A mathematical model was developed to describe the coupled hydrodynami
cs and high molecular weight protein transport in cell-filled ultrafil
tration hollow-fibre bioreactors (HFBRs). The multi-fibre reactor was
represented by a single, straight fibre surrounded by a symmetry envel
ope containing a homogeneous packed bed of cells. The low Reynolds num
ber flow in this cell-packed extracapillary space (ECS) was described
by Darcy's law. Since the protein transport and HFBR hydrodynamics wer
e coupled, numerical methods were required to solve the governing equa
tions of both the two-dimensional (axial and radial) and one-dimension
al (axial) models developed to predict the redistribution of proteins
retained in the ECS. Because of the large length/radius ratio of the r
epresentative fibre unit, the two-dimensional model predictions were c
losely duplicated by the simpler one-dimensional model over a wide ran
ge of operating conditions. An HFBR filed with mammalian cells was sim
ulated experimentally by filling the ECS of a hollow-fibre module with
an agarose/protein solution to form a porous medium with uniform init
ial protein concentration. All of the ECS protein distributions, measu
red after 5-16 days of lumen flow, were adequately described by the mo
del if an effective ECS conductivity of 5 x 10(-15) m(2) was assumed.
The model was then used to predict transient and steady-state protein
distributions in HFBRs under various packed-bed conditions. It was sho
wn that, for low ECS conductivities typical of values measured for mam
malian tissues, diffusion begins to compete effectively with convectio
n as an important mechanism of axial protein transport. Also, the rate
and extent of protein polarization in these cases was greatly reduced
compared to the predictions obtained for a cell-free HFBR. The implic
ations of these findings, particularly for product protein harvesting
from a cell-packed ECS, were discussed. (C) 1997 Elsevier Science Ltd.
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