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Scaling up animal cell culture
Chapter 9 from ‘The Basics’ = Chapter 26 from
‘Culture of Animal Cell Culture’
Why scale-up cultures?
What are small cultures?
Experiments requiring large number of
replicates
Determination of concentration-dependent
effects
Multi-well plates accommodate culture
volumes 2-3mls
What are small cultures?
Experiments require multiple samples
- To observe cell growth and to perform
substrate or product assays
- Culture volumes – 100 ml
- Conducted in T-flasks or spinner flasks in
Incubator
Why scale-up cultures?
Required to produce substantial quantities of
a cell product – such as virus or glycoprotein
or enzymes
Two approaches
- A Multiple process involving 1000 culture
flasks (100 ml)
- A Unit process involving 100-liter fermenter
Factors to control in Fermenters/Bioreactors?
Commercial Cultures 1 – 5 liters
Oxygen supply, temperature control, pH
control and culture mixing
Electrodes
Choice of Bioreactor
Equipment designed to grow cells in culture
Type and design of bioreactor and mode of
operation
- Depends on cell densities and productivity
The Stirred tank reactor (STR)
 Simplest and most
widely used
 Consists of cylindrical
vessel with a stirrer (a
pot and paddle)
 Designed differently for
animal cells and for
bacterial or fungal
cultures
Bioreactors
The Stirred tank reactor (STR)
Large-scale animal cell culture processes –
10,000 liters
- Stainless steel
Bench-top STRs (1-5 liters)
- Glass
What are the parameters that control
adequate culture growth?
Agitation –
Bubble bursting on culture surface resulting
from culture aeration
Stirring speed is low – rotation of a
suspended bar by a magnetic stirrer
- are not suitable in larger volumes
Impellers – vertical and horizontal movement
Parameter - Agitation
Maximum stirring rates for suspension – 100-
150 rpm
Microcarrier - < 40 rpm (suspension and
anchorage dependent cells)
Round bottom (animal cells) and flat
bottomed vessels (bacterial cells)
Parameter – Temperature control
Thermocirculator – pumps heated water
around an outer jacket
- Larger fermenters – pumps water through
coiled pipes within culture
Circulating warm air
Low volume fermenters – External heating
pads
Parameter – pH control
Optimal pH - 7.4 – for maximum growth
Enriched Co2 atmosphere decreases pH
fluctuations
1-litre culture @ 2x106 cells/ml @ gas flow of
100 ml/min
Parameter – pH control
Direct acid or alkali addition
Net acidic production (lactic acid) from
cellular metabolism – alkali (NaHCO3)
HCl is added
Computer-controlled pump or gas valve to a
pre-set pH value
Rotameters indicate rate of gas flow –
controlled by flow regulators (fig-9.6)
Parameter – Oxygen supply
Major problem
Gas diffusion from head space through culture
surface decreases
Oxygen transfer rate (OTR) across liquid
surface > Oxygen utilization rate (OUR)
What is Sparging?
 Common in bacterial cultures
 Cell damage is caused – bubble bursting
 Leads to foaming
 Alternative method – Surround gas sparger by fine-mesh
cage
Parameter – Oxygen supply
Control of oxygen supply by a sterilizable
oxygen probe
Solubility of oxygen in media can be
increased by addition of some liquid
perfluorocarbons
Indirect aeration – Oxygen supply
Indirect aeration involves medium sparging
Suitable for media recirculation
Oxygen supplied by gas diffusion through
thin walled silicone tubing
1 meter of tubing/2 liters of culture
(adequate twining or binding)
Alternative types of Bioreactors
 Airlift fermenter
 Consists of tall column
with an inner draught
tube
 Fluid circulation is
provided by stream of
air
 Less bubbling or
foaming
 Production of
monoclonal antibodies
Alternative types of Bioreactors
 Hollow-fiber
 Cartridge made up of
several thousand
minute capillary-like
plastic tubules (fibers)
with perfusable
membrane walls
 Anchorage-dependent
and independent cells
Alternative types of Bioreactors
Packed-bed or fixed-bed bioreactor
Support matrix for attachment and growth of
anchorage dependent cells
Continuous flow of medium
Glass bead column, ceramic and fluidized-
bed bioreactors
Alternative types of Bioreactors
 Glass bead column
 Glass column-glass
beads with a diameter
of 3-5 mm
 Medium is
recirculated through
packed bed by pump
and oxygenated by air
Alternative types of Bioreactors
 Ceramic bioreactor
 Series of channels run
through ceramic
cylinder
 Each channel is a square
with 1mm sides and an
inner surface area for
cell attachment
 No longer in use
Alternative types of Bioreactors
 Cell Cube
 Stack of 20 cm2
polystrene plates
spaced 1mm apart by
rigid spacers
 Cells attach to either
side of plate
 Flow of culture
medium between plates
 Production of vaccines
Alternative types of Bioreactors
 Fluidized-bed reactor
 Upward flow of
medium recirculated
by pumping
 Cells immobilized or
entrapped in beads are
held in suspension in
column
 This project is funded by a grant awarded under the President’s Community Based Job Training Grant as
implemented by the U.S. Department of Labor’s Employment and Training Administration (CB-15-162-06-60).
