Heat Transfer inside Elliptic Cylindrical Reactor: Effect of Bed Porosity

Article Preview

Abstract:

The study of heat transfer phenomenon in porous media by fluids percolated in the axial direction has been of interest to many researchers in various branches of science and technology. Applications are directed to different process such as filtration, distillation, absorption and adsorption in columns, drying and catalytic reactions in fixed beds. The literature has presented several solutions of the heat diffusion / convection equation in fixed bed reactors, but these studies are limited to a cylindrical geometry. In this sense, this work aim to present a pseudo-homogeneous three-dimensional model to describe the steady-state heat transfer within a fixed bed reactor with elliptic cylindrical geometry by considering variable porosity. The energy equation written in elliptical cylindrical coordinates and applied to the porous medium (particulate system) is discretized numerically using the finite volume method. Results of the temperature distribution within the bed are presented analyzed. It was verified that with increased porosity heat transfer inside the reactor tends to be more intense and thus, lower temperature gradients are found in all cross section of the reactor.

You might also be interested in these eBooks

Info:

Periodical:

Pages:

97-102

Citation:

Online since:

March 2013

Export:

Price:

Permissions CCC:

Permissions PLS:

Сopyright:

© 2013 Trans Tech Publications Ltd. All Rights Reserved

Share:

Citation:

[1] P. Andrigo, R. Bagatain and G. Pagani: Catal. Today, Vol. 52 (1999), p.197

Google Scholar

[2] Xueyan Guo and Ren Dai: Particuology, Vol. 8 (2010), p.293.

Google Scholar

[3] D.A. Nield and A. Bejan: Convection in Porous Media (Springer-Verlag, Yew York, 1992)

Google Scholar

[4] Wu-Shung Fu and Hsin-Chien Huang: Int. J. Heat Mass Transf. Vol. 42 (1998), p.13

Google Scholar

[5] D. Vortmeyer and J. Schuster: Chem. Eng. Sci. Vol. 38 (1983), p.1691

Google Scholar

[6] A.P.E. De Wash and G.F Froment: Chem. Eng. Sci., Vol. 27 (1972), p.567

Google Scholar

[7] A.G. Dixon, W.R. Paterson and D.L. Cresswell: Symposium Series, ACS, Vol. 65 (1978), p.238

Google Scholar

[8] A.M. Silveira: Heat Transfer in Porous Media: Analysis of the One Phase Model for Fixed Beds (PhD thesis, COPPE/UFRJ, Brazil, 1991).

Google Scholar

[9] L.G. Oliveira, R. Swarnakar and A.G. Barbosa de Lima: Int. J. Chem. Reactor Eng., Vol. 6 (2008), p.1

Google Scholar

[10] L.G. Oliveira: Heat Transfer in Elliptic Cylindrical Reactor of Fixed Bed: Thermo-fluid-dynamical and Geometrical Aspects (PhD Thesis, Federal University of Campina Grande, Brazil, 2004).

Google Scholar

[11] C.R. Maliska: Computational Heat Transfer and Fluid Mechanics (LCT, Rio de Janeiro, 2004).

Google Scholar

[12] K. Taylor, A.G. Smith and S. Ross: Second International Conference On CFD in the Minerals and Process Industries (CSIRO), Melbourne, Australia, (1999), p.273.

Google Scholar

[13] A.G. Barbosa de Lima, L.G. de Oliveira, W.C.P.B. de Lima, in: Materials with Complex Behaviour II, edited by A. Öchsner, L.F.M da Silva, H. Altenbach, volume 16, Springer-Verlag, Heidelberg (2012), pp.549-571.

Google Scholar