幂律流体中气泡上升的数值模拟

Purushotam Kumar, Kai Jin, S. Vanka
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引用次数: 3

摘要

在本文中,我们应用了一种最新发展的数值技术来研究在剪切变薄和剪切增厚的幂律流体中密闭气泡上升的三维动力学。该方法混合了流体体积法和水平集法,并通过求解第二个压力泊松方程(PPE),结合了尖锐表面力法(SSF)来计算表面张力。用液体体积分数方程捕捉气液界面,用几何重建方法对气液界面进行平流。采用水平集和高度函数法计算界面法线和曲率。界面和界面力的精确表示显著地抑制了传统流体体积法和连续表面力(CSF)常见的伪速度。该算法是在一个名为CUFLOW的内部代码中实现的,并在多个gpu平台上运行。我们探讨了流体流变、键数和壁面约束对气泡的瞬态形状、上升速度、上升路径和产生的涡结构的影响。幂律指数从0.25到1.50不等,涵盖剪切减薄和剪切增厚制度。考虑了3种键数(Bo = 2、10和50)和3种约束比(Cr = 4、6和8),并分析了它们对气泡动力学的影响。对于这里检查的参数范围,气泡在剪切变薄流体中的运动被认为是不稳定的,具有显著的形状振荡。气泡在其初次垂直上升的同时,在横截面上作二次运动上升。然而,在牛顿流体和剪切增稠流体中,气泡的形状可以在相对较短的时间内达到稳定状态,并且只与垂直路径有很小的偏差。
本文章由计算机程序翻译,如有差异,请以英文原文为准。
Numerical Simulation of a Gas Bubble Rising in Power-Law Fluids Using a Sharp Surface Force Implementation
In this paper, we have applied a recently-developed numerical technique to study the three-dimensional dynamics of a confined air bubble rising in shear thinning and shear-thickening power-law fluids. The method is a blend of Volume of Fluid and Level Set methods and incorporates a Sharp Surface Force Method (SSF) for surface tension forces by solving a second Pressure Poisson Equation (PPE). The gas-liquid interface is captured by an equation for the liquid volume fraction and advected using the geometry reconstruction method. The interface normal and curvature are computed using level-set and height function methods. The accurate representation of the interface and interfacial forces significantly suppressed the spurious velocities commonly observed with conventional volume of fluid method and the Continuum Surface Force (CSF). The algorithm is implemented in a in-house code called CUFLOW and runs on multiple GPUs platform. We explored the effects of fluid rheology, Bond number, and wall confinement on bubble’s transient shape, rise velocity, rise path, and generated vortex structures. The power-law index is varied from 0.25 to 1.50 covering shear-thinning and shear-thickening regimes. Three Bond numbers (Bo = 2, 10 and 50) and three confinement ratios (Cr = 4, 6 and 8) are considered, and their impacts on bubble’s dynamics are analyzed. For the range of parameters examined here, bubble motion in a shear-thinning fluid is seen to be unsteady with significant shape oscillations. The bubble rises with a secondary motion in the cross-sectional plane along with its primary vertical rise. However, in the Newtonian and shear-thickening fluids, the bubble’s shape is seen to reach a steady-state in a relatively short time and rise with only minor deviations from the vertical path.
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