NCC is an equal opportunity employer and does not discriminate on the following basis:
 against any individual in the United States, on the basis of race, color, religion, sex, national origin, age disability,
political affiliation or belief; and
 against any beneficiary of programs financially assisted under Title I of the Workforce Investment Act of 1998
(WIA), on the basis of the beneficiary’s citizenship/status as a lawfully admitted immigrant authorized to work in
the United States, or his or her participation in any WIA Title I-financially assisted program or activity.
Disclaimer
 This workforce solution was funded by a grant awarded under the
President’s Community-Based Job Training Grants as implemented
by the U.S. Department of Labor’s Employment and Training
Administration. The solution was created by the grantee and does
not necessarily reflect the official position of the U.S. Department of
Labor. The Department of Labor makes no guarantees, warranties,
or assurances of any kind, express or implied, with respect to such
information, including any information on linked sites and including,
but not limited to, accuracy of the information or its completeness,
timeliness, usefulness, adequacy, continued availability, or
ownership. This solution is copyrighted by the institution that
created it. Internal use by an organization and/or personal use by
an individual for non-commercial purposes is permissible. All other
uses require the prior authorization of the copyright owner.

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Scaling up animal cell culture using Bioreactors.ppt

  • 1. Scaling up animal cell culture Chapter 9 from ‘The Basics’ = Chapter 26 from ‘Culture of Animal Cell Culture’
  • 2. Why scale-up cultures? What are small cultures? Experiments requiring large number of replicates Determination of concentration-dependent effects Multi-well plates accommodate culture volumes 2-3mls
  • 3. What are small cultures? Experiments require multiple samples - To observe cell growth and to perform substrate or product assays - Culture volumes – 100 ml - Conducted in T-flasks or spinner flasks in Incubator
  • 4. Why scale-up cultures? Required to produce substantial quantities of a cell product – such as virus or glycoprotein or enzymes Two approaches - A Multiple process involving 1000 culture flasks (100 ml) - A Unit process involving 100-liter fermenter
  • 5. Factors to control in Fermenters/Bioreactors? Commercial Cultures 1 – 5 liters Oxygen supply, temperature control, pH control and culture mixing Electrodes
  • 6. Choice of Bioreactor Equipment designed to grow cells in culture Type and design of bioreactor and mode of operation - Depends on cell densities and productivity
  • 7. The Stirred tank reactor (STR)  Simplest and most widely used  Consists of cylindrical vessel with a stirrer (a pot and paddle)  Designed differently for animal cells and for bacterial or fungal cultures
  • 9. The Stirred tank reactor (STR) Large-scale animal cell culture processes – 10,000 liters - Stainless steel Bench-top STRs (1-5 liters) - Glass
  • 10.
  • 11. What are the parameters that control adequate culture growth? Agitation – Bubble bursting on culture surface resulting from culture aeration Stirring speed is low – rotation of a suspended bar by a magnetic stirrer - are not suitable in larger volumes Impellers – vertical and horizontal movement
  • 12. Parameter - Agitation Maximum stirring rates for suspension – 100- 150 rpm Microcarrier - < 40 rpm (suspension and anchorage dependent cells) Round bottom (animal cells) and flat bottomed vessels (bacterial cells)
  • 13. Parameter – Temperature control Thermocirculator – pumps heated water around an outer jacket - Larger fermenters – pumps water through coiled pipes within culture Circulating warm air Low volume fermenters – External heating pads
  • 14. Parameter – pH control Optimal pH - 7.4 – for maximum growth Enriched Co2 atmosphere decreases pH fluctuations 1-litre culture @ 2x106 cells/ml @ gas flow of 100 ml/min
  • 15.
