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首页> 外文期刊>Applied thermal engineering: Design, processes, equipment, economics >Heat transfer performance evaluation based on local thermal non-equilibrium for air forced convection in channels filled with metal foam and spherical particles
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Heat transfer performance evaluation based on local thermal non-equilibrium for air forced convection in channels filled with metal foam and spherical particles

机译:基于局部热非平衡的传热性能评价,用于填充金属泡沫和球形颗粒的通道中的空气强制对流

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摘要

A local thermal non-equilibrium heat transfer analysis was conducted for air forced convection in channels filled with metal foam and particles. A general analytical expression was obtained for evaluating Nusselt numbers for the hydro-dynamically and thermal fully developed channel flows subject to constant heat flux, which can be used to investigate heat transfer performances of various porous media under equal pumping power. Such performance evaluations were made for aluminum metal foams of the porosity ranging from 0.85 to 0.95 and the pore diameter to channel half height ratio ranging from 0.01 to 0.20, and also for various packed aluminum particles of the diameter to channel half height ranging from 0.01 to 0.20. It has been found that the conventional local thermal equilibrium model leads to substantial overestimation of Nusselt number in the range of moderate pumping power, especially when the metal foam with large pore diameter is used to fill the channel. The analysis also revealed that in the moderate range of pumping power, the metal foam of comparatively low porosity performs better, while, in the high range of pumping power, the packed bed with large particle diameter gives higher heat transfer performance due to enhanced thermal dispersion.
机译:对填充金属泡沫和颗粒的通道中的空气强制对流进行局部热非平衡传热分析。获得了对经过恒定热通量的水流动态和热完全发育通道流量评估水合物动态和热完全发育通道流量的一般分析表达,其可用于在等于泵送动力下研究各种多孔介质的传热性能。对于孔隙率的铝金属泡沫,孔径为0.85至0.95,孔径为10.01至0.20的孔径,以及用于频道半高度的各种填充铝颗粒的孔径为0.01至0.20。 0.20。已经发现,传统的局部热平衡模型导致中等泵浦功率范围内的露珠数大得多,特别是当使用具有大孔径的金属泡沫来填充通道时。该分析还显示,在适度的泵送动力范围内,相对低的孔隙率的金属泡沫表现得更好,而在高范围的泵送动力中,具有大粒径的填充床由于增强的热分散而导致较高的传热性能。 。

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