CFD simulation of heat transfer in turbulent pipe flow

被引：13
|
作者：
Dhotre, MT [1 ]
Joshi, JB [1 ]
机构：
[1] Univ Bombay, Inst Chem Technol, Bombay 400019, Maharashtra, India
来源：
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH | 2004年 / 43卷 / 11期
关键词：
D O I：
10.1021/ie0342311
中图分类号：
TQ [化学工业];
学科分类号：
0817 ;
摘要：
In the present work, the flow pattern in pipe flow has been simulated using a low-Reynolds-number k-epsilon model. The model has been extended to predict the heat-transfer coefficient in regions of both high and low Prandtl number. The computational fluid dynamic (CFD) approach has been shown to be superior to the conventional semiempirical approach for high turbulent Prandtl numbers and in cases where the molecular properties such as diffusivity and viscosity steeply change in the vicinity of the wall.
引用
收藏
页码：2816 / 2829
页数：14
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