A. Baudot et al., Total permeate pressure influence on the selectivity of the pervaporation of aroma compounds, J MEMBR SCI, 158(1-2), 1999, pp. 167-185
Pervaporation experiments with four aroma compounds (covering a wide range
of physicochemical properties: from hydrophilic low-boilers to very hydroph
obic high-boilers) diluted in model binary aqueous solutions, were conducte
d at 30 degrees C through three kinds of commercial organophilic membranes
on a plate-and-frame module. A model, based on the estimation of transmembr
ane transfer coefficients (with a driving force expressed in terms of parti
al pressure difference between each side of the membrane), was used in orde
r to represent the influence of the total permeate pressure on the selectiv
ity of the pervaporation of the various studied aroma compounds. At first,
a silicalite-filled silicone membrane set, best-suited for the selective ex
traction of small-size organic permeants, was used for the pervaporation of
low-boilers (diacetyl and ethyl acetate). With these two molecules, the se
paration factor of the pervaporation operation was independent of the total
permeate pressure. Moreover, the silicalite-filled membrane proved to be m
ore selective than the vapour-liquid equilibrium characteristic of the aque
ous feed containing the most hydrophobic low-boiler, i.e. ethyl acetate. A
second series of experiments was carried out on unfilled membranes (selecti
ve layer composed of PDMS and PEBA) with high-boiling aroma compounds (S-me
thylthiobutanoate and gamma-decalactone). In both cases, selectivities were
highly dependent of the total permeate pressure. The PDMS membrane display
ed an unusual behaviour with gamma-decalactone, as it appeared that the lac
tone flux was not induced by a difference in partial pressure at each side
of the membrane. Whatever the nature of the membrane-aroma compound associa
tions, the transmembrane transfer coefficient model resulted in an accurate
prediction of the selectivity pervaporation operation over a large range o
f total permeate pressure. (C) 1999 Elsevier Science B.V. All rights reserv
ed.