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Chapter 10: Natural Convection Gas Transport in Porous Media
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                           which characterizes the non-Darcy fluid, and the curvature parameter. The natural
                           convection from a heated circular cylinder into an unbounded porous medium was
                           investigated for the full range of Rayleigh numbers by Ingham and Pop (1987). At
                           small Rayleigh numbers a qualitative solution was obtained and at large Rayleigh
                           numbers the second-order boundary-layer solution was found that took into account
                           the first-order plume solution.
                             The effect of conduction-radiation on natural convection flow of an optically dense
                           viscous incompressible fluid along an isothermal cylinder of elliptic cross section
                           was investigated by Hossain et al. (1998). The boundary layer equations governing
                           the flow were shown to be nonsimilar. Full numerical solutions of the governing
                           equations were obtained using the implicit finite difference method. The solutions
                           were expressed in terms of the Nusselt number against the eccentric angle alpha in
                           the range (0, π). The working fluid was assumed to have a unit value for the Prandtl
                           number, Pr. It was found that the rate of heat transfer from the slender body is higher
                           than the corresponding one for the blunt body and that the radiation field further
                           enhances this increase.
                             Theflowandheattransferbytransientnaturalconvectioninaverticalcylinderfilled
                           with air saturated porous medium was studied by Slimi et al. (1998). The cylinder is
                           opened at both ends and heated with a constant wall heat flux density. That study was
                           carried out using the Forchheimer-extended Darcy flow model and a two-temperature
                           model. The results of that study provided the validity of the Darcy flow model and
                           the thermal boundary layer approximations. In a related study, Hossain et al. (1999)
                           considered non-Darcy convection heat and mass transfer along a vertical permeable
                           cylinder embedded in a porous medium for Prandtl number of unity.

                           10.7  NATURAL CONVECTION ABOUT SPHERES

                           Natural convection flow and heat transfer due to the presence of a heated sphere
                           embedded in a porous medium has motivated many researchers owing to its wide-
                           ranging applications in a number of fields such as chemical engineering, thermal
                           insulation systems, and nuclear waste management. Yamamoto (1974) was the first
                           to consider the natural convection problem around a sphere in a porous medium.
                           Asymptotic solutions for small Rayleigh numbers were obtained for steady natural
                           convection from a constant surface temperature sphere.
                             Sano and Okihara (1994) analyzed natural convection around a sphere embedded in
                           a porous medium for small Rayleigh numbers. The sphere was suddenly heated and,
                           subsequently, maintained at a constant heat flux over the surface. Asymptotic solu-
                           tions were obtained for the transient and steady-state temperature distribution around
                           the sphere. The effects of viscous dissipation, Joule heating and heat source/sink
                           on non-Darcy MHD natural convection flow over an isoflux permeable sphere in a
                           porous medium are numerically analyzed byYih (2000). The governing equations are
                           transformed into the nonsimilar boundary layer equations and solved by the Keller box
                           method. Numerical results for the wall shear stress and the Nusselt number are pre-
                           sented for the dimensionless coordinate along the surface, the Forchheimer number,
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