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Chapter 6: Plant and Animal Cell
Bioreactors
Function
Microbial System
Plant Cell System
Bulk mixing
To achieve homogeneity of
chemical environment in
the presence of nutrient
sink and product source
terms
To achieve homogeneity of
biomass distribution in the
presence of sedimentation
due to large size of cell
aggregates
Oxygen transfer
To meet oxygen supply
requirements of the
biomass, often limiting in
scale up
To meet oxygen
requirement of the
growing biomass without
depleting the
concentration of gaseous
products below a critical
level
Shear
Usually unimportant.
Usually very important due
to large size of cells and
aggregates.
Mammalian Cells
Stages in Cell Culture
• Primary cells
– Tissue taken from its original site and transferred
to an artificial medium for growth
– Requires the recurrent sacrifice of animals
• Secondary cells
– After the first passage of primary cells
– Have a finite number of passages
• Continuous or transformed cells
– Cells that can be subcultured indefinitely
Types of Mammalian Cells
•
Anchorage
Dependent cells
–
Require surface
attachment to grow
–
They include mostly
primary cells and
cell lines such as :
-Chinese Hamster
Ovary cells (CHO),
Baby Hamster
Kidney Cells (BHK)
and
Human Fibroblast
cells (FS-4)
• Suspension cells
– Cells not
requiring any
surface
attachment
– Examples are:
HeLa cells,
hybridoma cells
and other tumor
cells
Some Aspects of Bioreactor Design
Design of Bio –Engineering Equipment
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Vessel Design (Height : Diameter ratio)
Agitation
Mechanical seal
Stirrer
Inlet air
Aeration
Ports
Exhaust air
Inoculation port
Sampling valve/port
Harvest
Media Addition
Air sterilization
Special Considerations for Mammalian
Cell Bioreactor
• Cells are shear sensitive thus shearing should
be minimized
• Oxygenation through bubbling may damage
cells
• Round bottom culture vessel with aspect ratio
of 2:1
Special Modifications
Aeration and
Mixing
Modes of Operation
Batch mode of operation
A
well established production
method; generally used for vaccines The operation modes all
lack in the ability to
and biopharmaceuticals.
Stirred-Tank
Reactor
Low
Batch
select or differentiate
between viable and
non-viable cells
yield of product
Fed-batch mode
High
Feed
density culture
Longer
operation and higher yield
Accumulation
of dead cells and debris
Continuous mode
Fed-batch
Feed
High
density culture
Product
Harvest
can be harvested
continuously
Limited
Continuous
dilution rate
Perfusion Culture

Recycle
Feed
Harvest
Cell separation
device
Cell Separation
Methods in
Perfusion Mode
1. Filtration
2. Centrifugation
3. Gravitational settling
4. Immobilisation
Perfusion mode
 High density culture
 Product can be harvested
continuously
 High productivity
 Dilution rate not limited
 Separation of viable and dead
cells possible
All Perfusion strategies
must meet the following
conditions:
1. Stable operation
2. Easy to scale up
3. Versatility:The process can be
applied to any cells and any culture
medium
•Volume of the production
unit is smaller than
normally required with
batch culture.
•Lower investment cost on
the bioreactor.
Liquid
addition
Liquid
withd rawal
Liquid level in
bioreacto r
Sp in filter

Perfusion Culture
Systems

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

Spin filter bioreactors
Cell settler for perfusion culture
Centrifugal bioreactor
Tangential flow or crossflow filtratio
device for perfusion culture
Packed-bed basket perfusion culture
Fresh medium
pump
Air in
Spent medium
Celligen packed-bed
basket reactor (Wang et al.,1993)
Fibrous bed basket
Cell free medium
Draft tube
Make a comparison of an animal cell bioreactor
with a plant cell bioreactor.