In this research the liquid phase esterification of hexanoic acid and I-oct
anol was studied. Very high activities were obtained for zeolite BEA and Na
fion/silica composite with 13% of Nafion. The advantage of water removal in
this system was demonstrated. In a closed system an equilibrium conversion
of 35% was reached, while in a system with water removal all the reactants
were converted in a shorter period. The initial reaction rate decreases wh
en increasing the initial water concentration, following a Langmuir-Hinshel
wood type of rate expression. An active zeolite coated structured monolithi
c reactor configuration was prepared. Enhancement by the counter-current wa
ter stripping of the performance of the structured catalysts was demonstrat
ed. (C) 2001 Elsevier Science B.V. All rights reserved.