Numerical simulation of mixed convection flow and heat transfer in the lid-driven triangular cavity with different obstacle configurations. (April 2021)

• Record Type: Journal Article
• Authors: Xiong, Pei-Ying; Hamid, Aamir; Iqbal, Kaleem; Irfan, M.; Khan, Masood
• Is Part Of: International communications in heat and mass transfer. Volume 123(2021)
• Publication Date: 2021-04
• Subjects: Mixed convection -- Magneto-hydrodynamics -- Heat transfer enhancement -- Circular solid obstacles -- Triangular lid-driven cavity; Heat -- Transmission -- Periodicals; Mass transfer -- Periodicals; Chaleur -- Transmission -- Périodiques; Transfert de masse -- Périodiques; Heat -- Transmission; Mass transfer; Periodicals; 621.4022
• DOI: 10.1016/j.icheatmasstransfer.2021.105202
• Languages: English
• ISSNs: 0735-1933

Abstract

Abstract: There are several industrial applications, particularly lid-driven walls, for mixed convection heat transfer characteristics across various cavities. In order to increase the effectiveness of cooling, electrical, electronic and nuclear devices and to monitor the fluid flow and heat exchange of solar thermal installations and thermal storage, such a problem requires further investigation. The main goal of this profound study is to examine the convective heat transfer nature of thermal convection on Newtonian MHD fluid in a lid-driven triangular cavity subjected to heating by a thick triangular wall, including the effects of varying Richardson number, Reynolds number, Hartmann number, and cold circular obstacle. Graphical illustration shows that the upper wall having temperature Th is moving from left to right, whereas inclined sidewalls are adiabatic. Further, a cold circular obstacle containing temperature T ∗∗ is placed near the left and right wall of the triangular cavity with T ∗∗ < Th . The governing flow equations are tackled by the Galerkin Finite Element Method (GFEM) to prepare the desired results. Velocity contours, isotherms and heat transfer rates demonstrate flow kinematics and heat transport processes. The high estimate of the Reynolds number has been found to provide a decent rate of convective heat transfer to a good liquid progression. For a higher number of Grashof, which achieves the maximum convection intensity, it is checked that natural convection dominates within the convection system. The Richardson number is a rising function of the Nusselt number, while the opposite trend is observed due to the rise in the Hartmann number.