In the case of mass transfer where concentration differences in both phases
must be taken into account, one may define an overall mass-transfer coeffi
cient based on the apparent overall concentration difference. If the equili
brium relationship is linear, i.e., in cases where a Henry's law relationsh
ip can be applied, the overall mass-transfer coefficient will be concentrat
ion independent. However, in mass-transfer operations, a linear equilibrium
relationship is in most cases not a valid approximation wherefore the over
all mass-transfer coefficient becomes strongly concentration dependent as s
hown in this paper. In this case one has to discard the use of overall mass
-transfer coefficients and calculate the rate of mass transfer from the two
-film theory using the appropriate non-linear relationship to calculate the
equilibrium ratio at the interface between the two films. (C) 1998 Elsevie
r Science B.V. All rights reserved.