在换热器管道的内壁面上布置丁胞可以有效地增强管道内的传热.通过三维数值模拟,对含丁胞的圆形截面管道内的定常不可压缩湍流流动进行了数值模拟.本文采用RNG k-ε方程模型作为湍流计算模型和SIMPLE算法求解管道的流动传热情况.数值模拟结果表明,丁胞的大小、深度、排列密度等几何结构均对管道的换热效果有一定影响.在较低雷诺数下,含较小丁胞的管道换热效果好于含较大丁胞的管道;在较高雷诺数下,含较大丁胞的管道换热效果好干含较小丁胞的管道.
参考文献
[1] | G. I. Mahmood;M. L. Hill;D. L. Nelson;P. M. Ligrani;H.-K. Moon;B. Glezer .Local Heat Transfer and Flow Structure on and Above a Dimpled Surface in a Channel[J].Journal of turbomachinery,2001(1):115-123. |
[2] | Majumdar D;Amon C H .Oscillatory Momentum Transport Mechanisms in Transitional Complex Geometry Flow[J].Journal of Fluids Engineering,Transactions of the ASME,1997,119(01):29-35. |
[3] | Kesarev V S;Kozlov A P .Convective Heat Transfer in Turbulized Flow Past a Hemispherical Cavity[J].Heat Transfer Research,1994,25(02):156-160. |
[4] | Terekhcv V I;Kalinina S V;Mshvidobadze Y M .Flow Structure and Heat Transfer on a Surface with a Unit Hole Depression[J].Russ J Eng Thermophys,1999,11-33 |
[5] | Burgess N K;Oliveira M M;Ligrani P M.Nusselt Number Behavior on Deep Dimpled Surfaces with a Channel[A].,2002 |
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