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Research Papers

Lattice Boltzmann Method for Combined Natural Convection Surface Radiation in Open Cavity

[+] Author and Article Information
Ayoub Msaddak

Thermal Radiation Research Unit,
Faculty of Sciences of Tunis,
University of Tunis EL Manar,
El Manar 1,
Tunis 2092, Tunisia
e-mail: ayoub.msaddak@fst.utm.tn

Mohieddine Ben Salah

Thermal Process Laboratory,
Center of Research and Energy Technology,
Hammam Lif 2050, Tunisia
e-mail: mohieddine2002@yahoo.com

Ezeddine Sediki

Thermal Radiation Research Unit,
Faculty of Sciences of Tunis,
University of Tunis EL Manar,
El Manar 1,
Tunis 2092, Tunisia
e-mail: sediki.ezeddine@fst.utm.tn

1Corresponding author.

Contributed by the Heat Transfer Division of ASME for publication in the JOURNAL OF THERMAL SCIENCE AND ENGINEERING APPLICATIONS. Manuscript received July 3, 2017; final manuscript received February 16, 2018; published online May 22, 2018. Assoc. Editor: Sandip Mazumder.

J. Thermal Sci. Eng. Appl 10(5), 051011 (May 22, 2018) (10 pages) Paper No: TSEA-17-1225; doi: 10.1115/1.4039925 History: Received July 03, 2017; Revised February 16, 2018

Lattice Boltzmann method (LBM) is performed to study numerically combined natural convection and surface radiation inside an inclined two-dimensional open square cavity. The cavity is heated by a constant temperature at the wall facing the opening. The walls normal to the heated surface are assumed to be adiabatic, diffuse, gray, and opaque while the open boundary is assumed to be black at ambient temperature. A Bathnagar, Gross and Krook (BGK) collision model with double distribution function (D2Q9-D2Q4) is adopted. Effects of surface radiation, inclination angle, and Rayleigh number on the heat transfer are analyzed and discussed. Results are presented in terms of isotherms, streamlines, and Nusselt number. It was found that the presence of surface radiation enhances the heat transfer. The convective Nusselt number decreases with increasing surface emissivity as well as with Rayleigh number, while the total Nusselt number increases with increasing surface emissivity and Rayleigh number. The inclination angle has also a significant effect on flow and heat transfer inside the cavity. However, the magnitude of total heat transfer decreases considerably when open cavity is tilted downward.

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Figures

Grahic Jump Location
Fig. 1

Schematic of the problem geometry

Grahic Jump Location
Fig. 2

D2Q9 model and D2Q4 model

Grahic Jump Location
Fig. 3

Evolution of the isotherms (up) and streamlines (down) with inclination angle for Ra = 104, (a) ε = 0 and (b) ε = 0.8

Grahic Jump Location
Fig. 4

Evolution of the isotherms (up) and streamlines (down) with inclination angle for Ra = 106, (a) ε = 0 and (b) ε = 0.8

Grahic Jump Location
Fig. 5

Local convective Nusselt number at the hot wall as function of surface emissivity and inclination angle for Ra = 104 (a) and Ra = 106 (b)

Grahic Jump Location
Fig. 6

Average convective and radiative Nusselt number (a) and average total Nusselt number (b) as function of surface emissivity and inclination angle

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