带变形扭带的圆管内紊流强迫对流及换热特性

A. Boonloi, W. Jedsadaratanachai
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引用次数: 11

摘要

本文报道了一种改型扭带圆管换热器的传热、压力损失和热性能评价。在一般扭带上打孔以减少压力损失。在Re = 3000 ~ 10000湍流区,用数值方法研究了孔尺寸(LR = 0.30、0.44、0.78和0.88)和扭比(TR = 1、1.5、2和4)对单扭带和双扭带的影响。本文采用有限体积法和SIMPLE算法进行研究。本文报道了流动结构和换热性能方面的数值结果,并与光滑管和规则扭带进行了比较。结果表明,由于扭曲带所产生的纵向涡旋流,扭曲带比光滑管具有更高的换热率。纵向涡旋流动有助于增加流体混合。扭带的矩形打孔可以减少加热系统的压力损失。在Re = 3000, LR = 0.78, TR = 1时,双捻带和单捻带的最大热增强因子分别在1.39和1.31左右。
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Turbulent Forced Convection and Heat Transfer Characteristic in a Circular Tube with Modified-Twisted Tapes
Heat transfer, pressure loss, and thermal performance assessment in a circular tube heat exchanger with modified-twisted tapes are reported. The rectangular holes are punched out from the general twisted tape to reduce the pressure loss. The influences of the hole sizes (, LR = 0.30, 0.44, 0.78, and 0.88) and twisted ratios (, TR = 1, 1.5, 2, and 4) for the single and double twisted tapes are investigated with a numerical method at turbulent regime, Re = 3000–10,000. The finite volume method and the SIMPLE algorithm are used to investigate for the current research. The numerical results are reported in terms of flow structure and heat transfer behavior and compared with the smooth tube and the regular twisted tape. It is found that the modified-twisted tape provides higher heat transfer rate than the smooth tube due to the longitudinal vortex flows, created by the twisted tape. The longitudinal vortex flows help to increase fluid mixing. The rectangular punched holes of the twisted tape can reduce the pressure loss of the heating system. In addition, the maximum thermal enhancement factor is around 1.39 and 1.31 for the double twisted tape and single twisted tape, respectively, at Re = 3000, LR = 0.78, and TR = 1.
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