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contributor authorM. Sathiyamoorthy
contributor authorTanmay Basak
contributor authorS. Roy
contributor authorN. C. Mahanti
date accessioned2017-05-09T00:24:29Z
date available2017-05-09T00:24:29Z
date copyrightDecember, 2007
date issued2007
identifier issn0022-1481
identifier otherJHTRAO-27828#1723_1.pdf
identifier urihttp://yetl.yabesh.ir/yetl/handle/yetl/136163
description abstractThe present numerical investigation deals with steady natural convection flow in a closed square cavity when the bottom wall is sinusoidal heated and vertical walls are linearly heated, whereas the top wall is well insulated. In the nonuniformly heated bottom wall maximum temperature TH attains at the center of the bottom wall. The sidewalls are linearly heated, maintained at minimum temperature Tc at top edges of the sidewalls and at temperature Th at the bottom edges of the sidewalls, i.e., Tc≤Th≤TH. Nonlinear coupled PDEs governing the flow have been solved by the penalty finite element method with biquadratic rectangular elements. Numerical results are obtained for various values of Prandtl number (Pr)(0.01≤Pr≤10) and temperature difference aspect ratio A=[(Th−Tc)∕(TH−Tc)](0≤A≤1) for higher Raleigh number Ra=105. Results are presented in the form of streamlines, isotherm contours, local Nusselt number, and the average Nusselt number as a function of temperature difference aspect ratio A. The overall heat transfer process is shown to be tuned efficiently with suitable selection of A.
publisherThe American Society of Mechanical Engineers (ASME)
titleEffect of the Temperature Difference Aspect Ratio on Natural Convection in a Square Cavity for Nonuniform Thermal Boundary Conditions
typeJournal Paper
journal volume129
journal issue12
journal titleJournal of Heat Transfer
identifier doi10.1115/1.2768099
journal fristpage1723
journal lastpage1728
identifier eissn1528-8943
keywordsFlow (Dynamics)
keywordsTemperature
keywordsHeat transfer
keywordsNatural convection
keywordsBoundary-value problems
keywordsCavities AND Prandtl number
treeJournal of Heat Transfer:;2007:;volume( 129 ):;issue: 012
contenttypeFulltext


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