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Effect of power-law fluid behavior on momentum and heat transfer characteristics of an inclined square cylinder in steady flow regime

机译:幂律流体行为对稳态流动状态下倾斜方筒动量和传热特性的影响

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The governing equations describing the momentum and heat transfer phenomena of power-law non-Newtonian fluids over a heated square cylinder at 45° of incidence in the two-dimensional (2-D) steady flow regime are solved numerically. Extensive results on the detailed structure of the flow and temperature fields as well as on the gross engineering parameters are presented over the following ranges of conditions: 0.2≤n≤1; 0.1≤Re≤40 and 0.7 ≤Pr ≤100. At low Reynolds numbers, the flow remains attached to the surface of the cylinder. This seems to occur for all values of power-law index, at least up to about Re - 1. On the other hand, twin standing vortices were seen to form at Re - 10 for all values of power-law index considered herein. The influence of the Reynolds number and power-law index is delineated on the detailed structure of the flow field (streamlines), wake characteristics and surface pressure distribution as well as on the value of drag coefficients. Similarly, the effect of Prandtl number is studied on forced convective heat transfer for the two commonly encountered boundary conditions, namely, constant temperature or constant heat flux prescribed on the surface of the cylinder. Using the computed numerical results, simple heat transfer correlations are obtained in terms of the Nusselt number as a function of the pertinent governing parameters thereby enabling the prediction of the rate of heat transfer between the fluid and the immersed cylinder. In addition, variation of the local Nusselt number on the surface of the inclined of square cylinder and representative isotherm plots are also presented to elucidate the effect of Reynolds number, Prandtl number and power-law index on the heat transfer phenomenon.
机译:在二维(2-D)稳态流态下,求解了描述幂律非牛顿流体在加热的方筒上以45°入射角入射时的动量和传热现象的控制方程。在以下条件范围内,给出了有关流场和温度场的详细结构以及总工程参数的广泛结果:0.2≤n≤1; 0.1≤Re≤40和0.7≤Pr≤100。在低雷诺数下,流体保持附着在圆柱体表面上。对于幂律指数的所有值似乎都发生了这种情况,至少直到大约Re-1。另一方面,对于此处考虑的幂律指数的所有值,在Re-10处都形成了双股涡旋。雷诺数和幂律指数对流场(流线)的详细结构,尾流特性和表面压力分布以及阻力系数的值都有影响。同样,研究了普兰特数对两种常见边界条件(即圆柱体表面规定的恒定温度或恒定热通量)的强制对流换热的影响。使用计算的数值结果,可以根据努塞尔数作为相关控制参数的函数获得简单的传热相关性,从而可以预测流体与浸入式气缸之间的传热速率。此外,还提出了方形圆柱体斜面上的局部Nusselt数的变化以及代表性的等温线图,以阐明雷诺数,Prandtl数和幂律指数对传热现象的影响。

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