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Effects of nonperfect thermal sources in turbulent thermal convection

机译:非完美热源对湍流热对流的影响

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摘要

The effects of the plates thermal properties on the heat transfer in turbulent thermal convection are investigated by direct numerical simulations of the Navier-Stokes equations with the Boussinesq approximation. It has been found that the governing parameter is the ratio of the thermal resistances of the fluid layer R-f and the plates R-p; when this ratio is smaller than a threshold value (R-f/R(p)approximate to300 arbitrarily defined by requiring that the actual heat transfer differs by less than 2% from its ideal value), the finite conductivity of the plates limits the heat transfer in the cell. In addition, since R-f decreases for increasing Rayleigh numbers, any experimental apparatus is characterized by a threshold Rayleigh number that cannot be exceeded if the heat transfer in the cell has not to be influenced by the thermal properties of the plates. It has been also shown that the plate effects cannot be totally corrected by subtracting the temperature drop occurring within the plates from the measured total temperature difference. This is due to the changes produced in the thermal plume dynamics by the reduced local heat flux at the plate/fluid interface. A model with a correction factor has been derived to account for the plates effects and it gave the appropriate correction for a recent experiment in which the heat transfer measurements were systematically smaller than a theoretical prediction. In view of the present correction the discrepancy between theory and experiments addressed by Nikolaenko and Ahlers [Phys. Rev. Lett. 91, 084501 (2003)] can be therefore resolved. The application of the proposed correction to the results in the literature can also reconcile the heat transfer measurements for water and mercury that appear systematically smaller than in other fluids. (C) 2004 American Institute of Physics.
机译:通过用Boussinesq近似对Navier-Stokes方程进行直接数值模拟,研究了板热特性对湍流热对流中热传递的影响。已经发现,控制参数是流体层R-f和板R-p的热阻之比;而流体层R-f和板R-p的热阻之比为0。当该比率小于阈值时(通过要求实际传热与其理想值的差小于2%,Rf / R(p)大约为300任意定义),板的有限电导率限制了细胞。另外,由于R-f减小以增加瑞利数,因此任何实验装置的特征在于阈值瑞利数,如果电池中的传热不必受板的热性能影响,则不能超过该阈值。还已经表明,不能通过从测得的总温差中减去板内出现的温度下降来完全校正板效应。这是由于板/流体界面处的局部热通量减少,从而在热羽动力学中产生了变化。已经推导了具有校正因子的模型来考虑板的影响,并且该模型为最近的实验提供了适当的校正,在该实验中,传热测量值系统地小于理论预测值。鉴于目前的修正,Nikolaenko和Ahlers提出的理论与实验之间的差异[Phys。牧师91,084501(2003)]可以解决。在文献中对结果进行建议的校正也可以使水和汞的传热测量值协调一致,系统地看起来比其他流体中的要小。 (C)2004美国物理研究所。

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