Recently, the use of supercritical CO2 (SCCO2) as a solvent in enzyme-catal
yzed reactions has been a matter of considerable research because of its fa
vorable transport properties that can accelerate mass-transfer-limited enzy
matic reactions. Further, biocatalysts, especially lipases, have substrate
speciff city and catalyze the syntheses of esters from a variety of acids a
nd alcohols in SCCO2. Fatty acid esters obtained from alcoholysis of vegeta
ble oils have many applications, such as antifriction agents, food preserva
tives, and emulsifiers. However, despite the industrial importance of the p
roducts obtained from alcoholysis of vegetable oils, conversions of such re
actions in SCCO2 have hardly been reported in the literature. Hence, the ma
in objective of this work is to study the ethanolysis of palm kernel oil in
SCCO2 as catalyzed by two commercial Lipases. The experiments were perform
ed in a reactor vessel in the temperature range of 40-70 degreesC and from
60 to 200 bar using a water concentration of 0-10 wt % and oil/ethanol mola
r ratios fl om 1:3 to 1:10. The initial reaction rate was found to be a fun
ction of both pressure and the oil/ethanol molar ratio. A simple model, cap
able of representing the conversion-time relationship curve, is proposed.