Three-dimensional numerical predictions and experimental data have been obtained for natural convection from a 3 × 3 array of discrete heat sources flush-mounted on one vertical wall of a rectangular cavity and cooled by the opposing wall. Predictions performed in a companion paper (Heindel et al., 1995a) revealed that three-dimensional edge effects are significant and that, with increasing Rayleigh number, flow and heat transfer become more uniform across each heater face. The three-dimensional predictions are in excellent agreement with the data of this study, whereas a two-dimensional model of the experimental geometry underpredicts average heat transfer by as much as 20 percent. Experimental row-averaged Nusselt numbers are well correlated with a Rayleigh number exponent of 0.25 for RaLz ≲ 1.2 × 108.
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Laminar Natural Convection in a Discretely Heated Cavity: II—Comparisons of Experimental and Theoretical Results
T. J. Heindel,
T. J. Heindel
Heat Transfer Laboratory, School of Mechanical Engineering, Purdue University, West Lafayette, IN 47907-1288
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F. P. Incropera,
F. P. Incropera
Heat Transfer Laboratory, School of Mechanical Engineering, Purdue University, West Lafayette, IN 47907-1288
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S. Ramadhyani
S. Ramadhyani
Heat Transfer Laboratory, School of Mechanical Engineering, Purdue University, West Lafayette, IN 47907-1288
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T. J. Heindel
Heat Transfer Laboratory, School of Mechanical Engineering, Purdue University, West Lafayette, IN 47907-1288
F. P. Incropera
Heat Transfer Laboratory, School of Mechanical Engineering, Purdue University, West Lafayette, IN 47907-1288
S. Ramadhyani
Heat Transfer Laboratory, School of Mechanical Engineering, Purdue University, West Lafayette, IN 47907-1288
J. Heat Transfer. Nov 1995, 117(4): 910-917 (8 pages)
Published Online: November 1, 1995
Article history
Received:
December 1, 1994
Revised:
July 1, 1995
Online:
January 23, 2008
Citation
Heindel, T. J., Incropera, F. P., and Ramadhyani, S. (November 1, 1995). "Laminar Natural Convection in a Discretely Heated Cavity: II—Comparisons of Experimental and Theoretical Results." ASME. J. Heat Transfer. November 1995; 117(4): 910–917. https://doi.org/10.1115/1.2836310
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