A numerical study is carried out on double-diffusive natural convection in
a vertical annular porous layer whose vertical wads are at constant tempera
tures and concentrations. The investigation covers the range 10 less than o
r equal to R-T less than or equal to 500, 1 less than or equal to Le less t
han or equal to 10, -50 less than or equal to N less than or equal to 50, 1
less than or equal to A less than or equal to 5, 1 less than or equal to k
appa less than or equal to 10, where R-T, Le, N, A, and kappa are the therm
al Rayleigh number, Lewis number, buoyancy ratio, aspect ratio, and radius
ratio of the enclosure, respectively. The two extreme cases of heat-driven
and solute-driven natural convection correlations, valid in the boundary la
yer regime, are derived to calculate the average Nusselt and Sherwood numbe
rs in terms of the governing parameters of the problem. In order to investi
gate the effects of the combined thermal and solutal buoyancy forces on the
average heat and mass transfer, results have been obtained for a large ran
ge of buoyancy ratios N. Streamlines, isotherms, and isosolutes in the syst
em are produced to illustrate the flow structure transition from mass speci
es dominated opposing to thermal dominated and mass species dominated aidin
g flows, respectively. The thermal Rayleigh and Lewis numbers and the radiu
s ratio are found to influence the buoyancy ratio at which flow transition
and flow reversal occurs.