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Techniques used in
Presented by
Bilqees Fatima Ph.D.
Presented to
Dr. Muhammad Mohsin Javed
INSTITUTE OF INDUSTRIAL BIOTECHNOLOGY
G.C. UNIVERSITY Lahore
PAKISTAN
Media
formulation
Synthesis
Product
recovery
Final
polishing
Organism
Waste
Market
Raw
material
Is the use of biological materials (organisms, cells,
organelles, enzymes) to carry out a process for
commercial, medical or scientific reasons.
A growth medium or culture medium is a liquid or gel
designed to support the growth of organisms or cells
A bioprocess medium design principles take care of the
following in general
Source(s) of energy
Source(s) of carbon
Source(s) of nitrogen
Source(s) of minerals
Source(s) of growth factors
Source(s) of specific nutrient needs
Source(s) of oxygen environment
Raw material is used for the formulation of growth medium
Weigh out Heat to dissolve
Raw
Material
Sugarcane Bagasse
Treated Sugar-cane
Bagasse
Chemical sources
Mix in buffer
Biological sources
Methods of Sterilization
Chemicals (phenols, alcohols, aldehyde, helogens,
detergents, ethylene oxide, heavy metals)
Radiations (UV, γ-rays)
Filtration and
Heat
Is the process by which all living cells, viable spores, viruses
and viroids are either destroyed or removed from an object
or habitat.
Required high temperature and longer
exposure time
Hot air oven (160 C for 60 min)
Infra red conveyer (180 C for 7 min)
(Metal instruments and glass syringes)
1. DRY HEAT
Incineration
Hot air ovens
2. MOIST HEAT
Autoclave
Sealed chamber that furnished
pressurized steam for sterilization
Sterilizes
Instruments
Syringes
Needles
Other materials
Steam
pressure
(lb/inch2)
Temperature
(°C)
Holding time
(min)
15
20
30
121
126
134
15
12
3
Autoclave
The preparation of a population of organisms from a
dormant stock culture to an active state of growth that is
suitable for inoculation in the final production stage is
called inoculum development
Organism,
cells
The process of inoculum development
Sample Analysis
•pH
•DO
•Sugar
•Ammonia
•Phosphate
•Sulphate
•Products
•Precursors
•Contamination
Pressure probe
Level probe
pH probe
Temp. probe
DO probe
Antifoam
Acid/Base
Cooling
Air/agitation
Sugar/Oil
feed
Foam separation
Filtration
Centrifugation
Cell disruption
Fractional
Precipitation
Dialysis
Ultrafiltration
Electrophoresis
Distillation
Reverse osmosis
Diafiltration
Precipitation
Gel Filtration
Aqueous two phase
extraction
Sterile filtration
Crystallization
Lyophilization
Drying Packaging
Product recovery encompasses all processes following the
fermentation by which the desired product is Isolated,
Purified and Formulated for different end uses.
It may be possible to make some
materials surface active by the
application of surfactants such as
long chain fatty acids
amines and
quaternary ammonium
compounds
Depends upon differences in
surface activity materials
Collectors
Colligends
to obtain some products or to remove some impurities
directly from the broth
use the technique after a crude cell lysate has been
obtained.
Typical agents used in precipitation render the
compound of interest insoluble, are include:
• Acids and bases
• Salts
• Organic solvents
• Non-ionic polymer
• Polyelectrolytes
• Affinity precipitatants
Microorganisms and other similar
sized particles can be removed from
a broth
Vg = d2g (P-L) /18 
Vc = d2r (P-L) /18 
1. Basket bowl centrifuge
2. Tubular bowl centrifuge
3. Solid bowl centrifuge
4. Disc bowl centrifuge
5. Multichamber centrifuge
Types of centrifuges in their manner of liquid solid discharge
Stoke’s law
to release cellular contents a number of
methods for cell disintegration have been
developed
i. Detergents
ii. Osmotic shock
iii. Alkali treatment
iv. Enzyme treatment
Chemical Methods
Physical Methods
This method is used
while separating two or
more immiscible liquids
with different densities.
Mixture is taken in a
separating funnel.
Allowed the mixture to
stand for some time.
This separates the
liquids into layers.
It involves the treatment of organic solvent with aqueous solvent
containing desired solute
The solute which is preferential soluble in aqueous solvent, more
solute would be present in aqueous solvent at equilibrium
However, the use of organic solvents has limited application in
the bioprocessing of sensitive bioproduct.
 Phase separation
occurs when
hydrophilic polymers
are added to an
aqueous solution, and
concentration exceed a
certain value, two
immiscible aqueous
phases are formed.
