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Mixed convection of non-Newtonian fluids along a heated vertical flat plate

机译:非牛顿流体沿加热的垂直平板的混合对流

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Mixed convective heat transfer of non-Newtonian fluids on a flat plate has been investigated using a modified power-law viscosity model. This model does not contain physically unrealistic limits of zero or infinite viscosity as are encountered in the boundary-layer formulation with traditional models of viscosity for power-law fluids. These unrealistic limits can introduce an irremovable singularity at the leading edge; consequently, the model is physically incorrect. The present modified model matches well with the measurement of viscosity, and does not introduce irremovable singularities. Therefore, the boundary-layer equations can be solved by marching from the leading edge downstream as for Newtonian fluids. The numerical results are presented for a shear-thinning fluid in terms of the velocity and temperature distribution, and for important physical properties, namely the wall shear stress and heat transfer rates.
机译:已使用修正的幂律粘度模型研究了非牛顿流体在平板上的混合对流传热。该模型不包含在边界层配方中使用幂律流体的传统粘度模型所遇到的物理上不现实的零或无限粘度极限。这些不切实际的局限性可能会在前沿引入不可去除的奇异之处。因此,该模型在物理上是不正确的。本改进的模型与粘度的测量非常匹配,并且不会引入不可去除的奇异性。因此,边界层方程可以通过从牛顿流体的下游前沿进行求解。数值结果针对剪切稀化流体的速度和温度分布以及重要的物理特性(即壁面剪切应力和传热速率)进行了介绍。

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