变粘度和非牛顿流体对多孔介质自然对流传热传质影响的数值解和Taguchi实验方法

K. Tu, K. Yih, Fu-I Chou, J. Chou
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引用次数: 2

摘要

本文采用数值解法和田口法研究了变粘度和非牛顿流体对多孔介质中垂直渗透板自由对流传热传质耦合的影响。表面温度,板的浓度,吹/吸速度均匀。流体的粘度与温度成反比的线性函数。将偏微分方程转化为非相似方程,用凯勒盒法求解。局部努塞尔数和局部舍伍德数的数值结果用5个参数表示:1)吹/吸参数ξ;2)非牛顿流体n的幂律指数;3)浮力比N;4)路易斯数Le;5)粘度变化参数θr。田口法确定局部努塞尔(舍伍德)数最大值的最佳值为6.6328(10.3056)。
本文章由计算机程序翻译,如有差异,请以英文原文为准。
Numerical solution and Taguchi experimental method for variable viscosity and non-Newtonian fluids effects on heat and mass transfer by natural convection in porous media
In this article, both numerical solution and Taguchi method are presented to study the variable viscosity and non-Newtonian fluids effects on coupled heat and mass transfer by free convection over a vertical permeable plate in porous media. The surface temperature, concentration of the plate, and blowing/suction velocity are uniform. The viscosity of the fluid varies inversely as a linear function of the temperature. The partial differential equations are transformed into non-similar equations and solved by Keller box method. Numerical results of the local Nusselt number and local Sherwood number are expressed in the five parameters: 1) blowing/suction parameter ξ; 2) the power-law index of non-Newtonian fluid n; 3) buoyancy ratio N; 4) Lewis number Le; 5) viscosity-variation parameter θr. The best value for confirming the maximum of the local Nusselt (Sherwood) number by the Taguchi method is 6.6328 (10.3056).
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