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Experimental Investigation Of Forced And Mixed Convection Heat Transfer In A Foam-filled Horizontal Rectangular Channel

机译:泡沫水平矩形通道内强迫混合对流换热的实验研究

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An experimental study was performed to investigate the heat transfer characteristics of the mixed convection flow through a horizontal rectangular channel where open-cell metal foams of different pore densities (10,20 and 30 PPI) were situated. A uniform heat flux was applied at all of the bounding walls of the channel. For each of three values of the uniform heat flux, temperatures were measured on the entire surfaces of the walls. Results for the average and local Nusselt numbers are presented as functions of the Reynolds and Richardson numbers. The Reynolds number based on the channel height of the rectangular channel was varied from 600 to 33000, while the Richardson number ranged from 0.02 to 103, extending over forced, mixed and natural convection. Second important parameter that influences the heat transfer is the aspect ratio of the foams. Three different aspect ratios (AR) as 0.25, 0.5 and 1 are tested. Based on the experimental data, new empirical correlations have been constructed to link the Nusselt number. The results of all cases were compared to that of the empty channel and the literature. We found that our results were in agreement with those that are mentioned in the literature.
机译:进行了一项实验研究,以研究混合对流通过水平矩形通道的传热特性,在该矩形通道中放置了具有不同孔密度(10,20和30 PPI)的开孔金属泡沫。在通道的所有边界壁上施加均匀的热通量。对于均匀热通量的三个值中的每个值,在壁的整个表面上测量温度。平均和本地Nusselt数的结果表示为雷诺数和Richardson数的函数。基于矩形通道的通道高度的雷诺数在600到33000之间变化,而Richardson数在0.02到103之间变化,扩展到强制,混合和自然对流。影响传热的第二个重要参数是泡沫的长径比。测试了三种不同的纵横比(AR),分别为0.25、0.5和1。根据实验数据,已经建立了新的经验相关性以链接努塞尔数。将所有病例的结果与空通道和文献的结果进行比较。我们发现我们的结果与文献中提到的结果一致。

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