A diffusion model based on the random pore model is derived for immobilized
cell biocatalysts and verified with 19 sets of experimental diffusion data
. The predicted effective diffusivity relative to that for the support matr
ix reflects a quadratic dependence on the cell loading and contains a singl
e parameter that depends on the intracellular diffusivity and the chemical
partitioning coefficient. The model is used to predict optimal cell loading
s that maximize the total reaction rate in an immobilized cell biocatalyst.
A rule of thumb based on the diffusion model is obtained to the effect tha
t the cell loading should be at least 1/3 for single reactions regardless o
f the kinetics and diffusional resistances. A means of calculating improved
lower bounds is provided for cases where the cellular diffusional resistan
ce is known but the kinetics are not. The optimal cell loadings for reversi
ble first-order and for Michaelis-Menten kinetics are presented and demonst
rated to be within the range of conditions of practical interest. (C) 2000
John Wiley & Sons, Inc.