EFFECT OF DIFFERENT THERMAL BOUNDARY CONDITIONS AT BOTTOM WALL ON NATURAL CONVECTION IN CAVITIES

Natural convection in cavities is studied numerically using a finite volume based computational procedure. The enclosure used for flow and heat transfer analysis has been bounded by adiabatic top wall, constant temperature cold vertical walls and a horizontal bottom wall. The bottom wall is subjecte...

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Main Authors: ASWATHA, C. J. GANGADHARA GOWDA, S. N. SRIDHARA, K. N. SEETHARAMU
Format: Article
Language:English
Published: Taylor's University 2011-02-01
Series:Journal of Engineering Science and Technology
Subjects:
Online Access:http://jestec.taylors.edu.my/Vol%206%20Issue%201%20February%2011/Vol_6_1__109_130_ASWATHA.pdf
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spelling doaj-f00b8ede96d644ab9eff34b6c27d23432020-11-24T23:57:05ZengTaylor's UniversityJournal of Engineering Science and Technology1823-46902011-02-0161109130EFFECT OF DIFFERENT THERMAL BOUNDARY CONDITIONS AT BOTTOM WALL ON NATURAL CONVECTION IN CAVITIESASWATHAC. J. GANGADHARA GOWDAS. N. SRIDHARAK. N. SEETHARAMUNatural convection in cavities is studied numerically using a finite volume based computational procedure. The enclosure used for flow and heat transfer analysis has been bounded by adiabatic top wall, constant temperature cold vertical walls and a horizontal bottom wall. The bottom wall is subjected to uniform / sinusoidal / linearly varying temperatures. Nusselt numbers are computed for Rayleigh numbers (Ra) ranging from 103 to 107 and aspect ratios (H/L) of 1 to 3. Results are presented in the form of stream lines, isotherm plots and average Nusselt numbers. It is observed from this study that the uniform temperature at the bottom wall gives higher Nusselt number compared to the sinusoidal and linearly varying temperature cases. The average Nusselt numbers increases monotonically with Rayleigh number for aspect ratios 1, 2 and 3 for bottom wall and side walls. For the case of aspect ratios 2 and 3, the average Nusselt number for a given Rayleigh number increases at the bottom wall as compared to that for aspect ratio 1. However the average Nusselt number decreases as the aspect ratio increases from 1 to 3 for side wall.http://jestec.taylors.edu.my/Vol%206%20Issue%201%20February%2011/Vol_6_1__109_130_ASWATHA.pdfNatural convectionCavitiesAspect ratioThermal boundary conditionsNumerical heat transfer
collection DOAJ
language English
format Article
sources DOAJ
author ASWATHA
C. J. GANGADHARA GOWDA
S. N. SRIDHARA
K. N. SEETHARAMU
spellingShingle ASWATHA
C. J. GANGADHARA GOWDA
S. N. SRIDHARA
K. N. SEETHARAMU
EFFECT OF DIFFERENT THERMAL BOUNDARY CONDITIONS AT BOTTOM WALL ON NATURAL CONVECTION IN CAVITIES
Journal of Engineering Science and Technology
Natural convection
Cavities
Aspect ratio
Thermal boundary conditions
Numerical heat transfer
author_facet ASWATHA
C. J. GANGADHARA GOWDA
S. N. SRIDHARA
K. N. SEETHARAMU
author_sort ASWATHA
title EFFECT OF DIFFERENT THERMAL BOUNDARY CONDITIONS AT BOTTOM WALL ON NATURAL CONVECTION IN CAVITIES
title_short EFFECT OF DIFFERENT THERMAL BOUNDARY CONDITIONS AT BOTTOM WALL ON NATURAL CONVECTION IN CAVITIES
title_full EFFECT OF DIFFERENT THERMAL BOUNDARY CONDITIONS AT BOTTOM WALL ON NATURAL CONVECTION IN CAVITIES
title_fullStr EFFECT OF DIFFERENT THERMAL BOUNDARY CONDITIONS AT BOTTOM WALL ON NATURAL CONVECTION IN CAVITIES
title_full_unstemmed EFFECT OF DIFFERENT THERMAL BOUNDARY CONDITIONS AT BOTTOM WALL ON NATURAL CONVECTION IN CAVITIES
title_sort effect of different thermal boundary conditions at bottom wall on natural convection in cavities
publisher Taylor's University
series Journal of Engineering Science and Technology
issn 1823-4690
publishDate 2011-02-01
description Natural convection in cavities is studied numerically using a finite volume based computational procedure. The enclosure used for flow and heat transfer analysis has been bounded by adiabatic top wall, constant temperature cold vertical walls and a horizontal bottom wall. The bottom wall is subjected to uniform / sinusoidal / linearly varying temperatures. Nusselt numbers are computed for Rayleigh numbers (Ra) ranging from 103 to 107 and aspect ratios (H/L) of 1 to 3. Results are presented in the form of stream lines, isotherm plots and average Nusselt numbers. It is observed from this study that the uniform temperature at the bottom wall gives higher Nusselt number compared to the sinusoidal and linearly varying temperature cases. The average Nusselt numbers increases monotonically with Rayleigh number for aspect ratios 1, 2 and 3 for bottom wall and side walls. For the case of aspect ratios 2 and 3, the average Nusselt number for a given Rayleigh number increases at the bottom wall as compared to that for aspect ratio 1. However the average Nusselt number decreases as the aspect ratio increases from 1 to 3 for side wall.
topic Natural convection
Cavities
Aspect ratio
Thermal boundary conditions
Numerical heat transfer
url http://jestec.taylors.edu.my/Vol%206%20Issue%201%20February%2011/Vol_6_1__109_130_ASWATHA.pdf
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