Numerical Study of Forced Convection Flow Around Rectangular Cylinders with Different Aspect Ratios

A. Joda, I. Cuesta, A. Vernet
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引用次数: 14

Abstract

The unsteady two-dimensional forced convection heat transfer and fluid flow around rectangular cylinders are investigated numerically. A range of Reynolds number between 100 to 200 and aspect ratios (H/D) 1, 2 and 3 are considered. In the present work, a fractional step finite volume code with staggered variables arrangement is used to solve Navier-Stokes and energy equations. A second order central differencing scheme is applied for both diffusion and convection terms. Time advancement is discretized using a second order implicit Cranck-Nicolson scheme. At the outlet of the domain the convective boundary condition is applied for the velocities and the temperature. The computed results of drag and lift coefficients, Strouhal number, mean recirculation length and Nusselt numbers of the square cylinder are found to be in good agreement with previous numerical results. Correlations between the cylinder Nusselt number and Reynolds number are presented for H/D= 2 and 3. In addition, a correlation of heat transfer is proposed as a function of Reynolds number and the aspect ratio (H/D)
不同长径比矩形圆柱绕流强迫对流的数值研究
对非定常二维强制对流换热和矩形圆柱周围流体流动进行了数值研究。考虑了雷诺数在100到200之间的范围和纵横比(H/D) 1、2和3。本文采用交错变量排列的分数阶有限体积码来求解Navier-Stokes方程和能量方程。扩散项和对流项均采用二阶中心差分格式。采用二阶隐式Cranck-Nicolson格式对时间推进进行离散化。在区域的出口处,对速度和温度采用对流边界条件。计算得到的阻力系数、升力系数、斯特劳哈尔数、平均循环长度和努塞尔数与前人的计算结果吻合较好。给出了H/D= 2和3时圆柱努塞尔数与雷诺数的相关关系。此外,还提出了传热与雷诺数和展弦比(H/D)的关系。
本文章由计算机程序翻译,如有差异,请以英文原文为准。
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