Macroscopic turbulent models for heat and mass transfer in catalyst

被引：0

作者：

Mathey, F. ^{[1
]}

机构：

[1] Ctr Rech Claude Delorme Air Liquide, 1 Chemin Porte de Loges, F-78354 Jouy En Josas, France

来源：

THMT-12. PROCEEDINGS OF THE SEVENTH INTERNATIONAL SYMPOSIUM ON TURBULENCE, HEAT AND MASS TRANSFER | 2012年

关键词：

POROUS-MEDIA; PACKED-BED; FLOW; WALL; TRANSPORT; BOUNDARY;

D O I：

10.1615/ICHMT.2012.ProcSevIntSympTurbHeatTransfPal.170

中图分类号：

TH [机械、仪表工业];

学科分类号：

0802 ;

摘要：

This paper reports the development and validation of a Computational Fluid Dynamics (CFD) up-scaling approach to predict wit a porous media approximation the heat transfer efficiency of arbitrary randomly packed bed tubular reactors. The results demonstrate the feasibility to predict the flow, temperature and global heat transfer with macroscopic simulations with a good accuracy.

引用

页码：158 / 167

页数：10

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