The hydrolysis of racemic methyl ibuprofen ester in the presence of lipase
from Candida rugosa was investigated in shake flasks. Experiments were perf
ormed to study the effect of temperature, pH and shaking speed on the react
ion rate. Different hydrophobic co-solvents were screened for the highest r
eaction rate and the presence of enzyme inhibition by substrate and product
s was examined. A kinetic expression was then proposed to describe the reac
tion. Kinetic parameters were determined for the optimum operating conditio
ns and the proposed model was verified with the experimental results. Next,
this reaction was scaled up to a fed batch stirred tank reactor. Batch rea
ctor and fed batch reactor configurations were compared for better conversi
ons. The effects of aqueous phase hold-up, substrate concentration and feed
flow rate on the conversion of the reaction were also studied. Higher conv
ersions were obtained in a fed batch reactor when compared with the batch r
eactor. In the fed batch reactor, increased conversions were observed with
lower feed flowrates and high aqueous phase hold-up. (C) 2001 Society of Ch
emical Industry.