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Heat and mass transfer by natural convection in a non-Darcy porous medium

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Summary

The Forchheimer free convection heat and mass transfer near a vertical surface embedded in a fluid saturated porous medium has been analyzed. A similarity solution is presented for constant wall temperature and concentration distributions with specified power function form (Ax −1/2) of mass flux parameter. The effect of Grashof number (Gr), the buoyancy ratio (N), the Lewis number (Le) and the surface mass flux (f w ) on the nondimensional heat and mass transfer coefficients are presented.

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Abbreviations

A :

real constant

c :

inertial coefficient

D :

concentration molecular diffusion

f :

dimensionless stream function

g :

gravitational acceleration in thex direction

Gr:

the non-dimensional inertial parameter\(\frac{{c\sqrt K Kg\beta _T \theta _w }}{{v^2 }}\)

K :

permeability

k :

thermal conductivity

Le:

Lewis number\(\frac{\alpha }{D}\)

N :

Buoyancy ratio parameter\(\left( {\frac{{\beta _C \phi w}}{{\beta _T \theta w}}} \right)\)

p :

pressure

q :

local heat flux

m :

local mass flux

Ra x :

modified Rayleigh number\(\left( {\frac{{Kg\beta _T \theta _w x}}{{\alpha v}}} \right)\)

T :

temperature

C :

concentration

u, v :

velocity components inx andy directions respectively

x, y :

Cartesian coordinates

α:

effective thermal diffusivity

β T :

thermal expansion coeffcient

β c :

concentration expansion coefficient

θ:

dimensionless temperature variable

ϕ:

dimensionless concentration variable

η:

similarity parameter

μ:

viscosity

v :

kinematic viscosity

θ:

dimensionless temperature

ϱ:

fluid density

ω:

evaluated at wall condition

∞:

evaluated at the outer edge of the boundary layer

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Murthy, P.V.S.N., Singh, P. Heat and mass transfer by natural convection in a non-Darcy porous medium. Acta Mechanica 138, 243–254 (1999). https://doi.org/10.1007/BF01291847

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  • DOI: https://doi.org/10.1007/BF01291847

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