  • 16. Parameter – pH control Direct acid or alkali addition Net acidic production (lactic acid) from cellular metabolism – alkali (NaHCO3) HCl is added Computer-controlled pump or gas valve to a pre-set pH value Rotameters indicate rate of gas flow – controlled by flow regulators (fig-9.6)
  • 17. Parameter – Oxygen supply Major problem Gas diffusion from head space through culture surface decreases Oxygen transfer rate (OTR) across liquid surface > Oxygen utilization rate (OUR)
  • 18. What is Sparging?  Common in bacterial cultures  Cell damage is caused – bubble bursting  Leads to foaming  Alternative method – Surround gas sparger by fine-mesh cage
  • 19. Parameter – Oxygen supply Control of oxygen supply by a sterilizable oxygen probe Solubility of oxygen in media can be increased by addition of some liquid perfluorocarbons
  • 20. Indirect aeration – Oxygen supply Indirect aeration involves medium sparging Suitable for media recirculation Oxygen supplied by gas diffusion through thin walled silicone tubing 1 meter of tubing/2 liters of culture (adequate twining or binding)
  • 21. Alternative types of Bioreactors  Airlift fermenter  Consists of tall column with an inner draught tube  Fluid circulation is provided by stream of air  Less bubbling or foaming  Production of monoclonal antibodies
  • 22. Alternative types of Bioreactors  Hollow-fiber  Cartridge made up of several thousand minute capillary-like plastic tubules (fibers) with perfusable membrane walls  Anchorage-dependent and independent cells
  • 23. Alternative types of Bioreactors Packed-bed or fixed-bed bioreactor Support matrix for attachment and growth of anchorage dependent cells Continuous flow of medium Glass bead column, ceramic and fluidized- bed bioreactors
  • 24. Alternative types of Bioreactors  Glass bead column  Glass column-glass beads with a diameter of 3-5 mm  Medium is recirculated through packed bed by pump and oxygenated by air
  • 25. Alternative types of Bioreactors  Ceramic bioreactor  Series of channels run through ceramic cylinder  Each channel is a square with 1mm sides and an inner surface area for cell attachment  No longer in use
  • 26. Alternative types of Bioreactors  Cell Cube  Stack of 20 cm2 polystrene plates spaced 1mm apart by rigid spacers  Cells attach to either side of plate  Flow of culture medium between plates  Production of vaccines
  • 27. Alternative types of Bioreactors  Fluidized-bed reactor  Upward flow of medium recirculated by pumping  Cells immobilized or entrapped in beads are held in suspension in column
  • 28.  This project is funded by a grant awarded under the President’s Community Based Job Training Grant as implemented by the U.S. Department of Labor’s Employment and Training Administration (CB-15-162-06-60). NCC is an equal opportunity employer and does not discriminate on the following basis:  against any individual in the United States, on the basis of race, color, religion, sex, national origin, age disability, political affiliation or belief; and  against any beneficiary of programs financially assisted under Title I of the Workforce Investment Act of 1998 (WIA), on the basis of the beneficiary’s citizenship/status as a lawfully admitted immigrant authorized to work in the United States, or his or her participation in any WIA Title I-financially assisted program or activity.
  • 29. Disclaimer  This workforce solution was funded by a grant awarded under the President’s Community-Based Job Training Grants as implemented by the U.S. Department of Labor’s Employment and Training Administration. The solution was created by the grantee and does not necessarily reflect the official position of the U.S. Department of Labor. The Department of Labor makes no guarantees, warranties, or assurances of any kind, express or implied, with respect to such information, including any information on linked sites and including, but not limited to, accuracy of the information or its completeness, timeliness, usefulness, adequacy, continued availability, or ownership. This solution is copyrighted by the institution that created it. Internal use by an organization and/or personal use by an individual for non-commercial purposes is permissible. All other uses require the prior authorization of the copyright owner.