Bubble breakup and size evolution in turbulent vortex flow

IF 3.9 3区 工程技术 Q2 ENGINEERING, CHEMICAL
Yan Xing , Tao Zhong , Yanping Yao , Xiaokang Yan , Lin Li , Haijun Zhang , Jincai Ran
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Abstract

The size of bubbles exerts a significant impact on flotation efficiency. In the fine particle flotation system, small-sized bubbles are required to facilitate efficient collision and adhesion between fine particles and bubbles. This study employs numerical simulation of single-bubble breakup and high-speed dynamic camera experiments to investigate the mechanism of bubble breakup within the vortex generator and the effect of differently structured vortex tubes on bubble size reduction. The results indicate that the mechanisms facilitating bubble breakup in different regions of the vortex mineralization tube. These include the continuous low-energy vortex effects in the recirculation zone behind the vortex generator, strong strain rates and turbulent kinetic energy at the boundary between the return zone and the main flow region, and the shear obstruction effects on the wall near the vortex generator. Among the tested structures, the rectangular vortex generator exhibits the optimal performance in promoting bubble breakup. At the circulation flow rate of 0.21 m³ /h, the size of bubbles after passing through the rectangular vortex mineralization tube is 31 % of that after passing through a smooth tube. This is attributed to the fact that the rectangular vortex mineralization tube has the highest volume-averaged turbulent kinetic energy, while a continuous low-vorticity vortex region exists behind the vortex generator. This study demonstrates that bubble breakup can be promoted by increasing turbulent kinetic energy and creating local low-vorticity regions, thereby providing a reference for reducing bubble size in flotation processes.
湍流涡旋中气泡破碎与尺寸演化
气泡的大小对浮选效率有重要影响。在细颗粒浮选系统中,为了便于细颗粒与气泡之间的有效碰撞和粘附,需要小尺寸的气泡。本研究采用单泡破碎数值模拟和高速动态相机实验,研究了涡发生器内气泡破碎的机理以及不同结构的涡管对减小气泡尺寸的影响。结果表明,涡旋矿化管不同区域的气泡破碎机制不同。这包括涡发生器后的再循环区内持续的低能涡效应,回流区与主流区边界处的强应变率和湍流动能,以及涡发生器附近壁面上的剪切阻塞效应。在试验结构中,矩形涡发生器对气泡破碎的促进效果最佳。在循环流速为0.21 m³ /h时,通过矩形涡旋矿化管后的气泡大小为通过光滑管后的31 %。这是由于矩形涡化管具有最高的体积平均湍流动能,而涡发生器后存在连续的低涡度涡区。研究表明,增大湍流动能和形成局部低涡度区可以促进气泡破碎,为浮选过程中减小气泡尺寸提供参考。
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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来源期刊
Chemical Engineering Research & Design
Chemical Engineering Research & Design 工程技术-工程:化工
CiteScore
6.10
自引率
7.70%
发文量
623
审稿时长
42 days
期刊介绍: ChERD aims to be the principal international journal for publication of high quality, original papers in chemical engineering. Papers showing how research results can be used in chemical engineering design, and accounts of experimental or theoretical research work bringing new perspectives to established principles, highlighting unsolved problems or indicating directions for future research, are particularly welcome. Contributions that deal with new developments in plant or processes and that can be given quantitative expression are encouraged. The journal is especially interested in papers that extend the boundaries of traditional chemical engineering.
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