Abstract
An analytical model has been developed which describes the performance of a packed-bed immobilized enzyme reactor. In particular, two-substrate, reaction kinetics, thermodynamic equilibrium of complexation between one of the substrates and a ligand, and substrate diffusion processes are considered. Numerical simulations were performed and the results suggest that, when substrate-ligand binding occurs either in the bulk phase alone or in both the bulk and the pore phases, distinct effects are to be expected.
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