Jy. Oh et al., NUMERICAL STUDY OF HEAT-TRANSFER AND FLOW OF NATURAL-CONVECTION IN ANENCLOSURE WITH A HEAT-GENERATING CONDUCTING BODY, Numerical heat transfer. Part A, Applications, 31(3), 1997, pp. 289-303
A numerical study has been conducted to investigate steady state heat
transfer and flow characteristics of natural convection in a vertical
square enclosure when a temperature difference exists across an enclos
ure and, at the same time, a conducting body generates heat within the
enclosure. Dimensionless governing equations indicate that the heat t
ransfer and flow characteristics of this system are governed by the Ra
yleigh and Prandtl numbers, the area ratio, the conductivity ratio, an
d the temperature-difference ratio. Here the temperature-difference ra
tio is defined as the ratio of a temperature difference across the enc
losure to that caused by the heat source. In the present study, the Ra
yleigh number ranges from 10(3) to 10(4) and the temperature-differenc
e ratio from 0 to 50 while the Prandtl number, the area ratio, and the
conductivity ratio are kept constant at 0.71, 0.25, 1, respectively.
The analysis is performed by observing variations of streamlines, isot
herms, heatlines, and the average Nusselt numbers on the hot and cold
walls with respect to temperature difference ratios for each Rayleigh
number. The results show that, as the temperature difference ratio inc
reases, the flow dominated by the temperature difference across the en
closure proceeds to that dominated by the temperature difference due t
o the heat source, i.e., the ratio of the average Nusselt number of th
e hot wall to that of the cold wall changes from 1 to -1. As the Rayle
igh number becomes greater, the temperature difference ratio should be
much greater to achieve the average Nusselt number ratio of -1 becaus
e of convection effects caused by the temperature difference across th
e enclosure.