Turbulent Rayleigh-Benard convection of compressed gas: effect of sidewall thermal conductance

被引:6
作者
Srinivasan, V [1 ]
Madanan, U. [2 ]
Goldstein, R. J. [1 ]
机构
[1] Univ Minnesota, Dept Mech Engn, Heat Transfer Lab, Minneapolis, MN 55455 USA
[2] Indian Inst Technol Kanpur, Dept Mech Engn, Expt Thermofluids Lab, Kanpur 208016, Uttar Pradesh, India
关键词
Rayleigh-Benard convection; Nusselt number; Compressed gas experiments; Central-heater-based technique; Aspect ratio; Sidewall conductance; Semi-analytical models; ASPECT RATIO ONE; HEAT-TRANSPORT; NUMBER CONVECTION; CYLINDRICAL CELLS;
D O I
10.1016/j.ijheatmasstransfer.2021.121965
中图分类号
O414.1 [热力学];
学科分类号
摘要
Turbulent Rayleigh-Benard convection is experimentally studied for 1.96 x 10(9) <= Ra <= 1.36 x 10(12) to assess the effect of sidewall thermal conductance on Nusselt numbers and propose a simple yet novel experimental method that eliminates the requirement to correct for this effect. The proposed method relies on power input to a large central-heater located far from the sidewalls for estimating the experimental Nusselt numbers. Experiments are carried out using test cells of varied aspect ratios (width to height, AR (L/H) = 0.61, 1, 2) placed inside a pressure vessel filled with compressed gas. Nusselt numbers obtained using the proposed experimental method are then compared with the sidewall-corrected Nusselt numbers estimated using two semi-analytical models from the literature. This comparison is found to yield a reasonable agreement (to within +/- 8.6%) with both the models. Results from the present study are also presented in the form of a Nusselt number - Rayleigh number relation for the investigated range of parameters. (C) 2021 Elsevier Ltd. All rights reserved.
引用
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页数:9
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