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TYPES OF
BIOREACTORS
Types of Bioreactors
 Stirred tank bioreactor
 Pneumatically Agitated bioreactors:
Airlift bioreactor
Loop reactor
Bubble Column
 Immobilized microorganism reactors
 Membrane Reactors
 Photobioreactors
A disposable bioreactor
Immobilized bioreactor
A pilot plant bioreactor
Strategies for Choosing a
Bioreactor
 Microorganism species
 Growth and oxygen requirements
 Shear and rheology effects
 Cleaning and Sterility
 Light
 Foam
 Heating and cooling
 Materials of construction
Stirred Tank Bioreactors
 The most important type of bioreactor for
industrial production processes.
 Low capital and operating costs.
 Depending largely on the amount of heat to be
removed, the stirrer may be top- or bottom
driven.
 Tanks are fitted with baffles, which prevent
large central vortex as well as to improve
mixing.
 High agitation and aeration cause major
problems such as foaming, which may lead to
unknown contamination.
Stirred tank bioreactor
Schematic Diagram of a Stirred
Tank Bioreactor
Bubble Column Reactor
 Used in production of Baker’s yeast, beer and
vinegar.
 Also used in aeration and treatment of
wastewater.
 In bubble columns, the hydrodynamics and
mass transfer depend on the size of bubbles
and how they are released from the sparger.
Airlift Bioreactor
 Mixing is accomplished without any mechanical
agitation.
 Used for tissue culture because the tissues are
sensitive to shear stress, thus normal mixing is
not possible.
 Air is fed into the bottom of a central draught tube
through a sparger ring. The flow passes up
through the draft tube to the head space of the
bioreactor, where excess air, by-product and CO2
disengage.
 In general, airlift bioreactors the following
features:
 Internal loop or
 External loop
Difference between bubble column
and airlift bioreactor
Advantages of an Airlift
Bioreactor
 Low shear, which means it can be used for
plant and animal cells.
 Since there is no agitation, sterility is easily
maintained.
 In a large vessel, the height of the liquid can
be as high as 60m, the pressure at the bottom
of the vessel will increase the oxygen
solubility, thus increase the mass transfer.
 Extremely large vessel can be constructed.
Disadvantages of Airlift
Bioreactors
 High capital cost with large scale vessel.
 High energy cost. Although an agitator is not
required, a greater air throughput is necessary,
and the air has to be at higher pressure,
especially if large scale.
 As the microorganism circulate through the
bioreactor, the conditions change, and it is
impossible to maintain consistent levels of carbon
source, nutrients and oxygen throughout the
vessel.
 The separation of gas from the liquid is not very
efficient when foam is present.
In the design of an airlift bioreactor, these
disadvantages must be minimised.
Immobilized Cell Bioreactor
(ICB)
 Enzymes, viable cells, plant cells and animal cells
can be immobilized.
 It can be divided into stirred tank reactors, fixed bed
reactors, fluidized bed reactors. These reactors can
also be combined or modified.
 The choice of reactor design for an ICB would
depend on:
 Mass transfer requirements, eg. Oxygen supply and gas
removal
 Particle characteristics, eg. In stirred tank reactor,
damage to the particle is greater than in packed bed
reactor.
 Kinetic considerations
Methods of Immobilization
Methods of
Immobilization
Active
Immobilization
Cross-
linking
Covalent
bonding
Entrapment
in Gels
Passive
Immobilization
Adsorption Colonization
Advantages of immobilized Cell
Bioreactor
 Application to multi-step enzyme reaction may be
possible.
 The enzyme activity yield on immobilization is high.
 Operational stability is generally high.
 Operations for enzyme extraction and/or purification
are unnecessary.
 High cell densities can be employed.
 Cell densities and enzyme activities can be expected
to be maintained over a long period of operation.
 Products can be easily removed from immobilized
cells
 Immobilized cells appear to be less susceptible to
microbial contamination.
Disadvantages of Immobilized Cell
Reactor
 The cells may contain numerous catalytically
active enzymes, which may catalyze unwanted
side reactions.
 The cell membrane itself may serve as a
diffusion barrier, thus reducing productivity.
 Contamination by cells leaking out from
carriers may occur.
 The physiological state of the microorganism
cannot be controlled.
Immobilized yeast cells
Membrane Reactors
 A membrane reactor is a flow reactor within which
membranes are used to separate cells or enzymes from the
feed or product streams.
 Usually a continuous system.
 Products may also be removed continuously, but in some
applications they must be harvested intermittently or at the
end of the run.
 Polymeric microfiltration (0.1 – 5 μm) or ultrafiltration (20 –
1000 Å) membranes are most commonly used.
 Membranes are obtained in hollow-fiber or flatsheet form.
 Application in enzymatic reaction, production of primary and
secondary metabolites by microorganisms and plant cells,
generation of antibodies by mammalian cells.
Advantages of Membrane
Reactors
 A consequence of the retention of cells or
enzymes within the reactors. This allows the
reactors to be continuously perfused without
worrying about washout.
 Membrane also provide an in-situ separation
of the cells or enzymes from the product.
 Compared to immobilization technique, no
chemical agents or harsh conditions are
employed.
Challenges in Membrane
Reactors
 Cells and enzymes entrapped within
membrane reactors are subject to diffusion
and convection that can render their
distribution heterogeneous.
 An uneven flow distribution among the various
channels in a membrane reactor can have
significant effect.
Photobioreactors
 Designed for applications such as wastewater
treatment, water quality management,
remediation of contaminated soil.
 Organisms used: green and blue-green
(bacteria) algae, photoautotrophs,
photoheterotrophs
 Culture systems utilizing ponds or rectangular
tanks with limited mixing.
