This investigation presents a mathematical, uni-dimensional model for
the description of measured concentration profiles of sulphur and iron
in non-stirred bath-slag systems. Detailed analysis of the profiles i
n slags of several basicities show that the mass transfer is also infl
uenced by a convective transport mechanism overlaying diffusion. The i
nterfacial convection, known as the Marangoni effect, is considered to
be the reason for this convection at the phase boundary. The dependen
ce of the mass transfer on the basicity, the initial sulphur content o
f the bath, and the addition of a CaF2 mass content of 2.5% has been i
nvestigated. A computer calculated match of theoretical concentration
plots with the data measured yields the interdiffusivity of S2- and Fe
2+ within the slag, the average velocity of the convective material tr
ansport normal to the phase boundary, and the equilibrium sulphur cont
ents. The value of the average velocity increases exponentially with d
ecreasing slag viscosity. The relation between the mass transfer coeff
icients and both the diffusion coefficient in the bath and the interdi
ffusivity in the slag, familiar from the surface renewal theory, follo
ws as a consequence of the mass conservation law.