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Experimental Study on Heat Transfer and Friction Factor in Laminar Forced Convection over Flat Tube in Channel Flow

机译:扁管内层流强迫对流换热及摩擦系数的实验研究

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摘要

The heat transfer and fluid flow over a flat tube in the channel with laminar forced convection is experimentally investigated. The experiments were conducted at a flat tube in the flow direction, the five air velocity between 0.2 and1.0 m/s, and Reynolds number based on the hydraulic diameter (ReDh) was considered from 124.5 to 622.5. The uniform heat flux supplies are at the surface of the tube are 354.9, 1016.3 and 1935.8 W/m2 respectively. The experimental results indicate that the average Nusselt numbers View the MathML source for the flat tube increased with increase of ReDh at fixed of the heat flux supply. The View the MathML source increased with an increase of heat flux supply at fixed ReDh. On the other hand, the friction factor decreased with increases of the front free stream velocity. The View the MathML source relationship with ReDh in the power law, theView the MathML source–ReDh correlation was found to be View the MathML source. The correlation achieved good predictions of the measured data with the minimum root mean square value is 99.70%.
机译:实验研究了层流强迫对流通道中扁平管上的热传递和流体流动。实验是在扁平管上沿流动方向进行的,五次风速在0.2至1.0 m / s之间,基于水力直径(ReDh)的雷诺数被认为是从124.5至622.5。管表面的均匀热通量分别为354.9、1016.3和1935.8 W / m2。实验结果表明,在固定热通量的情况下,扁管的平均数随ReDh的增加而增加。固定ReDh时,随着热通量供应的增加,源也增加了。另一方面,摩擦因数随前自由流速度的增加而减小。在幂律中,ReDh与ReDh之间的关系被认为是View MathML源。最小均方根值为99.70%时,相关性对测量数据实现了良好的预测。

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