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Immobilization
Cell Culture
By:
Sukriti Singh
Sem 5, Sec D
Amity Institute of
Biotechnology NOIDA
Types of Cell culture
 Adherent Cell Culture: When
the primary cells are seeded on
or adhered to the culture
medium in high density.
 Suspension Cell Culture:
consists of single cells, small
cell groups and larger cell
aggregates dispersed in a liquid
medium and actively grow.
 Immobilization Cell Culture:
the cells are either encapsulate
or adsorbed or entrapped
within a polymeric or open
matrix.
Immobilization is often confused
with mineralisation
 Immobilization is closely related to mineralisation as
both are due to inorganic organic compounds.
 Any media has inorganic as well as organic compounds
compounds in its composition.
 Now when a cell consume inorganic compounds for its
metabolism and other organic compounds needed to be
grown then they are said to be “immobilising”, while
when a cell excrete inorganic waste compounds then
they are said to be “mineralising”.
Types of cell immobilisation
 We have already heard about enzyme immobilisation in
Enzymology, Enzyme can be immobilized through the
following techniques.
 Similarly Cells can be immobilized
in cell culture.
 The cells can be immobilised by
 covalently attached to the base
 Adsorbed or absorbed
 Cross-linked
 Encapsulate
 Assembled to a protein
 Entrapped
Different types of cell immobilization
Physical
Adsorption
The two basic cell immobilization
techniques include
 Immurement Culture/Encapsulation
 Entrapment
 Immurement Culture/Encapsulation
 Cells are encapsulated in a polymeric matrix by adsorption.
 Materials used in matrix: gelatin, polylysine, alginate(most common), Agarose.
 Medium diffuses freely into the matrix and into the cells, while product moves
out into the medium.
 For larger molecule production like MAB, Agarose in suspension of paraffin oil is
preferable to alginate since alginate does not allow diffusion of products out of
alginate beads.
 Uses
 Encapsulation protects cells from mechanical damage in large fermenters.
 Production of hormones, antibodies, immunochemical and enzymes over
much longer periods than possible in suspension culture.
 Helps in MAB production.
Immobilization of
Antibodies
 Entrapment culture
 Cells are held within an open matrix through which the
medium flows freely.
 Cells may be entrapped within porous ceramic walls of the
entrapping unit.
 Use:
 Porous micro carriers (170µm-6000µm) made up of gelatin or
collagen or glass or cellulose are arranged as fixed bed or
fluidized bed reactors or used in stirred bioreactors.
 Cells can also be enmeshed in cellulose fibres.
 Use:
 These fibres are autoclaved and washed and added in stirred
bioreactors at a certain conc.(3g/L).
 This yields upto 50g MAB/day.
Few of immobilized cells:
Cell immobilized in Ca-Alginate
Immobilisation of
prokaryotic cells
Cell immobilized in Gelatin
Cell immobilized in c) carragenan d) distilled water e) polylysine
Uses of immobilized cell
culture
 Help in making bio-transformants, biosensors.
 Secondary metabolite production.
 Biological washing powders.
 Food Industry.
 Bioreactors.
 Experimental waste water treatment.
Immobilisation of
micro algae
Immobilized algae used in
bioreactor
Immobilized micro algae (in
polymeric matrix) grown in
mixotrophic conditions used
in experimental waste water
treatment
 Immobilized Cell Preparation:
 Sodium alginate in growth medium.
 Stir until all sodium alginate is completely dissolved. No clump formation.
 Suspend wet cells in the alginate solution prepared in the above step. Let air
bubbles escape. Drip the yeast alginate mixture. The calcium crosslinking
solution is agitated on a magnetic stirrer.
 Gel formation can be achieved at room temperature as soon as the sodium
alginate drops come in direct contact with the calcium solution.
 Relatively small alginate beads are preferred to minimize the mass transfer
resistance. A diameter of 0.52mm can be readily achieved with a syringe and a
needle. The beads should fully harden in 12hours.
 Wash the beads with a fresh calcium crosslinking solution.
Ca-Alginate Immobilization of
Yeast cells Immobilisation of yeast
 Immobilized Cell Reactor Construction:
 Construct an immobilized cell reactor with a 500ml Erlenmeyer flask fitted.
 Place the hardened beads in the flask and seal it with a rubber stopper with appropriate
hose connections.
