Kinetics of single-substrate enzyme-catalyzed reactions in batch reactor (BR) using thermokinetic method were investigated

and the influence of product competitive inhibition on these models was discussed in details. Catalase-catalyzed decomposition of H2O2 and arginase-catalyzed hydrolysis of L-arginine were studied by microcalorimetry

and the reliability of this thermokinetic method applied to the study of kinetics of single-substrate enzyme-catalyzed reactions in BR has been verified by the experimental data.