System Example
Non-ionic polymer
/non-ionic
polymer /water
Polyethylene glycol
/ Dextran
Polyelectrolyte
/non-ionic
polymer /water
Sodium
carboxymethyle
cellulose
/polyethylene glycol
Polyelectrolyte
/Polyelectrolyte/
water
Sodium Dextran
sulphate
/sodium carboxymethyl
cellulose
Polymer
/low molecular
weight
component/wate
r
Dextran
/propyl alcohol
A large variety of natural and
synthetic hydrophilic
polymers are used today
Dialysis Ultrafiltration Nanofiltration
•Separation affected by the use of thin, selective, semi-
permeable barriers
• Ceramic and metal filters also perform similar task
•Dialysis membrane is usually
made of cellulose acetate
•Pore size = 1-20 nm in
diameter
low-pressure (10-100psi)
cross-flow membrane process
for separating colloidal and
suspended particles in the
range of 0.05-10 microns.
Reverse
Osmosis
Microfiltration
Ultrafiltration is a
selective fractionation
process utilizing
pressures up to 145
psi (10 bar).
It concentrates
suspended solids and
solutes of molecular
weight greater than
1,000.
UF is widely used in
– fractionation of milk and
whey,
– protein fractionation.
 Reverse osmosis is a high-
pressure, energy-efficient technique
for dewatering process streams,
concentrating low-molecular-weight
substances in solution, or purifying
wastewater.
Pressure requirement
•2–17 bar (30–250 psi) for
fresh and brackish water
•40–70 bar (600–1000 psi)
for seawater
Nanofiltration is a special
process selected when RO
and UF are not the ideal
choice for separation.
NF can perform separation
applications that are not
otherwise economically
feasible, such as
demineralization, color
removal, and desalination.
Nanofiltration removes most
of the organic molecules,
nearly all viruses, most of
the natural organic matter,
polyvalent ions and a range
of salts.
Membrane processes are not fundamentally
different, except in terms of size of molecules they
retains
Mixer
Buffer Select
Column
UV Detector
Injector Valve
Conductivity Meter
Peristaltic
Pump
Creates a gentle
squeezing action to
move fluid through
flexible tubing
system of
chromatographic
apparatus.
Ion Exchange Chromatography relies on charge-charge interactions
between the protein of interest and charges on a resin (bead).
• Once the protein of interest is
bound, the column is washed
with equilibration buffer to
remove unattached entities.
• Then the bound protein of
interest is eluted off using an
elution buffer of increasing ionic
strength or of a different pH.
• Either weakens the
attachment of the protein of
interest to the bead and the
protein of interest is bumped off
and eluted from the resin.
Affinity chromatography
separates the protein of
interest on the basis of a
reversible interaction
between it and its antibody
coupled to a
chromatography bead (here
labeled antigen) .
To elute the protein of
interest from the affinity
beads, the interaction can
be reversed by changing
the pH or ionic strength.
Adsorption
takes place in
high salt and
elution in low
salt
concentrations.
Crystallization is a process where solid particles of specified size and
shape are formed from a homogeneous phase.
Crystallization process consists of two steps
– Nucleation
– Crystal growth
Super saturated state consists of three zones
– Metastable zone
– Intermediate zone
– Labile zone
Crystallization may be initiated by
– Homogenous nucleation
– Hetrogenous nucleation
Drying
Drum dryer Spray dryer
• Drying removes the solvent, mainly water, from the
desired product and in most cases stabilizes the product
making it amenable for storing, packaging or formulation.
• Drying takes place by movement of water vapour from the
saturated surface through to the stagnant air film in to the
main stream of drying air.
• used for more temperature
stable products
• solid is in contact with
the heating surface for 6-
15 seconds
 heat transfer
coefficients are generally
between 1-2 kWm-2 K-1
•Most widely used for drying
of biological materials when
the starting material is in the
form of a liquid or paste.
•The droplets then fall into a
spiral stream of hot gas at
150-250°C.
•The high surface area:
volume ratio of the droplets
results in a rapid rate of
evaporation and complete
drying in a few seconds.
• Pressure gradient 0.1-2.0 torr
• A heating system to provide
latent heat of sublimation
The latent heat of sublimation of
ice is 2838 kJ/kg
In a typical phase diagram, the
boundary between gas and liquid
runs from the triple point to the
critical point. Freeze-drying (blue
arrow) brings the system around
the triple point, avoiding the direct
liquid-gas transition seen in
ordinary drying (green arrow).
•Foodstuffs, pharmaceuticals and
biological materials which are heat
sensitive even to low or moderate
temperatures are freeze-dried.
•The method involves freezing of
the material by exposure to cold air
followed by sublimation of ice in
vacuum from the frozen state to
produce a dried product.
Product viewable single
shelf freeze-dryer. Production freeze-drier.
