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首页> 外文期刊>Numerical Heat Transfer, Part A. Application: An International Journal of Computation and Methodology >Numerical simulation of steady-state conjugate heat transfer in a circular microtube inside a rectangular substrate
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Numerical simulation of steady-state conjugate heat transfer in a circular microtube inside a rectangular substrate

机译:矩形基板内圆形微管内稳态共轭传热的数值模拟

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摘要

The steady-state heat transfer for laminar flow inside circular microtubes within a rectangular substrate has been investigated. The Reynolds number, Prandtl number, thermal conductivity ratio, and diameter ranges were 1,000 - 1,900, 6.78 - 12.68, 27 - 2,658, and 300 - 1,000 mu m, respectively. Near the entrance, the local Nusselt number varied significantly along the tube periphery. The maximum temperature of the substrate and the outlet temperature of the fluid decreased as the Reynolds number increased. The peripheral average Nusselt number increased with increase of Reynolds number, Prandtl number, solid-to-fluid thermal conductivity ratio, and tube diameter-to-wafer thickness ratio. A correlation for peripheral average Nusselt number was developed.
机译:已经研究了矩形基板内圆形微管内部层流的稳态传热。雷诺数,普朗特数,热导率和直径范围分别为1,000-1,900、6.78-12.68、27-2,658和300-1,000微米。在入口附近,局部Nusselt数沿管子边缘变化很大。衬底的最高温度和流体的出口温度随着雷诺数的增加而降低。外围平均努塞尔数随雷诺数,普朗特数,固液导热系数和管径与晶圆厚度之比的增加而增加。建立了外周平均努塞尔数的相关性。

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