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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 被引量:19

Experimental Study of Heat Transfer Enhancement and Pressure Drop Characteristics of Oblique-cut Semi-elliptic Cylinder Shell Vortex Generators
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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α、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=700~26800。结果表明,在试验条件下α=12°时的换热效果要好于α=20°,Re=1300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=26800时分别为23.2%和18.33%。斜截半椭圆柱面涡流发生器(α=12°)的最优攻角为β=60o,最优前沿间距为S=20mm。当Re=26800,β=60°,S=20mm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4000,双排涡流发生器的换热效果要明显优于单排,Re=26800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°,α=12°时的涡旋作用距离大约在250~300mm。 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 α,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 α = 12° is better than that of α = 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(α = 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°,α = 12°.
出处 《机械工程学报》 EI CAS CSCD 北大核心 2010年第16期162-169,共8页 Journal of Mechanical Engineering
基金 高等学校博士学科点专项科研基金(20070079018) 河北省自然科学基金(E2008001231) 北京市'供热 供燃气 通风及空调工程'重点实验室开放课题(KF200708) 电力青年科技创新(2008)资助项目
关键词 涡流发生器 强化换热 压降 矩形通道 试验研究 Vortex generator Heat transfer enhancement Pressure drop Rectangular channel Experimental investigation
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  • 1GENTRY M C, JACOBI A M. Heat transfer enhancement by delta-wing vortex generators on a fiat plate: vortex interactions with the boundary layer [J]. Experimental Thermal and Fluid Science, 1997, 14(3): 231-242. 被引量:1
  • 2PESTEEI S M, SUBBARAO P M V, AGARWAL R S. Experimental study of the effect of winglet location on heat transfer enhancement and pressure drop in fin-tube heat exchangers [J]. Applied Thermal Engineering, 2005, 25(11-12): 1 684-1 696. 被引量:1
  • 3CHU P, HE Y L, LEI Y G, et al. Threedimensional numerical study on fin-and-oval-tube heat exchanger with longitudinal vortex generators[J]. Applied Thermal Engineering, 2009, 29(5-6): 859-876. 被引量:1
  • 4MOKRANI A, CASTELAIN C, PEERHOSSAINI H. Experimental study of the influence of the rows of vortex generators on turbulence structure in a tube[J]. Chemical Engineering and Processing, 2009, 48(2): 659-671. 被引量:1
  • 5VALENCIA A. Heat transfer enhancement due to self-sustained oscillating transverse vortices in channels with periodically mounted rectangular bars [J]. International Journal of Heat and Mass Transfer, 1999, 42(11): 2 053-2 062. 被引量:1
  • 6陈秋炀,曾敏,王令,王秋旺,周砚耕,黄彦平,肖泽军.纵向涡发生器对矩形窄通道内对流换热的影响[J].西安交通大学学报,2006,40(9):1010-1013. 被引量:10
  • 7王令,黄军,王秋旺,黄彦平.带周期性分布纵向涡发生器的矩形狭窄通道内传热流动的数值模拟[J].核动力工程,2007,28(3):27-31. 被引量:2
  • 8KWAK K M, TORII K, NISHINO K. Simultaneous heat transfer enhancement and pressure loss reduction for finned-tube bundles with the first or two transverse rows of built-in winglets [J]. Experimental Thermal and Fluid Science, 2005; 29(3): 625-632. 被引量:1
  • 9张永恒,王良璧,杨世春.涡产生器结构参数对管片式换热器局部传热特性的影响[J].化工学报,2003,54(3):294-298. 被引量:7
  • 10CHEN Y, FIEBIG M, MITRA N K. Conjugate heat transfer of a finned oval tube with a punched longitudinal vortex generator in form of a delta winglet-parametric investigation of the winglet [J]. International Journal of Heat and Mass Transfer, 1998, 41(23): 3 961-3 978. 被引量:1

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