TY - JOUR
T1 - Natural convection across a vertical layered porous cavity
AU - Lai, F. C.
AU - Kulacki, F. A.
N1 - Copyright:
Copyright 2014 Elsevier B.V., All rights reserved.
PY - 1988/6
Y1 - 1988/6
N2 - Numerical studies are reported for steady-state natural convection in a two-dimensional layered porous cavity heated from the side wall. Emphasis is placed on the effects caused by the sublayer thickness ratio, permeability contrast and non-uniform conductivity in a system comprising two sublayers. Calculations have covered a wide range of these parameters. It has been observed that the flow and temperature fields for a layered structure with K1/K2 < 1 are completely different from those of K1/K2 > 1. When the thermal properties are uniform, the average Nusselt number for a layered system of K1/K2 < 1 is always greater than that of a homogeneous system, and it increases with Rayleigh number, but decreases with the sublayer thickness ratio. For systems of K1/K2 > 1, the average Nusselt number is always less than that of a homogeneous system, and it increases with both Rayleigh number and the thickness ratio. When there exists a difference in the thermal conductivity of the two sublayers, a second recirculating cell is generated in the less permeable layer for K1/K2 > 1. The average Nusselt number is found to increase with the conductivity ratio for K1/K2 > 1, and decrease for K1/K2 > 1. Heat transfer results including streamline and isotherm patterns, temperature and velocity profiles, and the Nusselt vs Rayleigh number relation in terms of these parameters, are presented.
AB - Numerical studies are reported for steady-state natural convection in a two-dimensional layered porous cavity heated from the side wall. Emphasis is placed on the effects caused by the sublayer thickness ratio, permeability contrast and non-uniform conductivity in a system comprising two sublayers. Calculations have covered a wide range of these parameters. It has been observed that the flow and temperature fields for a layered structure with K1/K2 < 1 are completely different from those of K1/K2 > 1. When the thermal properties are uniform, the average Nusselt number for a layered system of K1/K2 < 1 is always greater than that of a homogeneous system, and it increases with Rayleigh number, but decreases with the sublayer thickness ratio. For systems of K1/K2 > 1, the average Nusselt number is always less than that of a homogeneous system, and it increases with both Rayleigh number and the thickness ratio. When there exists a difference in the thermal conductivity of the two sublayers, a second recirculating cell is generated in the less permeable layer for K1/K2 > 1. The average Nusselt number is found to increase with the conductivity ratio for K1/K2 > 1, and decrease for K1/K2 > 1. Heat transfer results including streamline and isotherm patterns, temperature and velocity profiles, and the Nusselt vs Rayleigh number relation in terms of these parameters, are presented.
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U2 - 10.1016/0017-9310(88)90067-1
DO - 10.1016/0017-9310(88)90067-1
M3 - Article
AN - SCOPUS:0024032830
VL - 31
SP - 1247
EP - 1260
JO - International Journal of Heat and Mass Transfer
JF - International Journal of Heat and Mass Transfer
SN - 0017-9310
IS - 6
ER -