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Aerobic fermentation
Anaerobic, Batch, Continuous
fermentation
By
Harinatha Reddy A
Department of Biotechnology
biohari14@gmail.com
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Name: Harinatha Reddy
Bank name: HDFC
Account number: 50100203661752
IFC code: HDFC0000514
Bangalore
Karnataka.
 The term “Aerobic fermentation” is misnamed because
fermentation is an anaerobic process.
 Simply, this is a process of burning simple sugars to energy in cells;
more scientifically, it can be called aerobic respiration.
 Yeast cell ferment glucose in the presence of oxygen and without
oxygen.

Aerobic Fermentation:
 The key difference between aerobic and anaerobic fermentation
is that aerobic fermentation uses oxygen whereas anaerobic
fermentation does not use oxygen.
 Aerobic” fermentation means that oxygen is present.
 Wine, beer and acetic acid, vinegar need oxygen in the “primary”
or first stage of fermentation.
 When creating vinegar, for example, exposing the surface of the
vinegar to as much oxygen as possible, creates a healthy, flavourful
vinegar with the correct pH.
Anaerobic fermentation:
 Fermentation is a metabolic process that consumes sugar in the
absence of oxygen.
 The products are organic acids, gases, alcohol, lactic acid.
 It occurs in yeast and bacteria, and also in oxygen-starved muscle
cells, as in the case of lactic acid fermentation.
 In 1857, Louis Pasteur concluded that alcoholic fermentation can be
caused by living yeast under anaerobic conditions.
1. Ethanol fermentation
2. Lactic acid fermentation
3. Methane gas production in fermentation
 In methane gas production Acetic acid can undergo reduction by
Methanogenic bacteria and produce methane and carbon dioxide:
CH3COO− + H+ → CH4 + CO2
 The reduction of carbon dioxide into methane in the presence of
hydrogen can be expressed as follows:
CO2 + 4 H2 → CH4 + 2H2O
Batch Fermentation:
Batch Fermentation:
 A batch fermentation is regarded as a
closed system.
 The fermenter is first filled with the raw
material (carbon source).
 Then the microbes are added and
allowed to ferment of the raw material
under optimum pH and Temperature.

 The products remain in the fermenter until the completion of
fermentation.
 After fermentation, the products are extracted and the fermenter is
cleaned and sterilized before next round or batch.
 Thus here the fermentation is done as separate batches.
 Setup is not changed from outside once the fermentation is started.
 Nutrients are added only in the beginning and not added in between
the fermentation process.
 Environmental conditions in the fermenter will not be constant.
 Relatively larger size fermenters are used.
 Suitable for the production of secondary metabolites whose
production is not associated with the growth of the microbes.
Example: antibiotics
 Less investment required.
 Chance of contamination is less.
Under optimal conditions there are four typical phases of
growth was observed in batch fermentation:
 Lag phase
 Log phase or Exponential phase
 Stationary phase
 Death phase
Lag phase:
 No cell division and there is no net increase in mass, But cells
increase in size.
 The cells are synthesizing new components.
 Lag phase also know as Phase of cell enlargement or Preparation
phase/cell adjustment phase.
Log phase:
 Microorganisms are dividing at the maximal rate .
 Their growth rate is constant during the log phase.
 The population is most uniform in terms of chemical and
physical properties during this phase.
 Cells are small in size, and produce primary metabolites.
 In the stationary phase the total number of viable
microorganisms remains constant. This may result from a
balance between cell division and cell death.
 In this phase bacteria growth rate is decreases, Due to the,
deposition of toxic waste products and empty of nutrients.
 The secondary metabolites are produced in this phase.
Stationary Phase:
Death Phase:
 The number of viable cells are decline death phase.
 Environmental changes like nutrient deprivation and the buildup
of toxic wastes lead to the decline in the number of viable cells.
FED BATCH FERMENTATION:
fed batch fermentation:
• Fed-batch fermentation defined as an operational technique in
biotechnological processes where one or more nutrients
(substrates) are fed (supplied) to the bioreactor during cultivation
or fermentation.
• FBF is Semi-closed type………but not semi continuous.
• Periodical substrate addition prolongs log and stationary phases.
 It is difficult to measure substrate concentration in fed
batch fermentation.
 But production CO2, Tmp and Changes in pH may be measured.
 Addition of substrates (Carbon and nitrogen and trace metals)
increases the product yield.
 Fed-batch fermentation has become popular for the production of
alcohol and recombinant proteins.
Product inhibition:
 End products of fermentation such as methanol, ethanol, acetic
acid and lactic acid inhibit the growth of microorganisms.
 By adding such substrates or nutrients to fermenter properly log-
time can be increase the cell growth.
