华南理工大学学报(自然科学版) ›› 2008, Vol. 36 ›› Issue (11): 17-21,26.

• 化学化工 • 上一篇    下一篇

高扭曲比螺旋扁管的管内传热及流阻性能

高学农 邹华春 王端阳 陆应生   

  1. 华南理工大学 传热强化与过程节能教育部重点实验室, 广东 广州 510640
  • 收稿日期:2007-11-02 修回日期:2008-04-21 出版日期:2008-11-25 发布日期:2008-11-25
  • 通信作者: 高学农(1969-),男,博士,副教授,主要从事传热强化和节能研究. E-mail:cexngao@scut.edu.cn
  • 作者简介:高学农(1969-),男,博士,副教授,主要从事传热强化和节能研究.
  • 基金资助:

    广东省科技攻关项目(2004810201008)

Heat Transfer and Flow Resistance Properties in Twisted Oblate Tube with Large Twist Ratio

Gao Xue-nong  Zou Hua-chun  Wang Duan-yang  Lu Ying-sheng     

  1.  Key Laboratory of Enhanced Heat Transfer and Energy Conservation of the Ministry of Education, South China University of Technology, Guangzhou 510640, Guangdong, China
  • Received:2007-11-02 Revised:2008-04-21 Online:2008-11-25 Published:2008-11-25
  • Contact: 高学农(1969-),男,博士,副教授,主要从事传热强化和节能研究. E-mail:cexngao@scut.edu.cn
  • About author:高学农(1969-),男,博士,副教授,主要从事传热强化和节能研究.
  • Supported by:

    广东省科技攻关项目(2004810201008)

摘要: 以水为介质,研究了不同截面短长轴比(B/A=0.27~0.47)和扭曲比(即导程与直径比,S/de=17.19—50.62)的高扭曲比螺旋扁管的管内传热和流阻性能.实验结果表明:高扭曲比螺旋扁管的管内努塞尔数和阻力系数均随B/A值和S/de值的增大而减小,但随B/A值的增加而减小得更快,B/A值对高扭曲比螺旋扁管的管内传热与流阻性能影响更大;在相同雷诺数和普朗特数下,高扭曲比螺旋扁管管内的努塞尔数为光滑管的1.3~2.5倍;阻力系数为光滑管的1.2~1.5倍.文中还通过多元线性回归法对实验数据进行了分析,提出了高扭曲比螺旋扁管管内努塞尔数和阻力系数的准数方程式,其最大误差分别是12%和6%,从而为该类型螺旋扁管换热器的工程设计提供了依据.

关键词: 螺旋扁管, 传热强化, 流阻, 扭曲比

Abstract:

Water was used as a working medium to investigate the internal heat transfer and flow resistance properties of the twisted tube with large twist ratio in the conditions of variable short-long diameter ratio ( B/A = 0. 27- 0.47) and twist ratio (the lead-to-diameter ratio, S/de = 17.19 - 50.62). Experimental results indicate that the B/A value greatly affects the internal Nusselt number and friction factor of the twisted tube because the parameters decrease with the increase of B/A and S/de values, more rapidly with the former, and that the Nusseh number and friction factor of the twisted oblate tube increase respectively by 30% - 150% and 20% - 50% , as compared with those of the smooth tube at the same Reynolds number and Prandtl number. Moreover, the formulae of Nusselt number and friction factor of the twisted oblate tube with large twist ratio are both deduced based on the multiple linear regression of experimental data, the maximum errors of which being respectively 12% and 6%. The proposed formulae lay a foundation for the design of heat exchanger with twisted oblate tubes.

Key words: twisted oblate tube, heat transfer enhancement, flow resistance, twist ratio