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Mixed convection heat transfer from an in-line row of square cylinders in cross-flow at low Reynolds number

机译:在低雷诺数下,由一排直排的方形圆柱体以对流的混合对流传热

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This article presents a two-dimensional numerical study on the unsteady laminar mixed convection heat transfer from a row of five in-line isothermal square cylinders placed in an unconfined medium and subjected to cross-flow of a Newtonian fluid at low Reynolds number (Re = 125). The hydrodynamic and thermal transport phenomena are captured for the separation ratios (spacing to cylinder size ratio, s/d) of 0.5, 1, 1.5, 2, 3, and 4. The mixed convection heat transfer is studied for Richardson numbers (Ri) ranging from 0 to 3 with a fixed Prandtl number (Pr = 0.71). Numerical calculations are performed by using a PISO algorithm-based finite volume solver in a collocated grid system. The instantaneous vorticity fields along with the isotherm patterns are systematically presented and discussed for different separation ratios and Richardson numbers. Depending on the engineering application, the temperature difference between the surface and the free stream could vary to make buoyancy of primary importance, entailing major modification of the flow field. Additionally, the instantaneous and mean drag and lift coefficients, Strouhal numbers, and mean Nusselt numbers are determined and discussed.
机译:本文提供了二维数值研究,该数值研究了将一排五个直列等温方形圆柱体放置在无侧限介质中并经受低雷诺数牛顿流体的横流的非稳态层流混合对流传热的问题(Re = 125)。对于分离比(间距与圆柱尺寸比,s / d)为0.5、1、1.5、2、3和4的流体动力学和热传输现象进行了捕获。研究了Richardson数(Ri)的混合对流传热范围为0到3,具有固定的Prandtl数(Pr = 0.71)。通过在并置网格系统中使用基于PISO算法的有限体积求解器进行数值计算。针对不同的分离比和理查森数,系统地给出了瞬时涡度场和等温线图。根据工程应用,表面和自由流之间的温差可能会发生变化,从而使浮力成为最重要的问题,这需要对流场进行重大修改。此外,确定并讨论了瞬时和平均阻力和升力系数,斯特劳哈尔数和平均努塞尔数。

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