This paper presents results on the kinetics of the hydrolysis of sunflower
oil catalysed by the enzymes of Candida cylindracea. The influence of the a
gitation is focused, in a standardized reactor, with a Rushton turbine as t
he agitating element. It is proved that an increase of the agitation speed
improves the kinetics of the reaction up to a certain value of the rotation
al speed where the agitation becomes turbulent. A large range of substrate
concentrations is investigated and discussed compared to the usual conditio
ns met in the literature.