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UBC Theses and Dissertations
Modelling of fluid flow and protein transport in hollow-fibre bioreactors Labecki, Marek
Abstract
A mathematical model (the Porous Medium Model, PMM) was developed to predict the
fluid flow and solute transport in hollow-fibre devices, with a particular emphasis on hollowfibre
bioreactors (HFBRs). In the PMM, both the extracapillary space (ECS) and the lumen
side are treated as interpenetrating porous regions with a continuous source or sink of fluid.
The hydrodynamic equations of the PMM are based on Darcy's law and continuity
considerations while the transport of the ECS protein is described by the time-dependent
convective-diffusion equation. Compared to the earlier Krogh Cylinder Model (KCM), in
which the fluid flow and protein transport are assumed to be the same for each fibre, the
PMM represents an improved approach in which the spatial domain corresponds to the real
dimensions of the hollow-fibre module. Thus, it can be applied to operating conditions where
macroscopic radial pressure and concentration gradients exist, such as in open-shell
operations. It was demonstrated that, in the absence of radial gradients, the PMM becomes
mathematically equivalent to the one-dimensional KCM. The PMM also takes into account
the osmotic pressure dependence on the ECS protein concentration, which causes a coupling
of the hydrodynamic and protein transport equations.
The Porous Medium Model was tested by applying it to one- and two-dimensional
closed-shell operations. Both confirmed that a significant polarization of the ECS protein
occurs in the direction of the existing pressure gradients under dominant convective transport
conditions. The downstream polarization of protein affects HFBR hydrodynamics by virtually
shutting down the flow in a significant portion of the ECS due to locally high osmotic
pressures. It can also facilitate harvesting of the product protein by increasing its
concentration near the downstream ECS port. Modelling studies of the hydrodynamics of hollow-fibre devices in the partial and full
filtration modes of operation were carried out for a wide range of membrane permeabilities
(10"14
Item Metadata
| Title |
Modelling of fluid flow and protein transport in hollow-fibre bioreactors
|
| Creator | |
| Publisher |
University of British Columbia
|
| Date Issued |
1994
|
| Description |
A mathematical model (the Porous Medium Model, PMM) was developed to predict the
fluid flow and solute transport in hollow-fibre devices, with a particular emphasis on hollowfibre
bioreactors (HFBRs). In the PMM, both the extracapillary space (ECS) and the lumen
side are treated as interpenetrating porous regions with a continuous source or sink of fluid.
The hydrodynamic equations of the PMM are based on Darcy's law and continuity
considerations while the transport of the ECS protein is described by the time-dependent
convective-diffusion equation. Compared to the earlier Krogh Cylinder Model (KCM), in
which the fluid flow and protein transport are assumed to be the same for each fibre, the
PMM represents an improved approach in which the spatial domain corresponds to the real
dimensions of the hollow-fibre module. Thus, it can be applied to operating conditions where
macroscopic radial pressure and concentration gradients exist, such as in open-shell
operations. It was demonstrated that, in the absence of radial gradients, the PMM becomes
mathematically equivalent to the one-dimensional KCM. The PMM also takes into account
the osmotic pressure dependence on the ECS protein concentration, which causes a coupling
of the hydrodynamic and protein transport equations.
The Porous Medium Model was tested by applying it to one- and two-dimensional
closed-shell operations. Both confirmed that a significant polarization of the ECS protein
occurs in the direction of the existing pressure gradients under dominant convective transport
conditions. The downstream polarization of protein affects HFBR hydrodynamics by virtually
shutting down the flow in a significant portion of the ECS due to locally high osmotic
pressures. It can also facilitate harvesting of the product protein by increasing its
concentration near the downstream ECS port. Modelling studies of the hydrodynamics of hollow-fibre devices in the partial and full
filtration modes of operation were carried out for a wide range of membrane permeabilities
(10"14
|
| Extent |
5550436 bytes
|
| Genre | |
| Type | |
| File Format |
application/pdf
|
| Language |
eng
|
| Date Available |
2009-03-03
|
| Provider |
Vancouver : University of British Columbia Library
|
| Rights |
For non-commercial purposes only, such as research, private study and education. Additional conditions apply, see Terms of Use https://open.library.ubc.ca/terms_of_use.
|
| DOI |
10.14288/1.0087507
|
| URI | |
| Degree (Theses) | |
| Program (Theses) | |
| Affiliation | |
| Degree Grantor |
University of British Columbia
|
| Graduation Date |
1994-11
|
| Campus | |
| Scholarly Level |
Graduate
|
| Aggregated Source Repository |
DSpace
|
Item Media
Item Citations and Data
Rights
For non-commercial purposes only, such as research, private study and education. Additional conditions apply, see Terms of Use https://open.library.ubc.ca/terms_of_use.