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正方形截面直通道内二次流现象的实验研究 被引量:4

Experimental Investigation on Secondary Flow of Air-Water Two-Phase Flow in Straight Channel with Square Cross-Section
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摘要 以空气-水为介质,通过可视化实验的方法,对边长为10 mm的正方形截面通道内空气-水垂直上升流动的两相流流型进行了实验研究,表观气速为0.04-100 m/s,表观水速为0.001-6 m/s.观察到了正方形截面通道内两相流动的典型流型,通过管外可视化及内视镜伸入管道内拍摄到清晰的环状流和爬动流流型,证实了正方形截面直通道内存在“二次流”现象,且对气-液两相流动的相分布有较大影响.将正方形截面爬动流与圆通道内的溪状流进行了比较,由于其中的作用力不同,它们在发生条件、流动形态及液膜形状上有很多异同点,圆通道内溪状流的液膜是随机出现和分布的,数条液带、液丝的位置不确定,尺寸相差悬殊.利用单能γ射线传感器测量了正方形通道内爬动流及环状流的液膜厚度,得到壁面上液膜厚度的分布图,证明了正方形通道内随着表观气速的增大,二次流作用逐渐增强,使得壁面上液膜分布的不均匀,壁面中心处液膜最厚. An experimental investigation was conducted on the vertically upward flow of Mr-water twophase in a channel with a square cross-section. The hydraulic diameter of the channel was 10mm; the superficial air velocity was 0. 04-100m/s; the superficial water velocity was 0. 001- 6 m/s. The typical flow patterns, creep flow and rivulet flow, were observed by flow visualization with a DV camera and an endoscope, and the flow pattern map and flow pattern transition boundaries were obtained. The thickness of liquid film of the creep flow and the annular flow in the square channel was measured by a γ-ray instrument. The results show that the mechanism to form the creep flow in the square channel is different from that to form the rivulet flow in a circular tube and a secondary flow exits in the square channel. The phase distribution on the inner wall of the noncircular channel indicates that the influence of the channel geometry results in the steeper radial distribution of the phases and velocities, and eventually turbulent secondary flow. With the increase in the gas velocity, the film thickness at center of the wall is greater than that at corner, indicating the significant effect of the secondary flow on the phase distribution in the noncircular channel.
出处 《西安交通大学学报》 EI CAS CSCD 北大核心 2009年第7期83-87,共5页 Journal of Xi'an Jiaotong University
基金 国家自然科学基金资助项目(50176039)
关键词 正方形截面通道 二次流 爬动流 环状流 相分布 square channel secondary flow creep flow annular flow phase distribution
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参考文献10

  • 1HOAGLAND L C.Turbulent flow in straight rectangular ducts-secondary flow,its cause and effect on the primary flow[D].Boston,Mass.,USA:MIT School of Engineering,1960.
  • 2ALY M,TRUPP A,GERRARD A.Measurements and prediction of fully developed turbulent flow in an equilateral triangular duct[J].J Fluid Mech,1978,85 (1):57-83.
  • 3HUSER A,BIRINGEN S,HATAY F F.Direct simulation of turbulent flow in a square duct:Reynolds-stress budgets[J].Phys Fluids,1994,6(9):3144-3152.
  • 4HIROTA M,FUJITA H,YOKOSAWA H,et al.Turbulent heat transfer in a square duct[J].Int J of Heat and Fluid Flow,1997,18(1):170-180.
  • 5VAZQUEZ M S,METAIS O.Large eddy simulation of the turbulent flow through a heated square duct[J].J Fluid Mech,2002,453:201-238.
  • 6VAZQUEZ MS,RODRIGUEZ W V,ISSA R.Effects of ridged walls on the heat transfer in a heated square duct[J].Int J of Heat and Mass Transfer,2005,48(10):2050-2063.
  • 7W(O)IK G,DREVER M,RATH H J.Flow patterns in small diameter vertical non-circular channels[J].Int J of Multiphase Flow,2000,26(6):1037-1061.
  • 8郭亚军,毕勤成,何永清,周莺,陈听宽.空气-水在垂直非圆截面通道内流型研究[J].核动力工程,2006,27(5):48-52. 被引量:2
  • 9BARAJAS A M,PANTON R L.The Effect of contact angle on two-phase flow in capillary tubes[J].Int J of Multiphase Flow,1993,19(2):337-346.
  • 10HUGHES D T.Minimum thickness of a liquid film flowing down a vertical tube[J].Int J of Multiphase Flow,1998,41(2):253-260.