 Deep channeled culture systems with a closed
circulating loop and better mixing.
Photobioreactor

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Fermenter.pptx

  • 2. Types of Bioreactors  Stirred tank bioreactor  Pneumatically Agitated bioreactors: Airlift bioreactor Loop reactor Bubble Column  Immobilized microorganism reactors  Membrane Reactors  Photobioreactors
  • 3. A disposable bioreactor Immobilized bioreactor A pilot plant bioreactor
  • 4. Strategies for Choosing a Bioreactor  Microorganism species  Growth and oxygen requirements  Shear and rheology effects  Cleaning and Sterility  Light  Foam  Heating and cooling  Materials of construction
  • 5. Stirred Tank Bioreactors  The most important type of bioreactor for industrial production processes.  Low capital and operating costs.  Depending largely on the amount of heat to be removed, the stirrer may be top- or bottom driven.  Tanks are fitted with baffles, which prevent large central vortex as well as to improve mixing.  High agitation and aeration cause major problems such as foaming, which may lead to unknown contamination.
  • 7. Schematic Diagram of a Stirred Tank Bioreactor
  • 8. Bubble Column Reactor  Used in production of Baker’s yeast, beer and vinegar.  Also used in aeration and treatment of wastewater.  In bubble columns, the hydrodynamics and mass transfer depend on the size of bubbles and how they are released from the sparger.
  • 9.
  • 10. Airlift Bioreactor  Mixing is accomplished without any mechanical agitation.  Used for tissue culture because the tissues are sensitive to shear stress, thus normal mixing is not possible.  Air is fed into the bottom of a central draught tube through a sparger ring. The flow passes up through the draft tube to the head space of the bioreactor, where excess air, by-product and CO2 disengage.  In general, airlift bioreactors the following features:  Internal loop or  External loop
  • 11. Difference between bubble column and airlift bioreactor
  • 12. Advantages of an Airlift Bioreactor  Low shear, which means it can be used for plant and animal cells.  Since there is no agitation, sterility is easily maintained.  In a large vessel, the height of the liquid can be as high as 60m, the pressure at the bottom of the vessel will increase the oxygen solubility, thus increase the mass transfer.  Extremely large vessel can be constructed.
  • 13. Disadvantages of Airlift Bioreactors  High capital cost with large scale vessel.  High energy cost. Although an agitator is not required, a greater air throughput is necessary, and the air has to be at higher pressure, especially if large scale.  As the microorganism circulate through the bioreactor, the conditions change, and it is impossible to maintain consistent levels of carbon source, nutrients and oxygen throughout the vessel.  The separation of gas from the liquid is not very efficient when foam is present. In the design of an airlift bioreactor, these disadvantages must be minimised.
  • 14.
  • 15. Immobilized Cell Bioreactor (ICB)  Enzymes, viable cells, plant cells and animal cells can be immobilized.  It can be divided into stirred tank reactors, fixed bed reactors, fluidized bed reactors. These reactors can also be combined or modified.  The choice of reactor design for an ICB would depend on:  Mass transfer requirements, eg. Oxygen supply and gas removal  Particle characteristics, eg. In stirred tank reactor, damage to the particle is greater than in packed bed reactor.  Kinetic considerations
  • 16. Methods of Immobilization Methods of Immobilization Active Immobilization Cross- linking Covalent bonding Entrapment in Gels Passive Immobilization Adsorption Colonization
  • 17. Advantages of immobilized Cell Bioreactor  Application to multi-step enzyme reaction may be possible.  The enzyme activity yield on immobilization is high.  Operational stability is generally high.  Operations for enzyme extraction and/or purification are unnecessary.  High cell densities can be employed.  Cell densities and enzyme activities can be expected to be maintained over a long period of operation.  Products can be easily removed from immobilized cells  Immobilized cells appear to be less susceptible to microbial contamination.
  • 18. Disadvantages of Immobilized Cell Reactor  The cells may contain numerous catalytically active enzymes, which may catalyze unwanted side reactions.  The cell membrane itself may serve as a diffusion barrier, thus reducing productivity.  Contamination by cells leaking out from carriers may occur.  The physiological state of the microorganism cannot be controlled.
  • 19.
  • 21. Membrane Reactors  A membrane reactor is a flow reactor within which membranes are used to separate cells or enzymes from the feed or product streams.  Usually a continuous system.  Products may also be removed continuously, but in some applications they must be harvested intermittently or at the end of the run.  Polymeric microfiltration (0.1 – 5 μm) or ultrafiltration (20 – 1000 Å) membranes are most commonly used.  Membranes are obtained in hollow-fiber or flatsheet form.  Application in enzymatic reaction, production of primary and secondary metabolites by microorganisms and plant cells, generation of antibodies by mammalian cells.
  • 22. Advantages of Membrane Reactors  A consequence of the retention of cells or enzymes within the reactors. This allows the reactors to be continuously perfused without worrying about washout.  Membrane also provide an in-situ separation of the cells or enzymes from the product.  Compared to immobilization technique, no chemical agents or harsh conditions are employed.
  • 23. Challenges in Membrane Reactors  Cells and enzymes entrapped within membrane reactors are subject to diffusion and convection that can render their distribution heterogeneous.  An uneven flow distribution among the various channels in a membrane reactor can have significant effect.
  • 24. Photobioreactors  Designed for applications such as wastewater treatment, water quality management, remediation of contaminated soil.  Organisms used: green and blue-green (bacteria) algae, photoautotrophs, photoheterotrophs  Culture systems utilizing ponds or rectangular tanks with limited mixing.  Deep channeled culture systems with a closed circulating loop and better mixing.