Please use this identifier to cite or link to this item: http://repositorio.ufc.br/handle/riufc/66672
Type: Artigo de Periódico
Title: Numerical analysis of natural convection in parallel, convergent, and divergent open-ended channels
Authors: Marcondes, Francisco
Melo, Vinícius de Souza
Gurgel, José Maurício Alves de Matos
Keywords: Convection;Channel flow;Finite-volume methods
Issue Date: 2006
Publisher: International Journal of Numerical Methods for Heat & Fluid Flow
Citation: MARCONDES, F.; MELO, V. de S.; GURGEL, J. M. Numerical analysis of natural convection in parallel, convergent, and divergent open-ended channels. International Journal of Numerical Methods for Heat & Fluid Flow, [s.l.], v. 16, n. 3, p. 304-323, 2006.
Abstract: Purpose – To investigate the natural convection in open-ended parallel, convergent, and divergent channels using a fully elliptic procedure without extending the domain outside the channel for the application of the boundary conditions at the inlet and outlet of the channels. Design/methodology/approach – The model is two-dimensional and fully elliptic in x and y directions, and the equations are solved only inside the channel by the finite volume method using a co-located arrangement with a segregated procedure and boundary fitted coordinates. The pressure-velocity coupling is solved by the PRIME algorithm. Findings – The results are shown in terms of velocity vectors, streamlines, isotherms, and the local and the average Nusselt number for all fluids and configurations investigated. For high values of the Rayleigh number, a recirculation region in the outlet of all investigated configurations and Prandtl numbers was observed. Based on the results, a single correlation is proposed to evaluate the average Nusselt number for all fluids and configurations analyzed. Research limitations/implications – The shown results are based on the following hypothesis: steady-state, two-dimensional, laminar flow, and Boussinesq’s aproximation. The results are presented in following range of parameters: 105 , (Smax/L)RaS max , 108, where Smax denotes the maximum distance between the plates and Ra denotes the Rayleigh number; half angle of convergence or divergence (u): 58 and 158; and Prandtl numbers: 0.7, 5.0, and 88. Originality/value – Local and average Nusselt numbers, for Prandtl numbers varying from 0.70 to 88, and a correlation for the average Nusselt number for all fluids and configurations are presented. The results presented in this paper are useful to engineers and researchers involved in thermal design and numerical methods.
URI: http://www.repositorio.ufc.br/handle/riufc/66672
ISSN: 0961-5539
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