二级参考文献9

  • 1Aly M, Trupp A, Gerrard A. Measurements and Prediction of Fully Developed Turbulent Flow in an EquilateralTriangular Duct[J]. J. Fluid Mech., 1978, 85( 1): 57 - 83.
  • 2Sadatomi M, Sato Y. Two-phase Flow in Vertical Noncircular Channels[J]. lnt. J. Multiphase Flow, 1982, 8(6):641 - 655.
  • 3Barnea D, Luninski Y, Taitel Y. Flow Pattern in Horizontal and Vertical Two Phase Flow in Small DiameterPipes[J]. Canadian Journal of Chemical Engineering ,1983, 61(3): 617-620.
  • 4W61k G, Drever M, Rath H J. Flow Patterns in Small Diameter Vertical Non-Circular Channels[J]. lnt. J. Mul-tiphaseFlow, 2000, 26: 1037-1061.
  • 5Bi Q C, Zhou Y, Chen T K. Researches on Two-Phase Flow Patterns in Circular and Triangular Channels[C].5th International Conference on Multiphase Flow(1CMF'04), Yokohama Japan, 2004, Paper No. 167.
  • 6Barajas A M, Panton R L. The Effect of Contact Angleon Two-phase Flow in Capillary Tubes[J]. lnt. J. Multi-phase Flow, 1993, 19(2): 337 - 346.
  • 7Hughes D T. Minimum Thickness of a Liquid Film Flowing Down a Vertical Tube[J]. lnt. J. Multiphase Flow,1998, 41(2): 253 - 260.
  • 8Taitel Y, Bamea D, Dukler A E. Modeling Flow Pattern Transitions for Steady Upwards Gas-Liquid Flow in Vertical Tubes [J]. A1ChE J, 1980, 26:345 - 35.
  • 9Zhao T S, Bi Q C. Co-Current Air-Water Two-Phase Flow Patterns in Vertical Triangular Mmicrochannels[J].lnt. J. Multiphase Flow, 2001, 27:765 - 782.

共引文献1

同被引文献41

  • 1薛娟萍,刘明言,强爱红.汽-液流动沸腾蒸发系统的混沌分析及预测[J].高校化学工程学报,2006,20(1):12-17. 被引量:6
  • 2阎维平,李洪涛,叶学民,谷根代.垂直自由下降液膜厚度的瞬时无接触测量研究[J].热能动力工程,2007,22(4):380-384. 被引量:14
  • 3WILLIMARTH T, ISII M. Two-phase flow regime in narrow rectangular vertical and horizontal Channels [J]. International Journal of Heat and Mass Transfer, 1994,37(12) : 1749-1758.
  • 4WILLIMARTH T, ISII M. Interfacial area concentration and void fraction of two-phase flow in narrow rectangular vertical channels[J]. Journal of Fluid Engineering, 1997,119(4) : 916-922.
  • 5TRIPLETT K A, GHIAASIAAN S M. Gas-liquid two-phase flow in microchannels: part II void fraction and pressure drop[J]. International Journal of Multiphase Flow, 1999, 25(11) :395-401.
  • 6WOLK G, DREVER M, RATH H J. Flow patterns in small diameter vertical non-circular channels[J]. International Journal of Multiphase Flow, 2000, 26(6) 1037-1061.
  • 7ZHAO T S, BI Q C. Co-current air-water two-phase pattern in vertical triangular mieroehannels[J]. International Journal of Multiphase Flow, 2001, 27(5) .765 -782.
  • 8SATITCHAICHAROEN P, WONGWISES S. Two- phase flow pattern maps for vertical upward gas-liquid flow in mini-gap channels[J]. International Journal of Multiphase Flow, 2004,30(2)225-236.
  • 9HIBIKI T, TAKAMASA T, ISHII M. Some characteristics of developing bubbly flow in a vertical mini pipe [J]. International Journal of Heat and Fluid Flow, 2007, 28(5)1034-1048.
  • 10KAWAHARA A, SADATOMI M, NEI K, et al. Experimental study on bubble velocity, void fraction and pressure drop for gas-liquid two-phase flow in a circular microchannel[J]. International Journal of Heat and Fluid Flow, 2009,30(5) :831-841.

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