Development freeze-dryer
Benchtop manifold
freeze-drier
Unloading trays of freeze-dried material from a
small cabinet-type freeze-drier
Freeze-dried coffee, a form of instant coffee

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Techniques used in bioprocessing

  • 1. Techniques used in Presented by Bilqees Fatima Ph.D. Presented to Dr. Muhammad Mohsin Javed INSTITUTE OF INDUSTRIAL BIOTECHNOLOGY G.C. UNIVERSITY Lahore PAKISTAN
  • 2. Media formulation Synthesis Product recovery Final polishing Organism Waste Market Raw material Is the use of biological materials (organisms, cells, organelles, enzymes) to carry out a process for commercial, medical or scientific reasons.
  • 3. A growth medium or culture medium is a liquid or gel designed to support the growth of organisms or cells A bioprocess medium design principles take care of the following in general Source(s) of energy Source(s) of carbon Source(s) of nitrogen Source(s) of minerals Source(s) of growth factors Source(s) of specific nutrient needs Source(s) of oxygen environment Raw material is used for the formulation of growth medium
  • 4. Weigh out Heat to dissolve Raw Material Sugarcane Bagasse Treated Sugar-cane Bagasse Chemical sources Mix in buffer Biological sources
  • 5. Methods of Sterilization Chemicals (phenols, alcohols, aldehyde, helogens, detergents, ethylene oxide, heavy metals) Radiations (UV, γ-rays) Filtration and Heat Is the process by which all living cells, viable spores, viruses and viroids are either destroyed or removed from an object or habitat.
  • 6. Required high temperature and longer exposure time Hot air oven (160 C for 60 min) Infra red conveyer (180 C for 7 min) (Metal instruments and glass syringes) 1. DRY HEAT Incineration Hot air ovens
  • 7. 2. MOIST HEAT Autoclave Sealed chamber that furnished pressurized steam for sterilization Sterilizes Instruments Syringes Needles Other materials Steam pressure (lb/inch2) Temperature (°C) Holding time (min) 15 20 30 121 126 134 15 12 3 Autoclave
  • 8. The preparation of a population of organisms from a dormant stock culture to an active state of growth that is suitable for inoculation in the final production stage is called inoculum development Organism, cells The process of inoculum development
  • 9. Sample Analysis •pH •DO •Sugar •Ammonia •Phosphate •Sulphate •Products •Precursors •Contamination Pressure probe Level probe pH probe Temp. probe DO probe Antifoam Acid/Base Cooling Air/agitation Sugar/Oil feed
  • 10. Foam separation Filtration Centrifugation Cell disruption Fractional Precipitation Dialysis Ultrafiltration Electrophoresis Distillation Reverse osmosis Diafiltration Precipitation Gel Filtration Aqueous two phase extraction Sterile filtration Crystallization Lyophilization Drying Packaging Product recovery encompasses all processes following the fermentation by which the desired product is Isolated, Purified and Formulated for different end uses.
  • 11. It may be possible to make some materials surface active by the application of surfactants such as long chain fatty acids amines and quaternary ammonium compounds Depends upon differences in surface activity materials Collectors Colligends
  • 12. to obtain some products or to remove some impurities directly from the broth use the technique after a crude cell lysate has been obtained. Typical agents used in precipitation render the compound of interest insoluble, are include: • Acids and bases • Salts • Organic solvents • Non-ionic polymer • Polyelectrolytes • Affinity precipitatants
  • 13. Microorganisms and other similar sized particles can be removed from a broth Vg = d2g (P-L) /18  Vc = d2r (P-L) /18  1. Basket bowl centrifuge 2. Tubular bowl centrifuge 3. Solid bowl centrifuge 4. Disc bowl centrifuge 5. Multichamber centrifuge Types of centrifuges in their manner of liquid solid discharge Stoke’s law
  • 14. to release cellular contents a number of methods for cell disintegration have been developed i. Detergents ii. Osmotic shock iii. Alkali treatment iv. Enzyme treatment Chemical Methods Physical Methods
  • 15. This method is used while separating two or more immiscible liquids with different densities. Mixture is taken in a separating funnel. Allowed the mixture to stand for some time. This separates the liquids into layers.
  • 16. It involves the treatment of organic solvent with aqueous solvent containing desired solute The solute which is preferential soluble in aqueous solvent, more solute would be present in aqueous solvent at equilibrium However, the use of organic solvents has limited application in the bioprocessing of sensitive bioproduct.
