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首页> 外文期刊>International Journal of Heat and Mass Transfer >Investigation of mixed convection heat transfer in a horizontal channel with discrete heat sources at the top and at the bottom
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Investigation of mixed convection heat transfer in a horizontal channel with discrete heat sources at the top and at the bottom

机译:在顶部和底部具有离散热源的水平通道中混合对流传热的研究

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Mixed convection heat transfer from arrays of discrete heat sources inside a horizontal channel has been investigated experimentally. Each of the lower and upper surfaces of the channel was equipped with 8x4 flush mounted heat sources subjected to uniform heat flux. Sidewalls, lower and upper walls are insulated and adiabatic. The experimental parametric study was made for aspect ratios of AR = 2,4 and 10, at various Reynolds and Grashof numbers. From the experimental measurements, row-average surface temperature and Nusselt number distributions of the discrete heat sources were obtained and effects of Reynolds and Grashof numbers on these numbers were investigated. From these results, the buoyancy affected secondary flow and the onset of instability have been discussed. Results show that top and bottom heater surface temperatures increase with increasing Grashof number. The top heater average-surface temperatures for AR = 2 are greater than those of bottom ones. For high values of Grashof numbers where natural convection is the dominant heat transfer regime (Gr~*/Re~2 > > 1), temperatures of top heaters can have much greater values. The variation of the row-average Nusselt numbers for the aspect ratio of AR = 4, show that with the increase in the buoyancy affected secondary flow and the onset of instability, values of Nusselt number level off and even rise as a result of heat transfer enhancement especially for low Reynolds numbers.
机译:实验研究了水平通道内离散热源阵列的混合对流传热。通道的下表面和上表面各装有8x4齐平安装的热源,它们受到均匀的热通量。侧壁,下壁和上壁是隔热且绝热的。在不同的雷诺数和Grashof数下,针对AR = 2,4和10的纵横比进行了实验参数研究。通过实验测量,获得了离散热源的行平均表面温度和Nusselt数分布,并研究了雷诺数和Grashof数对这些数的影响。从这些结果中,已经讨论了浮力影响的次级流量和不稳定的开始。结果表明,顶部和底部加热器表面温度随Grashof数的增加而增加。 AR = 2时,顶部加热器的平均表面温度高于底部加热器的平均表面温度。对于自然对流占主导地位的传热机制(Gr〜* / Re〜2 1)的高Grashof值,顶部加热器的温度可以具有更大的值。 AR = 4的纵横比的行平均Nusselt数的变化表明,随着浮力的增加,影响二次流和不稳定的发生,由于传热,Nusselt数的值趋于平稳甚至上升增强,特别是对于低雷诺数。

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