 Make all necessary connections. Start the experiment by filling the flask with the growth
media (100g/l glucose) to the working volume of 350ml.
 Immobilized Cell Reactor:
 Then following sequence of events will be monitored both online and offline.
 The responsibilities of online data acquisition and offline sample collection and analysis
will be shared by the entire class; the exact assignment will be determined in class. A
microcomputer will be programmed to take data on the glucose concentration and the
rate of NH4OH addition needed to maintain the pH at 4.0. The offline samples will be
analyzed for the optical density (for free cell concentration), glucose concentration, and
ethanol concentration.
 Furthermore, the liquid and gas flow rate will be measured with a graduated cylinder.
 The reactor will be operated in a batch manner until no more glucose is utilized. This
can be detected with the leveling off in the glucose concentration.
Ca-Alginate Immobilization of
Yeast cells
 The reactor will be operated in a batch manner until no more glucose is utilized. This
can be detected with the leveling off in the glucose concentration.
 Furthermore, the liquid and gas flow rate will be measured with a graduated cylinder.
 The reactor will be operated in a batch manner until no more glucose is utilized. This
can be detected with the leveling off in the glucose concentration.
 Substrate feeding will then commence at the rate of 0.4/hr. Record the substrate flow
rate. The approach to the first steady state during the startup will be followed.
 Various parameters (nitrogen consumption rate, carbon dioxide evolution rate, glucose
concentration, ethanol concentration, and free cell level) at the high steady state are
recorded.
 Decrease the substrate feeding rate to 0.2 /hr., Measure the substrate flow rate and
follow the transient approach to the new low steady state.
 Repeat above parts for the new steady state.
 If time permits, continue shifting the flow rate and obtain more information on steady states.
Continue operating the bioreactor until noticeable deterioration in the performance is
detected due to gel swelling, cell death, or severe contamination.
Ca-Alginate Immobilization of Yeast cells and large scale production of ethanol
Bioreactors
and
immobilised
cells
Immobilized
cells and their
use in
Bioreactors
Use of cell Immobilisation
Other benefits of using
Immobilized cell culture
 Gives higher cell density.
 Stability and longevity of cultures.
 Can be applicable to both suspension or monolayer
culture(adherent).
 Many systems protect the cells from shear forces due to
medium flow.
 Less dependence of cells at higher densities on external
supply of growth factors which saves culture cost.

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Immobilisation cell culture

  • 1. Immobilization Cell Culture By: Sukriti Singh Sem 5, Sec D Amity Institute of Biotechnology NOIDA
  • 2. Types of Cell culture  Adherent Cell Culture: When the primary cells are seeded on or adhered to the culture medium in high density.  Suspension Cell Culture: consists of single cells, small cell groups and larger cell aggregates dispersed in a liquid medium and actively grow.  Immobilization Cell Culture: the cells are either encapsulate or adsorbed or entrapped within a polymeric or open matrix.
  • 3. Immobilization is often confused with mineralisation  Immobilization is closely related to mineralisation as both are due to inorganic organic compounds.  Any media has inorganic as well as organic compounds compounds in its composition.  Now when a cell consume inorganic compounds for its metabolism and other organic compounds needed to be grown then they are said to be “immobilising”, while when a cell excrete inorganic waste compounds then they are said to be “mineralising”.
  • 4. Types of cell immobilisation  We have already heard about enzyme immobilisation in Enzymology, Enzyme can be immobilized through the following techniques.
  • 5.  Similarly Cells can be immobilized in cell culture.  The cells can be immobilised by  covalently attached to the base  Adsorbed or absorbed  Cross-linked  Encapsulate  Assembled to a protein  Entrapped
  • 6. Different types of cell immobilization
  • 8. The two basic cell immobilization techniques include  Immurement Culture/Encapsulation  Entrapment  Immurement Culture/Encapsulation  Cells are encapsulated in a polymeric matrix by adsorption.  Materials used in matrix: gelatin, polylysine, alginate(most common), Agarose.  Medium diffuses freely into the matrix and into the cells, while product moves out into the medium.  For larger molecule production like MAB, Agarose in suspension of paraffin oil is preferable to alginate since alginate does not allow diffusion of products out of alginate beads.  Uses  Encapsulation protects cells from mechanical damage in large fermenters.  Production of hormones, antibodies, immunochemical and enzymes over much longer periods than possible in suspension culture.  Helps in MAB production.
