1995
DOI: 10.1002/aic.690410508
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Convective diffusion and adsorption in a swarm of spheroidal particles

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Cited by 21 publications
(13 citation statements)
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“…For bodies in an elliptic shape Payne et al (1986), Elvira (1990), Haghighi et al (1990), Lu and Siebenmorgen (1992), Sarker et al (1994), Lima (1999) and Lima and Nebra (2000) can be mentioned. Besides these studies, and the work of Keltner (1973), Sheen and Hayakawa (1992), Coutelieris et al (1995), Feng a nd Michaelides (1997), Alassar (1999), Igathinathane and Chattopadhyay (2000), Carmo (2000), Carmo andLima (2000, 2001), Oliveira and Lima (2001), and Lima et al (2002a-b) can also be mentioned. Payne et al (1986) present a solution of the heat conduction equation for an irregular border using the Galerkin method with an equilibrium boundary condition at the surface of the solid.…”
Section: Introductionmentioning
confidence: 99%
“…For bodies in an elliptic shape Payne et al (1986), Elvira (1990), Haghighi et al (1990), Lu and Siebenmorgen (1992), Sarker et al (1994), Lima (1999) and Lima and Nebra (2000) can be mentioned. Besides these studies, and the work of Keltner (1973), Sheen and Hayakawa (1992), Coutelieris et al (1995), Feng a nd Michaelides (1997), Alassar (1999), Igathinathane and Chattopadhyay (2000), Carmo (2000), Carmo andLima (2000, 2001), Oliveira and Lima (2001), and Lima et al (2002a-b) can also be mentioned. Payne et al (1986) present a solution of the heat conduction equation for an irregular border using the Galerkin method with an equilibrium boundary condition at the surface of the solid.…”
Section: Introductionmentioning
confidence: 99%
“…5a and 5b was proposed by Coutelieris et al (1995) to ensure the continuity of the concentration on the outer boundary of the cell for any Peclet number. Equations 5c and 5d express the axial symmetry that has been assumed for the system.…”
Section: Theorymentioning
confidence: 99%
“…Due to the complexity of the 3D-flow around ellipsoids of revolution (Geissler, 1974;Rosenfeld et al, 1992), it is very difficult to obtain the gradient velocity and concentration at the fluid-particle interface outside the body, so the mass transfer rate is usually expressed in terms of the overall mass transfer coefficient (Strumillo and Kudra, 1986;Saravacos, 1995). As a result, as an approach the mean convective mass transfer coefficient on the surface of a spheroid can be obtained using either of the following methods: a) agreement between the predicted and experimental data using, for example, the least squares error technique (Queiroz, 1994;Carmo, 2004;Carmo and Lima, 2005) or b) empirical and theoretical mathematical correlations (Lochiel and Calderbank, 1964;Masliyah and Epstein, 1972;Clift et al, 1978;Coutelieris et al, 1995;Feng and Michaelides, 1997).…”
Section: Analytical Proceduresmentioning
confidence: 99%