The Simulation of Boiling Heat Transfer in Metal Foam Tube

Article Preview

Abstract:

A three-dimensional physical mode of metal foam tube was built by CFD software. The Brinkman-Forchheimer extended Darcy equation and user-defined function (UFD) of the mass transfer and energy transfer between vapor phase and liquid phase compiled by C language were used in the simulation of boiling heat transfer in metal foam tube. The results show that, at a given mass flow rate, the pressure drop nonlinearly increases as the vapor quality rises; At the low mass flow rate, with the increasing of vapor quality, the flow pattern is transferred to wavy flow from stratified flow and then transfer to stratified wavy flow, while the heat transfer coefficient decreases with the increasing of vapor quality. At the high mass flow rate, with the increasing of vapor quality, the flow pattern is transferred to annular flow from slug flow, while the heat transfer coefficient increases with the increasing of vapor quality. The simulation results agree well with the experimental data.

You might also be interested in these eBooks

Info:

Periodical:

Pages:

3312-3315

Citation:

Online since:

October 2013

Export:

Price:

Permissions CCC:

Permissions PLS:

Сopyright:

© 2014 Trans Tech Publications Ltd. All Rights Reserved

Share:

Citation:

[1] C. Y. Zhao, W Lu, S. A Tassou. Flow Boiling Heat Transfer in Horizontal Metal-Foam Tubes. Journal of Heat Transfer, 2009, 131(12): 121002-8.

DOI: 10.1115/1.3216036

Google Scholar

[2] Brahim Madani, Lounes Tadrist, Frederic Topin. Experimental analysis of upward flow boiling heat transfer in a channel provided with copper metallic foam. Thermal Engineering, 2013, 52: 336-344.

DOI: 10.1016/j.applthermaleng.2012.11.046

Google Scholar

[3] Wei Liu, Aiwu Fan, Xiaoming Huang. Theory and application of heat and mass transfer in porous media. Beijing: Science Press, 2006. (in Chinese).

Google Scholar