Diffusional mass transfer limitations in hollow fiber bioreactors - with de
nsely packed whole cells in its extracapillary space to perform biotransfor
mation reactions - have been studied theoretically using a steady-state dif
fusion and reaction model. Simple analytical expressions have been derived
to calculate the radial and axial concentration profiles for zero- and firs
t-order kinetics, as well as to plot effectiveness factor versus Thiele mod
ulus plots for first-order kinetics. The influence of the magnitude of the
effective diffusion coefficients, the thickness of the isotropic membrane a
s well as the size of the annular cell region have been assessed to optimis
e the reactor performance.