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An experimental study of air flow and heat transfer over in-line flat tube bank

机译:直管扁平管束内空气流动和传热的实验研究

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摘要

An experimental study has been made to investigate heat transfer and air flow around flat tube of in-line flat tube banks with laminar forced convection. Measurements were conducted for sixteen tubes in the flow direction;four tubes in the rows, the three air velocity (0.6, 0.8 and 1.0 ms-1) and Reynolds number are ReDh = 527, 703 and 880,where Dh isthe hydraulic diameter of the tube. The total heat flux supplies in all tubes are 967.92, 2258.48 and 3629.70 Wm-2, respectively. The study results indicate that the average Nusselt number of all flat tubes has increased 23.7%-36.7% with Reynolds numbers varying from 527 to 880 at the fixed heat flux; also averageNusselt number has increased11.78% - 23.75% at the heat flux are varying 967.92, 2258.48 and 3629.70 Wm-2, respectively at the Reynolds number Re = 703. In addition, the pressure drop decreaseswith the increase of Reynolds number. The Nusselt number-Reynolds number correlation was found to be 2 1 C Nu  C Re , the correlation yielded good predictions of the measured data with the mean error R2 = 0.992.
机译:已经进行了实验研究,以研究具有层流强制对流的直列扁平管束的扁平管周围的热传递和空气流动。在流动方向上对16个管进行了测量;在排中的四个管中,三个风速(0.6、0.8和1.0 ms-1)和雷诺数分别为ReDh = 527、703和880,其中Dh是管道的水力直径管。所有管中的总热通量分别为967.92、2254.88和3629.70 Wm-2。研究结果表明,在固定热通量下,所有扁管的平均努塞尔数增加了23.7%-36.7%,雷诺数从527变化到880。在雷诺数Re = 703时,热通量的平均努塞尔数也增加了11.78%-23.75%,变化为967.92、2254.88和3629.70 Wm-2。此外,压降随着雷诺数的增加而减小。 Nusselt数与雷诺数的相关性为2 1 C NuCRe,该相关性对测量数据进行了良好的预测,平均误差R2 = 0.992。

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