The common methods for calculating the mass transfer across liquid-liq
uid interfaces in technical applications take into account the mass tr
ansfer resistances within the bulk phases. The transfer resistance of
the interface and a possible coupling between the momentum and the mas
s transport is not taken into account. In the present paper a survey i
s given of theoretical approaches which can describe this coupling and
the additional mass transfer resistance. A theory is proposed by Hamp
e which can be used to explain the coupling between momentum and mass
transport employing thermodynamics of irreversible processes. On the b
asis of this work, the influence of the dilatation of a flat interface
on the mass transfer is deduced. It is also concluded from this theor
y that the diffusion coefficients within the bulk phases are coupled n
ear the thermodynamic equilibrium.