Experimental investigation and analysis for the bubble size distribution during alkaline water electrolysis by using a wire electrode

Yang Liu , Shuang Li , Honglu Wu , Yixiang Shi
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Abstract

The determination of bubble size distribution is a prerequisite for the study of gas-liquid two-phase flow characteristics in electrolytic cells. Here the departure diameter of hydrogen bubbles and oxygen bubbles and their detachment process from a nickel wire electrode during water electrolysis are studied using high-speed photography. The results show that in industrial alkaline environment, the departure diameters of most hydrogen bubbles and oxygen bubbles are generally smaller than 60 ​μm and 250 ​μm with the current density ranges from 0.15 to 0.35 ​A/cm2. The adhesion force of hydrogen bubbles on a nickel wire is found to be so weak that they can separate with a tiny size. The diameters of oxygen bubbles conform to normal distribution, and its distribution range widens with the increase of current density. The theoretical analysis show that the comprehensive conversion rate of current-to-bubble is unexpectedly low especially at low current densities, which may be attributed to the loss of gas components caused by bubble detachment mode. The majority of oxygen bubbles detach by a sudden bounce after coalescence, which may bring strong disturbance to the concentration boundary layer. This also indicates the coalescence-induced bubble departure mode may occupy a dominant position in the electrolyzers.

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利用线电极对碱性水电解过程中的气泡大小分布进行实验研究和分析
测定气泡大小分布是研究电解槽中气液两相流动特性的先决条件。本文利用高速摄影技术研究了水电解过程中氢气泡和氧气泡的离去直径及其从镍丝电极上脱离的过程。结果表明,在工业碱性环境中,电流密度为 0.15 至 0.35 A/cm2 时,大多数氢气泡和氧气泡的离开直径一般小于 60 μm 和 250 μm。氢气泡在镍丝上的附着力非常弱,以至于它们能以极小的尺寸分离。氧气泡的直径呈正态分布,其分布范围随着电流密度的增加而扩大。理论分析表明,电流到气泡的综合转换率出乎意料地低,尤其是在低电流密度下,这可能是由于气泡分离模式造成的气体成分损失。大部分氧气泡在凝聚后会突然反弹脱离,这可能会对浓度边界层造成强烈扰动。这也表明凝聚引起的气泡脱离模式可能在电解槽中占据主导地位。
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