤。气泡长度可以近似为破裂时间和两相混合物速度的乘积。观察到液体粘度和两相混合物速度对气泡长度的显着影响,尽管对于给定的两相混合物速度或液体粘度,气泡长度对气液流量比存在线性关系。这表明剪切应力在确定当前微流体装置中的气泡长度中起着重要的作用,即使在毛细管状态较低的情况下,也预期挤压状态将占主导地位。建立了表示气泡长度与气液流量比,液体粘度和两相混合物速度的函数的经验关系式,以描述实验结果。随着气液流量比从0.5增加到1,气泡频率达到最大。泰勒气泡的横截面形状在低毛细管数下接近方形,这与文献结果相符。 (C)2013 Elsevier B.V.保留所有权利。

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