Numerical study of turbulent natural convection in a cube having finite thickness heat-conducting walls

Bibliografiske detaljer
Parent link:Heat and Mass Transfer
Vol. 51, iss. 11.— 2015.— [P. 1559-1569]
Hovedforfatter: Sheremet M. A. Mikhail Aleksandrovich
Institution som forfatter: Национальный исследовательский Томский политехнический университет Энергетический институт Кафедра атомных и тепловых электростанций
Andre forfattere: Miroshnichenko I. V.
Summary:Title screen
Three-dimensional transient natural convection in a cubic enclosure having finite thickness solid walls subject to opposing and horizontal temperature gradient has been investigated by a finite volume method. The turbulent flow considered into the volume is described mathematically by the 3D Reynolds averaged Navier-Stokes equations using the standard k-ε model with wall functions, including the energy equation. The velocity and temperature distributions were calculated at fixed Prandtl number, Pr = 0.7 and different values of the Rayleigh number, thermal conductivity ratio and dimensionless time. Three-dimensional velocity and temperature fields, temperature profiles at middle cross-sections and average Nusselt numbers have been presented. It has been found that an insertion of the third coordinate for the conjugate problem leads to a decrease in the average Nusselt number by 5.8 % in conditions of a stationary heat transfer mode.
Режим доступа: по договору с организацией-держателем ресурса
Udgivet: 2015
Fag:
Online adgang:http://dx.doi.org/10.1007/s00231-015-1520-8
Format: Electronisk Book Chapter
KOHA link:https://koha.lib.tpu.ru/cgi-bin/koha/opac-detail.pl?biblionumber=648015

MARC

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320 |a [References: p. 1569 (41 tit.)] 
330 |a Three-dimensional transient natural convection in a cubic enclosure having finite thickness solid walls subject to opposing and horizontal temperature gradient has been investigated by a finite volume method. The turbulent flow considered into the volume is described mathematically by the 3D Reynolds averaged Navier-Stokes equations using the standard k-ε model with wall functions, including the energy equation. The velocity and temperature distributions were calculated at fixed Prandtl number, Pr = 0.7 and different values of the Rayleigh number, thermal conductivity ratio and dimensionless time. Three-dimensional velocity and temperature fields, temperature profiles at middle cross-sections and average Nusselt numbers have been presented. It has been found that an insertion of the third coordinate for the conjugate problem leads to a decrease in the average Nusselt number by 5.8 % in conditions of a stationary heat transfer mode. 
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