  • 17.  Phase separation occurs when hydrophilic polymers are added to an aqueous solution, and concentration exceed a certain value, two immiscible aqueous phases are formed. System Example Non-ionic polymer /non-ionic polymer /water Polyethylene glycol / Dextran Polyelectrolyte /non-ionic polymer /water Sodium carboxymethyle cellulose /polyethylene glycol Polyelectrolyte /Polyelectrolyte/ water Sodium Dextran sulphate /sodium carboxymethyl cellulose Polymer /low molecular weight component/wate r Dextran /propyl alcohol A large variety of natural and synthetic hydrophilic polymers are used today
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  • 19. Dialysis Ultrafiltration Nanofiltration •Separation affected by the use of thin, selective, semi- permeable barriers • Ceramic and metal filters also perform similar task •Dialysis membrane is usually made of cellulose acetate •Pore size = 1-20 nm in diameter low-pressure (10-100psi) cross-flow membrane process for separating colloidal and suspended particles in the range of 0.05-10 microns. Reverse Osmosis Microfiltration
  • 20. Ultrafiltration is a selective fractionation process utilizing pressures up to 145 psi (10 bar). It concentrates suspended solids and solutes of molecular weight greater than 1,000. UF is widely used in – fractionation of milk and whey, – protein fractionation.
  • 21.  Reverse osmosis is a high- pressure, energy-efficient technique for dewatering process streams, concentrating low-molecular-weight substances in solution, or purifying wastewater. Pressure requirement •2–17 bar (30–250 psi) for fresh and brackish water •40–70 bar (600–1000 psi) for seawater
  • 22. Nanofiltration is a special process selected when RO and UF are not the ideal choice for separation. NF can perform separation applications that are not otherwise economically feasible, such as demineralization, color removal, and desalination. Nanofiltration removes most of the organic molecules, nearly all viruses, most of the natural organic matter, polyvalent ions and a range of salts.
  • 23. Membrane processes are not fundamentally different, except in terms of size of molecules they retains
  • 24. Mixer Buffer Select Column UV Detector Injector Valve Conductivity Meter Peristaltic Pump
  • 25. Creates a gentle squeezing action to move fluid through flexible tubing system of chromatographic apparatus.
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  • 27. Ion Exchange Chromatography relies on charge-charge interactions between the protein of interest and charges on a resin (bead). • Once the protein of interest is bound, the column is washed with equilibration buffer to remove unattached entities. • Then the bound protein of interest is eluted off using an elution buffer of increasing ionic strength or of a different pH. • Either weakens the attachment of the protein of interest to the bead and the protein of interest is bumped off and eluted from the resin.
  • 28. Affinity chromatography separates the protein of interest on the basis of a reversible interaction between it and its antibody coupled to a chromatography bead (here labeled antigen) . To elute the protein of interest from the affinity beads, the interaction can be reversed by changing the pH or ionic strength.
  • 29. Adsorption takes place in high salt and elution in low salt concentrations.
  • 30. Crystallization is a process where solid particles of specified size and shape are formed from a homogeneous phase. Crystallization process consists of two steps – Nucleation – Crystal growth Super saturated state consists of three zones – Metastable zone – Intermediate zone – Labile zone Crystallization may be initiated by – Homogenous nucleation – Hetrogenous nucleation
  • 31. Drying Drum dryer Spray dryer • Drying removes the solvent, mainly water, from the desired product and in most cases stabilizes the product making it amenable for storing, packaging or formulation. • Drying takes place by movement of water vapour from the saturated surface through to the stagnant air film in to the main stream of drying air.
  • 32. • used for more temperature stable products • solid is in contact with the heating surface for 6- 15 seconds  heat transfer coefficients are generally between 1-2 kWm-2 K-1
  • 33. •Most widely used for drying of biological materials when the starting material is in the form of a liquid or paste. •The droplets then fall into a spiral stream of hot gas at 150-250°C. •The high surface area: volume ratio of the droplets results in a rapid rate of evaporation and complete drying in a few seconds.
  • 34. • Pressure gradient 0.1-2.0 torr • A heating system to provide latent heat of sublimation The latent heat of sublimation of ice is 2838 kJ/kg In a typical phase diagram, the boundary between gas and liquid runs from the triple point to the critical point. Freeze-drying (blue arrow) brings the system around the triple point, avoiding the direct liquid-gas transition seen in ordinary drying (green arrow). •Foodstuffs, pharmaceuticals and biological materials which are heat sensitive even to low or moderate temperatures are freeze-dried. •The method involves freezing of the material by exposure to cold air followed by sublimation of ice in vacuum from the frozen state to produce a dried product.
  • 35. Product viewable single shelf freeze-dryer. Production freeze-drier. Development freeze-dryer Benchtop manifold freeze-drier Unloading trays of freeze-dried material from a small cabinet-type freeze-drier
  • 36. Freeze-dried coffee, a form of instant coffee