BACKGROUND: Biochemical oxidation reactions require oxygen to be supplied by dispersed bubbles. Drawbacks of the gas-liquid system are enzyme denaturation and low oxygen utilization efficiency. Therefore, oxygen production through the decomposition of H 2 O 2 is useful for controlled oxygen transfer in bioreactors.
RESULTS:Catalase-containing liposomes (CALs) were prepared in 50 mmol L -1 Tris/0.1 mol L -1 NaCl buffer (pH 7.4) and the kinetic model was developed for the oxygen production by CAL-catalyzed decomposition of 1.0 mmol L -1 H 2 O 2 . Applying the model to the observed time course of oxygen produced gave overall resistance in the reaction based on the pseudo-steadystate assumption inside liposomes for H 2 O 2 and oxygen. The reaction resistance was estimated with the liposomal catalase concentration e t,in and the kinetic parameters of free enzyme reaction. At e t,in = 0.59 μmol L -1 , the CAL reaction proceeded under reaction control, while at e t,in = 5.05 μmol L -1 , the H 2 O 2 transfer resistance was involved. For the latter case, the permeability coefficient P P of H 2 O 2 through the liposome membrane was determined as 1.06 × 10 -6 m s -1 at 25 • C. The model predicted the H 2 O 2 concentration inside liposomes with different e t,in values. Furthermore, the oxygen concentration in the CAL dispersions was reasonably simulated. The oxygen production rate could be altered based on temperature (10-55 • C) and the fractional volume of CALs. CONCLUSION: The CAL-catalyzed oxygen production was controlled based on the e t,in and P P values, which determine the relative importance of the reaction and H 2 O 2 transfer resistances. The CAL would be applied to oxidation reactions instead of gas-liquid systems.