Strong wall and transverse size effects on pressure drop of flow through open-cell metal foam

Abstract In applications where a fluid flows through the open pores of metal foam, the foam is treated as an infinite porous medium for which the Darcy law and the Forchheimer equation are applied, in order to describe the pressure drop and to obtain the permeability and form drag coefficient. However, in many practical applications the foam is confined, and depending on the transverse size of the foam (perpendicular to the flow direction), the confining walls and the size may have a strong effect on the velocity field and the resulting pressure drop and its behavior. Actually, for small confined foam size, the above flow relations may not be applicable, or they may require modifications in order to account for the added pressure drop due to the confining walls and size effects. Little or no attention has been paid to the transverse size of the foam perpendicular to the confining wall, which may explain some of the divergence in reported pressure drop in the literature. For confined cylindrical foam systems, this paper experimentally establishes a minimum diameter necessary for the foam to have diameter-independent pressure drop, i.e., negligible wall and size effects and constant permeability and form drag coefficient. This minimum diameter is obtained for two types of open-cell aluminum foam subjected to fully-developed airflow in the Forchheimer regime. Below this diameter, values of the two key flow properties show strong dependence on diameter. The Reynolds number ranged from approximately 15,000 to 115,000, and the foam diameters ranged from five to forty five cells for 10- and 20- pore per inch aluminum foam. The intertwined wall and size effect is isolated and studied.

[1]  Zhenmin Cheng,et al.  Estimating radial velocity of fixed beds with low tube‐to‐particle diameter ratios , 1997 .

[2]  J. Bear Dynamics of Fluids in Porous Media , 1975 .

[3]  W. Soboyejo,et al.  An investigation of the microstructure and strength of open-cell 6101 aluminum foams , 2002 .

[4]  Byung Ha Kang,et al.  Flow and heat transfer correlations for porous fin in a plate-fin heat exchanger , 2000 .

[5]  Kye-Bock Lee,et al.  Pressure loss and forced convective heat transfer in an annulus filled with aluminum foam , 2006 .

[6]  W. Roberts,et al.  A study on pressure drop and heat transfer in open cell metal foams for jet engine applications , 2007 .

[7]  D. E. Beasley,et al.  Theory and design for mechanical measurements , 1991 .

[8]  Donald C. Price,et al.  Experimental Determination of Permeability and Inertia Coefficients of Mechanically Compressed Aluminum Porous Matrices , 1997 .

[9]  D. Poulikakos,et al.  The Effects of Compression and Pore Size Variations on the Liquid Flow Characteristics in Metal Foams , 2002 .

[10]  J. P. Du Plessis,et al.  Pressure drop modelling in cellular metallic foams , 2002 .

[11]  K. Schnitzlein,et al.  The influence of confining walls on the pressure drop in packed beds , 2001 .

[12]  Jenn-Jiang Hwang,et al.  Measurement of interstitial convective heat transfer and frictional drag for flow across metal foams , 2002 .

[13]  Martine Baelmans,et al.  Airflow through Beds of Apples and Chicory Roots , 2004 .

[14]  J. L. Lage,et al.  Protocol for measuring permeability and form coefficient of porous media , 2005 .

[15]  F. Topin,et al.  About the use of fibrous materials in compact heat exchangers , 2004 .

[16]  M. Hawley,et al.  Wall Effect in Packed Columns , 1969 .

[17]  A. Mortensen,et al.  Permeability of open-pore microcellular materials , 2005 .

[18]  Yiannis Ventikos,et al.  Simulations of flow through open cell metal foams using an idealized periodic cell structure , 2003 .

[19]  A. B. Metzner,et al.  Wall effects in laminar flow of fluids through packed beds , 1981 .

[20]  Nihad Dukhan,et al.  Equivalent particle diameter and length scale for pressure drop in porous metals , 2008 .

[21]  Jack Legrand,et al.  Pressure drop prediction for flow through high porosity metallic foams , 1994 .

[22]  S. Ergun Fluid flow through packed columns , 1952 .

[23]  D. A. Nield Alternative model for wall effect in laminar flow of a fluid through a packed column , 1983 .

[24]  N. Dukhan,et al.  Air Flow Through Compressed and Uncompressed Aluminum Foam: Measurements and Correlations , 2006 .

[25]  J. Hyun,et al.  Effective Thermal Conductivity and Permeability of Aluminum Foam Materials1 , 2000 .

[26]  Donald A. Nield,et al.  Two Types of Nonlinear Pressure-Drop Versus Flow-Rate Relation Observed for Saturated Porous Media , 1997 .

[27]  R. Mahajan,et al.  Thermophysical properties of high porosity metal foams , 2002 .

[28]  D. Seguin,et al.  Experimental characterisation of flow regimes in various porous media—I: Limit of laminar flow regime , 1998 .

[29]  A. Bejan,et al.  Convection in Porous Media , 1992 .