Measurement and Analysis of Bubble Size Distribution in the Electrochemical Stirred Tank Reactor

Raghad S. Mahmood, Alanood A. Alsarayreh, A. Abbas
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Abstract

The dimensions of bubbles were measured in a stirrer tank electrochemical reactor, where the analysis of the bubble size distribution has a substantial impact on the flow dynamics. The high-speed camera and image processing methods were used to obtain a reliable photo. The influence of varied air flow rates (0.3; 0.5; 1 l/min) on BSD was thoroughly investigated. Two types of distributors (cubic and circular) were examined, and the impact of various airflow rates on BSD was investigated in detail. The results showed that the bubbles for the two distributors were between 0.5 and 4.5 mm. For both distributors at each airflow, the Sauter mean diameter for the bubbles was calculated. According to the results, as the flow rate raised, the bubble size for cubic distributors increased from 2.35 to 2.41 mm and for circular distributors from 2.76 to 2.88 mm.
电化学搅拌槽反应器中气泡尺寸分布的测量与分析
在搅拌槽电化学反应器中测量气泡的尺寸,其中气泡尺寸分布的分析对流动动力学有很大影响。为了获得可靠的照片,采用了高速摄像机和图像处理方法。深入研究了不同空气流速(0.3;0.5;1L/min)对BSD的影响。研究了两种类型的分配器(立方体和圆形),并详细研究了不同气流速率对BSD的影响。结果表明,两个分布器的气泡在0.5到4.5mm之间。对于每个气流下的两个分布器,计算了气泡的Sauter平均直径。结果表明,随着流速的增加,立方体分布器的气泡尺寸从2.35毫米增加到2.41毫米,圆形分布器从2.76毫米增加到2.88毫米。
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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