水平螺旋管自然对流换热的实验测量

Getnet S. Kidane, A. Fakheri
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引用次数: 0

摘要

实验测量了螺旋盘管的自然对流换热系数,并与水平圆柱的自然对流换热系数进行了比较。研究发现,当盘管节距与管径比小于1.2左右时,盘管的换热系数接近于直径与盘管直径相等的水平圆柱体的换热系数。当P/d比大于1.4时,换热系数接近直径为d的水平圆柱体的换热系数。采用一种改进的特性,即长度,它包含了管径、盘管直径和盘管间距,用于定义努塞尔数和瑞利数。利用所提出的特征长度,可以利用直线水平圆柱体的可用Nusselt和Rayleigh数相关性在实验和可用数据Ra≤105范围内确定水平螺旋管的Nusselt数,最大偏差在15.4%以内。
本文章由计算机程序翻译,如有差异,请以英文原文为准。
Experimental Measurement of the Natural Convection Heat Transfer for Horizontal Helicoidal Pipes
The natural convection heat transfer coefficient for the helicoidal coils are experimentally measured and compared with those for horizontal cylinders. It is found that when the coil pitch to pipe diameter ratio is less than around 1.2, the heat transfer coefficient of the coils approaches that of a horizontal cylinder having a diameter equal to the coil diameter. For the P/d ratio greater than 1.4, the heat transfer coefficient approaches that for horizontal cylinder of diameter d. A modified characteristic, length which incorporates the tube diameter, the coil diameter, and the coil spacing, is used to define Nusselt and Rayleigh numbers. Using the proposed characteristic length, it is shown that the Nusselt number for horizontal helicoidal pipes can be determined using the available Nusselt and Rayleigh number correlation for straight horizontal cylinders in the range of the experimental and available data, Ra ≤ 105, within a maximum deviation of 15.4%.
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