  • 10.  Entrapment culture  Cells are held within an open matrix through which the medium flows freely.  Cells may be entrapped within porous ceramic walls of the entrapping unit.  Use:  Porous micro carriers (170µm-6000µm) made up of gelatin or collagen or glass or cellulose are arranged as fixed bed or fluidized bed reactors or used in stirred bioreactors.  Cells can also be enmeshed in cellulose fibres.  Use:  These fibres are autoclaved and washed and added in stirred bioreactors at a certain conc.(3g/L).  This yields upto 50g MAB/day.
  • 11. Few of immobilized cells: Cell immobilized in Ca-Alginate Immobilisation of prokaryotic cells
  • 12. Cell immobilized in Gelatin Cell immobilized in c) carragenan d) distilled water e) polylysine
  • 13. Uses of immobilized cell culture  Help in making bio-transformants, biosensors.  Secondary metabolite production.  Biological washing powders.  Food Industry.  Bioreactors.  Experimental waste water treatment.
  • 14. Immobilisation of micro algae Immobilized algae used in bioreactor Immobilized micro algae (in polymeric matrix) grown in mixotrophic conditions used in experimental waste water treatment
  • 15.  Immobilized Cell Preparation:  Sodium alginate in growth medium.  Stir until all sodium alginate is completely dissolved. No clump formation.  Suspend wet cells in the alginate solution prepared in the above step. Let air bubbles escape. Drip the yeast alginate mixture. The calcium crosslinking solution is agitated on a magnetic stirrer.  Gel formation can be achieved at room temperature as soon as the sodium alginate drops come in direct contact with the calcium solution.  Relatively small alginate beads are preferred to minimize the mass transfer resistance. A diameter of 0.52mm can be readily achieved with a syringe and a needle. The beads should fully harden in 12hours.  Wash the beads with a fresh calcium crosslinking solution. Ca-Alginate Immobilization of Yeast cells Immobilisation of yeast
  • 16.  Immobilized Cell Reactor Construction:  Construct an immobilized cell reactor with a 500ml Erlenmeyer flask fitted.  Place the hardened beads in the flask and seal it with a rubber stopper with appropriate hose connections.  Make all necessary connections. Start the experiment by filling the flask with the growth media (100g/l glucose) to the working volume of 350ml.  Immobilized Cell Reactor:  Then following sequence of events will be monitored both online and offline.  The responsibilities of online data acquisition and offline sample collection and analysis will be shared by the entire class; the exact assignment will be determined in class. A microcomputer will be programmed to take data on the glucose concentration and the rate of NH4OH addition needed to maintain the pH at 4.0. The offline samples will be analyzed for the optical density (for free cell concentration), glucose concentration, and ethanol concentration.  Furthermore, the liquid and gas flow rate will be measured with a graduated cylinder.  The reactor will be operated in a batch manner until no more glucose is utilized. This can be detected with the leveling off in the glucose concentration. Ca-Alginate Immobilization of Yeast cells
  • 17.  The reactor will be operated in a batch manner until no more glucose is utilized. This can be detected with the leveling off in the glucose concentration.  Furthermore, the liquid and gas flow rate will be measured with a graduated cylinder.  The reactor will be operated in a batch manner until no more glucose is utilized. This can be detected with the leveling off in the glucose concentration.  Substrate feeding will then commence at the rate of 0.4/hr. Record the substrate flow rate. The approach to the first steady state during the startup will be followed.  Various parameters (nitrogen consumption rate, carbon dioxide evolution rate, glucose concentration, ethanol concentration, and free cell level) at the high steady state are recorded.  Decrease the substrate feeding rate to 0.2 /hr., Measure the substrate flow rate and follow the transient approach to the new low steady state.  Repeat above parts for the new steady state.  If time permits, continue shifting the flow rate and obtain more information on steady states. Continue operating the bioreactor until noticeable deterioration in the performance is detected due to gel swelling, cell death, or severe contamination.
  • 18. Ca-Alginate Immobilization of Yeast cells and large scale production of ethanol
  • 21. Use of cell Immobilisation
  • 22. Other benefits of using Immobilized cell culture  Gives higher cell density.  Stability and longevity of cultures.  Can be applicable to both suspension or monolayer culture(adherent).  Many systems protect the cells from shear forces due to medium flow.  Less dependence of cells at higher densities on external supply of growth factors which saves culture cost.