One of the earliest transport models for membranes was given by Kimura
and Sourirajan [1] in 1967. Their two-parameter model, termed the pre
ferential sorption-capillary flow model, characterized the performance
of membranes for many solution systems. Ohya et al. [2,3] subsequentl
y adopted this model to solve for the separation performance of commer
cial RO permeators. However, the resulting system of solution consists
of eight equations, two of which require numerical integration that m
ust be solved simultaneously in order to obtain the non-dimensional tr
ansport characteristics, lambda and theta. In this paper a simplificat
ion is introduced in the integral expression leading to an analytical
solution. For conditions typical of seawater desalination operations,
it is shown that the discrepancy introduced in the integrals as a resu
lt of the simplification is much less than 1.0%, while for the concent
ration of fruit juice, the resulting error is about 2.0%.