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Fermentation
Fermentation
• Submerged fermentation (Smf)/ Liquid
fermentation (Lf)
• Solid state fermentation (SSF)
Submerged fermentation
• Media concentration is very much lower as
compared to water content.
• Required processed ingredients are
expensive
• Higher water activity becomes the major
cause of contamination in SLF
• Large-scale bioreactors are required
because media is very much diluted.
• High air pressure consumes more power
and there is poor transfer of gas in SLF
• Vigorous mixing makes diffusion easy.
• Online sensors are available and sampling
is easy for biomass measurement.
• Water makes downstream process difficult
and very expensive.
• High quantity of liquid waste is produced,
causes difficulties in dumping
Solid state fermentation (SSF)
• Organisms requiring less water for growth
are preferred such as filamentous fungi.
• Inert support (natural or artificial),
containing all components for growth in
the form of solution
• Less chances of contamination because of
low availability of water
• Small size bioreactors can be used.
• Less consumption of energy for aeration
and gas transfer.
• Limiting factor for growth is diffusion of
nutrients
• Lots of difficulties in measuring the
quantity of biomass present and other
online processes
• Downstream processing is easy, cheaper
and less time consuming.
• Liquid waste is not produced
Fermentation Process
• Batch
• Fed batch
• Continuous
Batch Fermentation
• Fermentation Kinetics
• μ (h-1): Specific growth rate dx/dt
• Yx/s: g of cell biomass formed/g of substrate
consumed
• Yp/x: Product produced/g of cells formed
• Yp/s: Product produced/g of substrate consumed
Continuous Fermentation
• Homogeneously mixed Bioreactor
• Chemostat or turbidostat
• Chemostat- growth controlled by adjusting conc.
Of substrate
• Turbidostat- cell growth kept constant, by using
turbidity to monitor biomass conc.
• Plug flow Reactor- solution flows through tubular
reactor
Fermentation classification
• Type 1- product directly derived from primary
metabolism. E.g. SCP, Ethanol
• Type II- product also derived from substrate,
but production takes place in secondary
pathway e.g. citric acid
• Type III- primary metabolism function first,
accompanied by substrate consumption, growth,
product is formed by intermediary metabolism
e.g. Antibiotics
Flask Fermentation
• Lab Scale
Fermenter
• Height and width
2:1-6:1
• 4-12 baffles
1:10-1:12
• 4-8 radial blades
• SS jacket 316, 317
Impeller
Sterilization
• In situ
• Ex situ
Air Lift fermenter

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1589353475-fermentation.ppt12345789934578

  • 2. Fermentation • Submerged fermentation (Smf)/ Liquid fermentation (Lf) • Solid state fermentation (SSF)
  • 3. Submerged fermentation • Media concentration is very much lower as compared to water content. • Required processed ingredients are expensive • Higher water activity becomes the major cause of contamination in SLF • Large-scale bioreactors are required because media is very much diluted.
  • 4. • High air pressure consumes more power and there is poor transfer of gas in SLF • Vigorous mixing makes diffusion easy. • Online sensors are available and sampling is easy for biomass measurement. • Water makes downstream process difficult and very expensive. • High quantity of liquid waste is produced, causes difficulties in dumping
  • 5. Solid state fermentation (SSF) • Organisms requiring less water for growth are preferred such as filamentous fungi. • Inert support (natural or artificial), containing all components for growth in the form of solution • Less chances of contamination because of low availability of water • Small size bioreactors can be used.
  • 6. • Less consumption of energy for aeration and gas transfer. • Limiting factor for growth is diffusion of nutrients • Lots of difficulties in measuring the quantity of biomass present and other online processes • Downstream processing is easy, cheaper and less time consuming. • Liquid waste is not produced
  • 7. Fermentation Process • Batch • Fed batch • Continuous
  • 8. Batch Fermentation • Fermentation Kinetics • μ (h-1): Specific growth rate dx/dt • Yx/s: g of cell biomass formed/g of substrate consumed • Yp/x: Product produced/g of cells formed • Yp/s: Product produced/g of substrate consumed
  • 9. Continuous Fermentation • Homogeneously mixed Bioreactor • Chemostat or turbidostat • Chemostat- growth controlled by adjusting conc. Of substrate • Turbidostat- cell growth kept constant, by using turbidity to monitor biomass conc. • Plug flow Reactor- solution flows through tubular reactor
  • 10.
  • 11. Fermentation classification • Type 1- product directly derived from primary metabolism. E.g. SCP, Ethanol • Type II- product also derived from substrate, but production takes place in secondary pathway e.g. citric acid • Type III- primary metabolism function first, accompanied by substrate consumption, growth, product is formed by intermediary metabolism e.g. Antibiotics
  • 12.
  • 14. Fermenter • Height and width 2:1-6:1 • 4-12 baffles 1:10-1:12 • 4-8 radial blades • SS jacket 316, 317
  • 17.