Characteristics Fed-batch culture
Cultivation system Semi-closed type
Addition of fresh nutrition Yes
Volume of culture Increases
Chance of contamination Maximum
Log phase longer
Product yield High
Semi Continuous fermentation:
Semi Continuous fermentation:
 In semi-continuous fermentation, a portion of the culture medium
is removed from the bioreactor and replaced by fresh medium
(identical in nutrients, pH and temperature etc.).
 In the semi-continuous fermentation, the lag phase and other
non-productive phases are very much shortened.
 The product output is much higher compared to batch culture
systems.
 Semi-continuous fermentation technique has been successfully
used in the industrial production of alcohol.
 These include the technical difficulties of handling bioreactors.
 Addition of nutrients that may cause contamination and
changes in physiological and metabolic characters of
microorganisms.
Disadvantages of semi-continuous fermentation.
Continuous culture or Continuous fermentation:
Continuous culture or Continuous fermentation:
 In Continuous fermentation the fresh medium is continuously
added and metabolic end products and microorganisms are
continuously removed at the same rate.
 It is an open system.
 Here the log phase of the microbes is maintained in the fermenter
for prolonged periods of time in by the addition of fresh media
are regular intervals.
 The continuous fermentation process never stops in between and
it continues to run for a long period of time with the addition
of nutrients and harvesting the metabolites at regular intervals.
 Nutrients are added many times (in the beginning and in between
the fermentation process).
 The process is not stopped for the collection of the products, but
it is continuously taken out from the fermenter.
 Smaller size fermenter is required.
 The yield of the product is very high.
 Environmental conditions (pH, Tmp, con.CO2) in the fermenter will be
kept constant.
 Suitable for the primary metabolites whose production is associated
with the growth of the organism.
 Example: organic acids, amino acids.
 Less commonly used for large scale production.
 Chance of contamination is more.
 Two types of Continuous bioreactors:
1. Chemostat bioreactors
2. Turbidostat bioreactors
Chemostat bioreactors:
 A chemostat is a bioreactor to which fresh medium is continuously
added, and metabolic end products and microorganisms are
continuously removed.
 One of the most important features of chemostats is that
microorganisms can be grown in a physiological steady state
under constant environmental conditions and culture parameters.
 Chemostats are frequently used in the industrial manufacturing
of ethanol.
 Chemostats in research are used for investigations in cell
biology, as a source for large volumes of uniform cells or
protein.
 Chemostats can also be used to enrich specific types of
bacterial mutants in culture such as auxotrophs.
Turbidostat bioreactors:
 A turbidostat is a continuous fermentation device, similar to a
chemostat.
 In this case turbidity measurement is used to monitor the addition
of nutrients, removal of end products and biomass concentration.
Applications of continuous fermentation:
 Continuous fermentation process have been used for the
production of antibiotics, organic solvents, single cell protein,
ethanol and waste water treatments.
Advantages of continuous fermentation:
 The size of the bioreactor are smaller than compared to batch
fermentation.
 The yield of the product is constant.
 Continuous fermentation may run continuously for a period of
30 to 40 days.
Disadvantages:
 It is not used widely in industries.
 Maintenance of sterile conditions is difficult.
 Nutrient variations also alter the growth and physiology of the cells
and product yield.
Or Increase
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Aerobic, anaerobic, batch and continuous fermentation

  • 1. Aerobic fermentation Anaerobic, Batch, Continuous fermentation By Harinatha Reddy A Department of Biotechnology biohari14@gmail.com
  • 2. To download power point : Pay: 20 US $ or RS : 400 and send pay receipt to mail (biohari14@gmail.com). I will send power point to your mail id. Name: Harinatha Reddy Bank name: HDFC Account number: 50100203661752 IFC code: HDFC0000514 Bangalore Karnataka.
  • 3.  The term “Aerobic fermentation” is misnamed because fermentation is an anaerobic process.  Simply, this is a process of burning simple sugars to energy in cells; more scientifically, it can be called aerobic respiration.  Yeast cell ferment glucose in the presence of oxygen and without oxygen.  Aerobic Fermentation:
  • 4.  The key difference between aerobic and anaerobic fermentation is that aerobic fermentation uses oxygen whereas anaerobic fermentation does not use oxygen.
  • 5.  Aerobic” fermentation means that oxygen is present.  Wine, beer and acetic acid, vinegar need oxygen in the “primary” or first stage of fermentation.  When creating vinegar, for example, exposing the surface of the vinegar to as much oxygen as possible, creates a healthy, flavourful vinegar with the correct pH.
