Non-negligible buoyancy effect on bubbles travelling in horizontal microchannels of comparable size at small Bond numbers

IF 3.6 2区 工程技术 Q1 MECHANICS International Journal of Multiphase Flow Pub Date : 2024-10-10 DOI:10.1016/j.ijmultiphaseflow.2024.105019
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Abstract

When a gas bubble is transported by a liquid flow confined within a horizontal channel of comparable size, buoyancy effects are usually assumed to be negligible if the Bond number of the flow is less than unity. However, recent experimental studies showed that buoyancy may still significantly impact the bubble dynamics even when Bo1, provided that the flow speed is sufficiently small, such that the viscous and inertial forces are weak. To derive a new criterion to assess the significance of buoyancy on the flow of small bubbles in horizontal microchannels, we have performed systematic numerical simulations using the free software Basilisk, covering a wide range of Bond, capillary and Reynolds numbers, Bo=0.0040.4, Ca=1040.5 and Re=0100, and exploring the bubble-to-channel diameter ratios db/D=0.20.9. We demonstrate that the nondimensional group Bo(db/D)2/Ca is effective in assessing the importance of buoyancy in flows with negligible inertial effects. When Bo(db/D)2/Ca<0.1, buoyancy effects are negligible and the bubble travels along the channel axis. When Bo(db/D)2/Ca>10, buoyancy effects dominate and the bubble travels in the vicinity of the upper wall. For intermediate values, bubbles take equilibrium positions between the channel centre and the wall, and the threshold Bo(db/D)2/Ca=1 is effective in predicting whether bubbles will travel closer to the channel centre or to the wall. The capillary number at the denominator describes the lift force generated by the deformation of the bubble due to viscous shear, which acts towards the channel centre thus opposing buoyancy. Inertial forces significantly alter the shape and equilibrium position of the bubble when the Weber number of the flow exceeds unity and Bo/We<1. Under the action of inertia, bubbles of size comparable to the channel diameter become elongated but remain centred. Smaller bubbles migrate towards the channel wall and do not exhibit a preferential near-wall circumferential position.
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在小邦德数条件下,气泡在大小相当的水平微通道中移动时受到的浮力效应不可忽略
当气体气泡被限制在大小相当的水平通道内的液流输送时,如果液流的邦德数小于 1,通常认为浮力效应可以忽略不计。然而,最近的实验研究表明,只要流速足够小,粘滞力和惯性力较弱,即使当邦德数为 1 时,浮力仍会对气泡动力学产生重大影响。为了推导出评估浮力对水平微通道中小气泡流动影响的新标准,我们使用免费软件 Basilisk 进行了系统的数值模拟,涵盖了 Bond、毛细管和雷诺数(Bo=0.004-0.4、Ca=10-4-0.5 和 Re=0-100)的广泛范围,并探讨了气泡与通道直径之比 db/D=0.2-0.9。我们证明,Bo(db/D)2/Ca 这一非线性组能有效评估浮力在惯性效应可忽略不计的流动中的重要性。当 Bo(db/D)2/Ca<0.1 时,浮力效应可忽略不计,气泡沿通道轴线运动。当 Bo(db/D)2/Ca>10 时,浮力效应占主导地位,气泡在上壁附近流动。对于中间值,气泡在通道中心和壁面之间处于平衡位置,阈值 Bo(db/D)2/Ca=1 可以有效预测气泡是靠近通道中心还是靠近壁面。分母处的毛细管数描述了气泡因粘性剪切力变形而产生的升力,该升力作用于通道中心,从而与浮力相反。当水流的韦伯数超过 1 和 Bo/We<1 时,惯性力会明显改变气泡的形状和平衡位置。较小的气泡向通道壁移动,并不表现出靠近壁周的优先位置。
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来源期刊
CiteScore
7.30
自引率
10.50%
发文量
244
审稿时长
4 months
期刊介绍: The International Journal of Multiphase Flow publishes analytical, numerical and experimental articles of lasting interest. The scope of the journal includes all aspects of mass, momentum and energy exchange phenomena among different phases such as occur in disperse flows, gas–liquid and liquid–liquid flows, flows in porous media, boiling, granular flows and others. The journal publishes full papers, brief communications and conference announcements.
期刊最新文献
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