The purpose of this work is to analyze the performance of hollow-fiber
reverse-osmosis (HFRO) systems. First, the mass and momentum balances
on the fluids inside and outside of the hollow fibers are derived. Co
nsequently, these equations are coupled with the membrane transport ex
pressions to provide a two-phase model for completely describing the h
ydrodynamic behavior of HFRO units. The model equations are solved num
erically via discretization techniques. Experimental data are used for
two objectives; transport-parameters estimation and model validation.
Based upon optimization principles, a parameter-estimation technique
is proposed for correlating the membrane-transport coefficients with t
he operating pressures and concentrations. The model validity is eluci
dated by comparing the theoretical predictions with the experimental d
ata for different HFRO modules and over a wide range of operating para
meters.