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Numerical modelling of the rise of Taylor bubbles through a change in pipe diameter

机译:管道直径变化引起泰勒气泡上升的数值模拟

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摘要

The rise of Taylor bubbles through expansions in vertical pipes is modelled using Computational Fluid Dynamics. The predictions from the models are compared against existing experimental work and show good agreement, both quantitatively and qualitatively. Many workers, including the present work, find that, as the bubble passes through the expansion, it will either remain intact or split into one or more daughter bubbles. We find that the critical length of bubble, defined as the maximum length that will pass through intact, is proportional to the cosecant of the angle of the expansion. Further, we show that for an abrupt expansion, the critical bubble length became unaffected by the walls of the upper pipe as the diameter was increased.
机译:使用计算流体动力学模拟泰勒气泡在垂直管道中的膨胀而引起的上升。将模型的预测与现有的实验工作进行比较,从数量和质量上都显示出良好的一致性。许多工人,包括目前的工作,都发现,当气泡通过膨胀时,它将保持原状或分裂成一个或多个子气泡。我们发现气泡的临界长度(定义为将完整通过的最大长度)与膨胀角的余割线成比例。此外,我们表明,对于急剧的膨胀,随着直径的增加,气泡的临界长度不受上管壁的影响。

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