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机构地区:[1]北京科技大学机械工程学院,北京100083 [2]中国科学院工程热物理研究所,北京100190 [3]中国科学院研究生院,北京100190
出 处:《北京科技大学学报》2010年第3期384-389,共6页Journal of University of Science and Technology Beijing
摘 要:采用Delaunay三角化方法对计算区域进行网格划分,开发了适合于非结构化网格的蒙特卡洛直接模拟程序,并对程序的正确性进行了验证.在此基础上模拟分析了粗糙元为三角形的平行平板间微通道内稀薄气体的二维流动与换热.通道进出口压力固定,上下平板温度恒定.计算分析了粗糙元高度、宽度以及分布密度的影响.结果表明:微通道内粗糙元对流动与换热有明显的扰动;随着粗糙元的变大,速度跳跃显著,甚至出现漩涡,增加了通道内的压力损失;但粗糙元增强了微通道壁面与气体之间的换热.The computational domain was meshed by Delaunay triangulation method.A Monte Carlo direct simulation program was developed for unstructured grids and its validity was checked.On that case,the two-dimensional flow and heat transfer of rarefied gas in parallel plate micro-channels with triangular roughness elements were simulated.The pressure of the micro-channels' inlet and outlet and the temperature of the plates above and below were constant.The influences of the height,width and distribution density of roughness elements were computed and analyzed.The results show that roughness elements in the micro-channels can create obvious disturbance for the flow and heat transfer.The greater the roughness elements,the more visible the oscillation of velocity,even vortexes occur,which increases the pressure loss;but roughness elements can enhance the heat transfer.
分 类 号:TK124[动力工程及工程热物理—工程热物理]
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