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Thermophoresis particle deposition on unsteady two-dimensional forced convective heat and mass transfer flow along a wedge with variable viscosity and variable Prandtl number

机译:沿二维非定常二维对流传热和传质沿不定粘度和不定普朗特数的楔形物进行热泳颗粒沉积

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摘要

In this paper, the effects of thermophoresis particle deposition on an unsteady two dimensional forced convective heat and mass transfer flow past a wedge taking into account the variation of fluid viscosity and fluid Prandtl number with temperature are studied. The local similarity equations are derived and solved numerically using Nachtsheim-Swigert shooting iteration technique along with the sixth order Runge-Kutta integration scheme. Comparisons with previously published work are performed, and the results are found to be in excellent agreement Results for the non-dimensional velocity, temperature, concentration, Prandtl number and thermophore-tic velocity are displayed graphically whereas thermophoretic deposition velocity is shown in the tabulated form for various values of the pertinent parameters. The obtained numerical results show that in modeling the thermal boundary-layer flow with a temperature-dependent viscosity, consideration of the Prandtl number as a constant within the boundary layer produces unrealistic results, and therefore, it must be treated as a variable rather than a constant within the boundary layer. The results also show that the thermophoretic particle deposition velocity decreases as the thermophoretic coefficient increases.
机译:在本文中,考虑了流体粘度和流体普朗特数随温度的变化,研究了热泳颗粒沉积对不稳定的二维强迫对流传热和通过楔块的传质的影响。使用Nachtsheim-Swigert射击迭代技术以及六阶Runge-Kutta积分方案,导出并求解了局部相似性方程。与先前发表的工作进行了比较,发现结果非常吻合。无量纲速度,温度,浓度,普朗特数和热泳速度的结果以图形方式显示,而热泳沉积速度以表格形式显示有关参数的各种值。所得的数值结果表明,在对具有温度依赖性粘度的热边界层流进行建模时,将Prandtl数视为边界层内的常数会产生不切实际的结果,因此,必须将其视为变量而不是a边界层内的常数。结果还表明,随着热泳系数的增加,热泳粒子的沉积速度降低。

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