The influence of pipe length on thermal statistics computed from DNS of turbulent heat transfer

被引:29
作者
Saha, S. [1 ]
Chin, C. [1 ]
Blackburn, H. M. [2 ]
Ooi, A. S. H. [1 ]
机构
[1] Univ Melbourne, Dept Mech Engn, Melbourne, Vic 3010, Australia
[2] Monash Univ, Dept Mech & Aerosp Engn, Clayton, Vic 3800, Australia
关键词
Turbulent heat transfer; Direct numerical simulation; Pipe flow; Prandtl number; DIRECT NUMERICAL-SIMULATION; LARGE-SCALE MOTION; CHANNEL FLOW; PRANDTL NUMBER; BOUNDARY-LAYER; TRANSPORT; REYNOLDS;
D O I
10.1016/j.ijheatfluidflow.2011.09.003
中图分类号
O414.1 [热力学];
学科分类号
摘要
We present results from direct numerical simulation of turbulent heat transfer in pipe flow at a bulk flow Reynolds number of 5000 and Prandtl numbers ranging from 0.025 to 2.0 in order to examine the effect of streamwise pipe length (pi delta pi D/2 <= L <= 12 pi delta) on the convergence of thermal turbulence statistics. Various lower and higher order thermal statistics such as mean temperature, rms of fluctuating temperature, turbulent heat fluxes, two-point auto and cross-correlations, skewness and flatness were computed and it is found that the value of L required for convergence of the statistics depends on the Prandtl number: larger Prandtl numbers requires comparatively shorter pipe length for convergence of most of the thermal statistics. (C) 2011 Elsevier Inc. All rights reserved.
引用
收藏
页码:1083 / 1097
页数:15
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