期刊文献+

管内自由衰减旋流阻力与换热的衰减特性 被引量:2

Friction and Heat Transfer Decaying Characteristics of Free Decaying Swirl Flow in Pipe
下载PDF
导出
摘要 针对管内自由衰减旋流局部流动、阻力及换热特性理论研究的不足,根据流体力学动量矩定理,从理论上推导了管内自由衰减旋流当地最大切向速度、当地阻力系数以及当地换热努塞尔数沿管长衰减的解析式,理论解与试验结果吻合良好.并且揭示:①旋流初始切向速度比越大、雷诺数越小或管壁粗糙度越大,则管内当地最大切向速度、当地阻力系数以及当地换热努塞尔数的衰减也就越快;②管内自由衰减旋流当地阻力系数的衰减要比当地换热努塞尔数的衰减来得迅速。 According to the momentum moment theorem of fluid dynamics, the analytical decaying equations of the local maximum tangential velocity, the local friction factor and the local Nusselt number of the free decaying swirl flow in pipe were obtained. The theoretical equations are in good agreement with the experimental data and show that:(1) if the initial tangential to axial velocity ratio is larger, or the Reynolds number is smaller, or the wall roughness is larger, then the local maximum tangential velocity, the local friction factor and the local Nusselt number decay more rapidly along the axial distance; (2) under the same conditions, the friction factor decays more rapidly than the Nusselt number, and this helps to increase the thermodynamical performance of the enhanced heat transfer of the free decaying swirl flow in a tube.
出处 《上海交通大学学报》 EI CAS CSCD 北大核心 1999年第3期323-325,330,共4页 Journal of Shanghai Jiaotong University
关键词 传热 自由衰减旋流 管内换热 换热 衰减特性 heat transfer free decaying swirl flow in a pipe tangential velocity local friction factor
  • 相关文献

参考文献3

  • 1吴慧英.管内衰减旋流及其复合强化传热的研究[M].南京:东南大学动力系,1997..
  • 2吴慧英,管内衰减旋流及其复合强化传热的研究,1997年
  • 3Chang F,Int J Heat Fluid Flow,1995年,16卷,12期,2175页

共引文献1

同被引文献13

  • 1王杨君,邓先和,洪蒙纳,李志武.管内周期性自旋流强化传热的结构优化[J].化工学报,2006,57(11):2554-2561. 被引量:16
  • 2王杨君,邓先和,李志武,洪蒙纳.旋流片支撑管束的传热与流阻性能[J].化工学报,2007,58(1):21-26. 被引量:13
  • 3Gentery C C. Rod baffle heat exchanger technology [ J ]. Chemical Engineer Progress, 1990,86 ( 7 ) -48-57.
  • 4邓先和,何兆红,周亮.采用旋流片支撑的矩形管束换热器:中国,ZL200720053973.7[P].2008-05-14.
  • 5Sadik Kakac, Ramesh K Shah, Win Aung. Handbook of single phase convective heat transfer [ M ]. New York: John Wiley & Sons, 1987:61-64.
  • 6Webb R L,Eckert E R G. Application of rough surfaces to heat exchanger design [ J ]. International Journal of Heat and Mass Transfer, 1972,15 : 1647-1658.
  • 7Manglik R M,Bergles A E.Heat transfer and pressure drop correlations for twisted-tape inserts in isothermal tubes.Part Ⅰ.Laminar flows[J].ASME J Heat Transfer,1993,115(4):881-889.
  • 8Manglik R M,Bergles A E.Heat transfer and pressure drop correlations for twisted-tape inserts in isothermal tubes.Part Ⅱ.Transition and turbulent flows[J].ASME J Heat Transfer,1993,115(4):890-896.
  • 9Saha S K,Dutta A.Thermohydraulic study of laminar swirl flow through a circular tube fitted with twisted tapes[J].ASME J Heat Transfer,2001,123(1):417-427.
  • 10Shih T H,Liou W W,Shabbir A,et al.A new k-ε eddy viscosity model for high reynolds number turbulent flows model development and validation[J].Computers Fluids,1995,24(3):227-238.

引证文献2

二级引证文献4

相关作者

内容加载中请稍等...

相关机构

内容加载中请稍等...

相关主题

内容加载中请稍等...

浏览历史

内容加载中请稍等...
;
使用帮助 返回顶部