NUMERICAL STUDY OF HEAT-TRANSFER AND FLOW OF NATURAL-CONVECTION IN ANENCLOSURE WITH A HEAT-GENERATING CONDUCTING BODY

Authors
Citation
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
Citations number
14
Categorie Soggetti
Mechanics,Thermodynamics
ISSN journal
10407782
Volume
31
Issue
3
Year of publication
1997
Pages
289 - 303
Database
ISI
SICI code
1040-7782(1997)31:3<289:NSOHAF>2.0.ZU;2-X
Abstract
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.