Numerical investigation of double-diffusive convection in an open cavity with partially heated wall via heatline approach

Double-diffusive natural convection in an open top square cavity, partially heated and salted from the side, is studied numerically via the heatline approach. Constant temperatures and concentrations are imposed along the right and left walls, while the heat balance at the surface is assumed to obey...

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Published in:International Journal of Thermal Sciences
Main Author: 2-s2.0-84945288095
Format: Article
Language:English
Published: Elsevier Masson SAS 2016
Online Access:https://www.scopus.com/inward/record.uri?eid=2-s2.0-84945288095&doi=10.1016%2fj.ijthermalsci.2015.09.017&partnerID=40&md5=47fde52ccdfcf996727191ceed754f6d
id Arbin N.; Saleh H.; Hashim I.; Chamkha A.J.
spelling Arbin N.; Saleh H.; Hashim I.; Chamkha A.J.
2-s2.0-84945288095
Numerical investigation of double-diffusive convection in an open cavity with partially heated wall via heatline approach
2016
International Journal of Thermal Sciences
100

10.1016/j.ijthermalsci.2015.09.017
https://www.scopus.com/inward/record.uri?eid=2-s2.0-84945288095&doi=10.1016%2fj.ijthermalsci.2015.09.017&partnerID=40&md5=47fde52ccdfcf996727191ceed754f6d
Double-diffusive natural convection in an open top square cavity, partially heated and salted from the side, is studied numerically via the heatline approach. Constant temperatures and concentrations are imposed along the right and left walls, while the heat balance at the surface is assumed to obey Newton's law of cooling. The finite difference method is used to solve the dimensionless governing equations. The governing parameters involved in this investigation are the thermal Marangoni number (0 ≤ MaT ≤ 1000), the solutal Marangoni number (0 ≤ Mac ≤ 1000), the Lewis number (10 ≤ Le ≤ 100), the heater size, (0.2 ≤ s ≤ 0.8), Grashof number, Gr = 104, Prandtl number, Pr = 10, Biot number, Bi = 0.1 and aspect ratio 1. The numerical results are reported for the effect of the Marangoni number, Lewis number and heater size on the contours of streamlines, isotherms, isoconcentrations, masslines and heatlines. The predicted results for the average Nusselt number and Sherwood number are presented for various parametric conditions. It is shown that the heat and mass transfer mechanisms are affected by the heater segment length. A direct relation between both opposing (N = -2) and aiding flow (N = 2), and heat and mass transfer process is found for various values of the Marangoni and Lewis numbers. © 2015 Elsevier Masson SAS.
Elsevier Masson SAS
12900729
English
Article

author 2-s2.0-84945288095
spellingShingle 2-s2.0-84945288095
Numerical investigation of double-diffusive convection in an open cavity with partially heated wall via heatline approach
author_facet 2-s2.0-84945288095
author_sort 2-s2.0-84945288095
title Numerical investigation of double-diffusive convection in an open cavity with partially heated wall via heatline approach
title_short Numerical investigation of double-diffusive convection in an open cavity with partially heated wall via heatline approach
title_full Numerical investigation of double-diffusive convection in an open cavity with partially heated wall via heatline approach
title_fullStr Numerical investigation of double-diffusive convection in an open cavity with partially heated wall via heatline approach
title_full_unstemmed Numerical investigation of double-diffusive convection in an open cavity with partially heated wall via heatline approach
title_sort Numerical investigation of double-diffusive convection in an open cavity with partially heated wall via heatline approach
publishDate 2016
container_title International Journal of Thermal Sciences
container_volume 100
container_issue
doi_str_mv 10.1016/j.ijthermalsci.2015.09.017
url https://www.scopus.com/inward/record.uri?eid=2-s2.0-84945288095&doi=10.1016%2fj.ijthermalsci.2015.09.017&partnerID=40&md5=47fde52ccdfcf996727191ceed754f6d
description Double-diffusive natural convection in an open top square cavity, partially heated and salted from the side, is studied numerically via the heatline approach. Constant temperatures and concentrations are imposed along the right and left walls, while the heat balance at the surface is assumed to obey Newton's law of cooling. The finite difference method is used to solve the dimensionless governing equations. The governing parameters involved in this investigation are the thermal Marangoni number (0 ≤ MaT ≤ 1000), the solutal Marangoni number (0 ≤ Mac ≤ 1000), the Lewis number (10 ≤ Le ≤ 100), the heater size, (0.2 ≤ s ≤ 0.8), Grashof number, Gr = 104, Prandtl number, Pr = 10, Biot number, Bi = 0.1 and aspect ratio 1. The numerical results are reported for the effect of the Marangoni number, Lewis number and heater size on the contours of streamlines, isotherms, isoconcentrations, masslines and heatlines. The predicted results for the average Nusselt number and Sherwood number are presented for various parametric conditions. It is shown that the heat and mass transfer mechanisms are affected by the heater segment length. A direct relation between both opposing (N = -2) and aiding flow (N = 2), and heat and mass transfer process is found for various values of the Marangoni and Lewis numbers. © 2015 Elsevier Masson SAS.
publisher Elsevier Masson SAS
issn 12900729
language English
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accesstype
record_format scopus
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