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Numerical simulation of bubble dispersion in turbulent Taylor-Couette flow

机译:湍流Taylor-Couette流中气泡扩散的数值模拟

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摘要

We investigate bubble dispersion in turbulent Taylor-Couette flow. The aim of this study is to describe the main mechanisms yielding preferential bubble accumulation in near-wall structures of the flow. We first proceed to direct numerical simulation of Taylor-Couette flows for three different geometrical configurations (three radius ratios η = R 1/R 2: η = 0.5, η = 0.72, and η = 0.91 with the outer cylinder at rest) and Reynolds numbers corresponding to turbulent regime ranging from 3000 to 8000. The statistics of the flow are discussed using two different averaging procedures that permit to characterize the mean azimuthal velocity, the Taylor vortices contribution and the small-scale turbulent fluctuations. The simulations are compared and validated with experimental and numerical data from literature. The second part of this study is devoted to bubble dispersion. Bubble accumulation is analyzed by comparing the dispersion obtained with the full turbulent flow field to bubble dispersion occurring at lower Reynolds numbers in previous works. Several patterns of preferential accumulation of bubbles have been observed depending on bubble size and the effect of gravity. For the smaller size considered, bubbles disperse homogeneously throughout the gap, while for the larger size they accumulate along the inner wall for the large gap width (η = 0.5). Varying the intensity of buoyancy yields complex evolution of the bubble spatial distribution. For low gravity effect, bubble entrapment is strong leading to accumulation along the inner wall in outflow regions (streaks of low wall shear stress). When buoyancy effect dominates on vortex trapping, bubbles rise through the vortices, while spiral patterns stretched along the inner cylinder are clearly identified. Force balance is analyzed to identify dominating forces leading to this accumulation and accumulation patterns are compared with previous experiments.
机译:我们研究湍流泰勒-库埃特流中的气泡分散。这项研究的目的是描述在流动的近壁结构中产生优先气泡聚集的主要机理。我们首先对三种不同的几何构造(三个半径比η= R 1 / R 2:η= 0.5,η= 0.72和η= 0.91,外筒处于静止状态)进行泰勒-库埃特流的直接数值模拟,以及雷诺兹数值对应于从3000到8000范围内的湍流状态。使用两种不同的平均程序讨论了流量的统计,这些程序可以表征平均方位角速度,泰勒涡旋贡献和小规模湍流波动。仿真结果与来自文献的实验和数值数据进行了比较和验证。这项研究的第二部分致力于气泡的扩散。通过比较在整个湍流场中获得的弥散度与先前工作中以较低雷诺数发生的气泡弥散度来分析气泡的积累。根据气泡的大小和重力的影响,已经观察到几种气泡优先积累的模式。对于较小的尺寸,气泡会均匀地分散在整个间隙中,而对于较大的尺寸,气泡会沿着内壁积累较大的间隙宽度(η= 0.5)。改变浮力强度会产生气泡空间分布的复杂演变。对于低重力效应,气泡截留力很强,导致沿内壁在流出区域内聚集(壁剪切应力低的条纹)。当浮力作用在旋涡捕获中占主导地位时,气泡会通过旋涡上升,而沿内圆柱伸展的螺旋形则清晰可见。分析力平衡以识别导致这种积累的主导力,并将积累模式与以前的实验进行比较。

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