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首页> 外文期刊>Applied thermal engineering: Design, processes, equipment, economics >Numerical study of buoyancy's effect on flow and heat transfer of kerosene in a tiny horizontal square tube at supercritical pressure
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Numerical study of buoyancy's effect on flow and heat transfer of kerosene in a tiny horizontal square tube at supercritical pressure

机译:超临界压力下微型水平方向管中煤油流动和热传递对煤油流动和传热的数值研究

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摘要

The flow and heat transfer characteristics of China No. 3 aviation kerosene (RP-3) flowing in a tiny horizontal square tube at supercritical pressure under gravity are numerically studied, focusing mainly on the secondary flow and buoyancy effects on heat transfer at different flow parameters. The heated length of the tube is 480 mm while the inner length of side is 2 mm. Results indicate that buoyancy will cause secondary flow, and the intensity of secondary flow decreases with mass flow rate and pressure, while increases with volume heat source density. The heat transfer coefficient difference between the walls also decreases with mass flow rate and pressure, while increases with volume heat source density. Temperature of the top wall is higher than that of the bottom wall, while the average heat flux of the top wall is lower than that of the bottom wall. Heat transfer coefficient of the bottom wall is the highest, while that of the top wall is the lowest. Jackson's criterion and Petukhov's criterion were tested to assess the application of the two criteria in the present study. Results indicate that Jackson's criterion can be used to judge the buoyancy effect quantitatively while Petukhov's criterion can not.
机译:在重力下的超临界压力下流动的中国3号航空煤油(RP-3)流动的流动和传热特性进行了数值研究,主要研究了对不同流动参数的传热和浮力影响的二次流动和浮力影响。管的加热长度为480mm,而侧的内部长度为2mm。结果表明,浮力将导致二次流动,二次流量的强度随质量流量和压力降低,而大量的热源密度增加。壁之间的传热系数差异也随质量流量和压力而降低,而具有体积热源密度的增加。顶壁的温度高于底壁的温度,而顶壁的平均热通量低于底壁的热通量。底壁的传热系数是最高的,而顶壁的底壁是最低的。杰克逊的标准和Petukhov的标准进行了测试以评估本研究中的两个标准的应用。结果表明,杰克逊的标准可用于定量判断浮力效果,而Petukhov的标准不能判断浮力效果。

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