Conjugate natural convection in enclosures with external and internal heat sources

2006 ◽  
Vol 44 (3-4) ◽  
pp. 148-165 ◽  
Author(s):  
Fu-Yun Zhao ◽  
Guang-Fa Tang ◽  
Di Liu
2013 ◽  
Vol 224 (5) ◽  
pp. 1103-1114 ◽  
Author(s):  
Saman Shalbaf ◽  
Aminreza Noghrehabadi ◽  
Mohammad Reza Assari ◽  
Alireza Daneh Dezfuli

1976 ◽  
Vol 98 (1) ◽  
pp. 55-61 ◽  
Author(s):  
R. J. Kee ◽  
C. S. Landram ◽  
J. C. Miles

Steady natural convective flow fields were numerically and experimentally characterized for 0.7 Prandtl number fluids having constant, uniformly distributed, internal heat sources. The bounding isothermal walls containing the fluid were considered to be either a sphere or a cylinder of finite height. An instrumented cylinder containing radioactive tritium gas was used to demonstrate experimental and analytical agreement for local temperatures over a range of Grashof numbers. For the spherical geometry, a generalized correlation was obtained for the surface-averaged Nusselt number as a function of a modified Grashof number.


2006 ◽  
Vol 129 (5) ◽  
pp. 679-682 ◽  
Author(s):  
Seung Dong Lee ◽  
Jong Kuk Lee ◽  
Kune Y. Suh

This paper presents results of steady-state experiments concerned with natural convection heat transfer of air in a rectangular pool in terms of the Nusselt number (Nu) versus the modified Rayleigh number (Ra′) varying from 109 to 1012. Cartridge heaters were immersed in the working fluid to simulate uniform volumetric heat generation. Two types of boundary conditions were adopted in the test: (I) top cooled, and (II) top and bottom cooled. The other sides were kept insulated. In the case of boundary condition II, the upward heat transfer ratio, Nuup∕(Nuup+Nudn), turned out to be 0.7–0.8 in the range of Ra′ between 1.05×1010 and 3.68×1011.


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