Membrane contactors, providing a non-dispersive extraction technique,
were used for the removal of valeric (n-pentanoic) acid from synthetic
aqueous solutions simulating an industrial wastewater from polymer ma
nufacturing. Amberlite LA-2 (secondary amine) in toluene was chosen as
the extraction system. Equilibrium conditions were determined and mec
hanistically modelled for different extractant concentrations allowing
the further calculation of mass transfer coefficients. The influence
of the hydrodynamics of both the aqueous and organic phases on the ove
rall mass transfer coefficient, calculated through two proposed method
s, was studied. The integration of extraction and backextraction was a
lso carried out, allowing a further acid removal with lower extractant
concentrations. (C) 1997 Elsevier Science B.V.