首页> 外文期刊>Journal of Heat Transfer >Drag Coefficient and Stanton Number Behavior in Fluid Flow Across a Bundle of Wing-Shaped Tubes
【24h】

Drag Coefficient and Stanton Number Behavior in Fluid Flow Across a Bundle of Wing-Shaped Tubes

机译:翼状管束中流体流动的阻力系数和斯坦顿数特性

获取原文
获取原文并翻译 | 示例
       

摘要

Transient numerical simulations of fluid and heat flow were performed for eight heat exchanger segments with cylindrical and wing-shaped tubes in staggered arrangement. Their hydraulic diameters d{sub}h were from 0.5824 to 3.899 cm for the cylindrical tubes, and from 0.5413 to 3.594 cm for the wing-shaped tubes. Based on the recorded time distributions of velocity u{sub}f(t) and temperature T{sub}f(t), time average Reynolds number Rc{top}-, drag coefficient (C{top}-){sub}d, and Stanton number St{top}-were calculated. In general, the drag coefficient and the Stanton number are smaller for the wing-shaped tubes than for the cylindrical tubes. However, with an increasing hydraulic diameter, these differences between both forms of tubes diminish. The time average values were further used to construct the drag coefficient and the Stanton number as polynomial functions (C{top}-){sub}d(d{sub}h,Rc{top}-) and St{top}-(d{sub}h,Rc{top}-).
机译:对交错排列的圆柱形和翼形管的八个热交换器段进行了流体和热流的瞬态数值模拟。对于圆柱管,它们的水力直径d {sub} h为0.5824至3.899 cm,对于翼形管,其水力直径为{d}(0.5413至3.594 cm)。根据记录的速度u {sub} f(t)和温度T {sub} f(t)的时间分布,平均时间雷诺数Rc {top}-,阻力系数(C {top}-){sub} d ,并计算出斯坦顿数St {top}。通常,翼形管的阻力系数和斯坦顿数小于圆柱管。但是,随着水力直径的增加,两种形式的管之间的这些差异将逐渐减小。时间平均值还被用来构造阻力系数和斯坦顿数作为多项式函数(C {top}-){sub} d(d {sub} h,Rc {top}-)和St {top}-( d {sub} h,Rc {top}-)。

著录项

相似文献

  • 外文文献
  • 中文文献
  • 专利
获取原文

客服邮箱:kefu@zhangqiaokeyan.com

京公网安备:11010802029741号 ICP备案号:京ICP备15016152号-6 六维联合信息科技 (北京) 有限公司©版权所有
  • 客服微信

  • 服务号