湍流
机械
管道流量
雷诺数
明渠流量
直接数值模拟
物理
湍流动能
偏斜
雷诺应力
平均流量
流量调节
奇兹公式
流量(数学)
旋转对称性
塞流
平坦度(宇宙学)
Kε湍流模型
计算机模拟
能量(信号处理)
频道(广播)
二次流
流速
流量测量
经典力学
流体力学
流动分离
湍流模型
作者
J. G. M. Eggels,F. Unger,Marvin H. Weiss,Jerry Westerweel,Ronald J. Adrian,Rainer Friedrich,F. T. M. Nieuwstadt
标识
DOI:10.1017/s002211209400131x
摘要
Direct numerical simulations (DNS) and experiments are carried out to study fully developed turbulent pipe flow at Reynolds number Re c ≈ 7000 based on centreline velocity and pipe diameter. The agreement between numerical and experimental results is excellent for the lower-order statistics (mean flow and turbulence intensities) and reasonably good for the higher-order statistics (skewness and flatness factors). To investigate the differences between fully developed turbulent flow in an axisymmetric pipe and a plane channel geometry, the present DNS results are compared to those obtained from a channel flow simulation. Beside the mean flow properties and turbulence statistics up to fourth order, the energy budgets of the Reynolds-stress components are computed and compared. The present results show that the mean velocity profile in the pipe fails to conform to the accepted law of the wall, in contrast to the channel flow. This confirms earlier observations reported in the literature. The statistics on fluctuating velocities, including the energy budgets of the Reynolds stresses, appear to be less affected by the axisymmetric pipe geometry. Only the skewness factor of the normal-to-the-wall velocity fluctuations differs in the pipe flow compared to the channel flow. The energy budgets illustrate that the normal-to-the-wall velocity fluctuations in the pipe are altered owing to a different ‘impingement’ or ‘splatting’ mechanism close to the curved wall.
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