• CN:11-2187/TH
  • ISSN:0577-6686

›› 2010, Vol. 46 ›› Issue (16): 162-169.

• 论文 • 上一篇    下一篇

斜截半椭圆柱面涡流发生器强化换热和压降特性的试验研究

叶秋玲;周国兵;程金明;王锡;程伟良   

  1. 华北电力大学能源动力与机械工程学院
  • 发布日期:2010-08-20

Experimental Study of Heat Transfer Enhancement and Pressure Drop Characteristics of Oblique-cut Semi-elliptic Cylinder Shell Vortex Generators

YE Qiuling;ZHOU Guobing;CHENG Jinming;WANG Xi;CHENG Weiliang   

  1. School of Energy Power and Mechanical Engineering, North China Electric Power University
  • Published:2010-08-20

摘要: 在矩形通道内布置一对斜截半椭圆柱面涡流发生器(高宽比h/b=1/2),通过改变斜边倾角、来流攻角β、前沿间距S、布置方式以及顺列、错列两排涡流发生器研究不同工况下的换热和压降特性。试验雷诺数范围为Re=700~26 800。结果表明,在试验条件下 =12°时的换热效果要好于 =20°,Re=1 300时两者的最高局部对流换热系数分别比平直通道高19.7%和10.7%,Re=26 800时分别为23.2%和18.33%。斜截半椭圆柱面涡流发生器( =12°)的最优攻角为β=60º,最优前沿间距为S= 20 mm。当Re=26 800,β=60°,S=20 mm时的最高局部对流换热系数约比平直通道高23.2%,压力损失约比平直通道高33.7%。雷诺数较小时,由于回流滞止区的影响,布置两排涡流发生器后,换热效果反而弱于单排。随着雷诺数增大到4 000,双排涡流发生器的换热效果要明显优于单排,Re=26 800时,最高局部对流换热系数约比单排涡流发生器高14.4%,比平直通道高33.4%。通过试验得出斜截半椭圆柱面涡流发生器在β=60°,=12°时的涡旋作用距离大约在250~300 mm。

关键词: 矩形通道, 强化换热, 试验研究, 涡流发生器, 压降

Abstract: The heat transfer enhancement and pressure drop characteristics of a pair of oblique-cut semi-elliptic cylinder shell vortex generators(aspect ratio h/b= 1/2) in a rectangular channel are experimentally investigated by changing the elevation angle , attack angle β, spacing of the leading-edges S, and the arrangement under various operating conditions. The performance of two rows of in-line and staggered arrayed vortex generators are also investigated. Experimental Reynolds number, Re, ranges from 700 to 26 800. The results indicate that under the present experimental conditions, the heat transfer enhancement of  = 12° is better than that of  = 20° with the highest local convective heat transfer coefficients 19.7% and 10.7% higher than that of the flat channel at Re = 1 300, and 23.2%, 18.33% at Re = 26 800, respectively. The optimal attack angle and spacing of the leading-edges for oblique-cut semi-elliptic cylinder shell vortex generators ( = 12°) are β = 60° and S = 20 mm with the highest local heat transfer coefficient and the pressure drop about 23.2% and 33.7 % higher than the flat channel at Re = 26 800. Due to the effect of the wake region, the heat transfer enhancement of two rows is weaker than the single row at low Reynolds. As the Reynolds number increases up to 4 000, the heat transfer enhancement of two rows is better than the single row with the highest local heat transfer coefficient about 14.4% higher than the single row vortex generators and 33.4% higher than the flat-channel at Re = 26 800. In addition, the results show that the vortices acting distance of oblique-cut semi-elliptic cylinder shell vortex generator is approximately between 250mm and 300 mm at β = 60°,  = 12°.*

Key words: Experimental investigation, Heat transfer enhancement, Pressure drop, Rectangular channel, Vortex generator

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