  • 7.  Fermentation is a metabolic process that consumes sugar in the absence of oxygen.  The products are organic acids, gases, alcohol, lactic acid.  It occurs in yeast and bacteria, and also in oxygen-starved muscle cells, as in the case of lactic acid fermentation.  In 1857, Louis Pasteur concluded that alcoholic fermentation can be caused by living yeast under anaerobic conditions.
  • 8. 1. Ethanol fermentation 2. Lactic acid fermentation 3. Methane gas production in fermentation  In methane gas production Acetic acid can undergo reduction by Methanogenic bacteria and produce methane and carbon dioxide: CH3COO− + H+ → CH4 + CO2  The reduction of carbon dioxide into methane in the presence of hydrogen can be expressed as follows: CO2 + 4 H2 → CH4 + 2H2O
  • 9.
  • 11. Batch Fermentation:  A batch fermentation is regarded as a closed system.  The fermenter is first filled with the raw material (carbon source).  Then the microbes are added and allowed to ferment of the raw material under optimum pH and Temperature. 
  • 12.  The products remain in the fermenter until the completion of fermentation.  After fermentation, the products are extracted and the fermenter is cleaned and sterilized before next round or batch.  Thus here the fermentation is done as separate batches.
  • 13.  Setup is not changed from outside once the fermentation is started.  Nutrients are added only in the beginning and not added in between the fermentation process.  Environmental conditions in the fermenter will not be constant.
  • 14.  Relatively larger size fermenters are used.  Suitable for the production of secondary metabolites whose production is not associated with the growth of the microbes. Example: antibiotics  Less investment required.  Chance of contamination is less.
  • 15. Under optimal conditions there are four typical phases of growth was observed in batch fermentation:  Lag phase  Log phase or Exponential phase  Stationary phase  Death phase
  • 16. Lag phase:  No cell division and there is no net increase in mass, But cells increase in size.  The cells are synthesizing new components.  Lag phase also know as Phase of cell enlargement or Preparation phase/cell adjustment phase.
  • 17. Log phase:  Microorganisms are dividing at the maximal rate .  Their growth rate is constant during the log phase.  The population is most uniform in terms of chemical and physical properties during this phase.  Cells are small in size, and produce primary metabolites.
  • 18.  In the stationary phase the total number of viable microorganisms remains constant. This may result from a balance between cell division and cell death.  In this phase bacteria growth rate is decreases, Due to the, deposition of toxic waste products and empty of nutrients.  The secondary metabolites are produced in this phase. Stationary Phase:
  • 19. Death Phase:  The number of viable cells are decline death phase.  Environmental changes like nutrient deprivation and the buildup of toxic wastes lead to the decline in the number of viable cells.
  • 21. fed batch fermentation: • Fed-batch fermentation defined as an operational technique in biotechnological processes where one or more nutrients (substrates) are fed (supplied) to the bioreactor during cultivation or fermentation. • FBF is Semi-closed type………but not semi continuous. • Periodical substrate addition prolongs log and stationary phases.
  • 22.  It is difficult to measure substrate concentration in fed batch fermentation.  But production CO2, Tmp and Changes in pH may be measured.  Addition of substrates (Carbon and nitrogen and trace metals) increases the product yield.  Fed-batch fermentation has become popular for the production of alcohol and recombinant proteins.
  • 23. Product inhibition:  End products of fermentation such as methanol, ethanol, acetic acid and lactic acid inhibit the growth of microorganisms.  By adding such substrates or nutrients to fermenter properly log- time can be increase the cell growth.
  • 24. Characteristics Fed-batch culture Cultivation system Semi-closed type Addition of fresh nutrition Yes Volume of culture Increases Chance of contamination Maximum Log phase longer Product yield High
  • 26. Semi Continuous fermentation:  In semi-continuous fermentation, a portion of the culture medium is removed from the bioreactor and replaced by fresh medium (identical in nutrients, pH and temperature etc.).
  • 27.  In the semi-continuous fermentation, the lag phase and other non-productive phases are very much shortened.  The product output is much higher compared to batch culture systems.  Semi-continuous fermentation technique has been successfully used in the industrial production of alcohol.
  • 28.  These include the technical difficulties of handling bioreactors.  Addition of nutrients that may cause contamination and changes in physiological and metabolic characters of microorganisms. Disadvantages of semi-continuous fermentation.
  • 29. Continuous culture or Continuous fermentation:
  • 30. Continuous culture or Continuous fermentation:  In Continuous fermentation the fresh medium is continuously added and metabolic end products and microorganisms are continuously removed at the same rate.  It is an open system.  Here the log phase of the microbes is maintained in the fermenter for prolonged periods of time in by the addition of fresh media are regular intervals.
  • 31.  The continuous fermentation process never stops in between and it continues to run for a long period of time with the addition of nutrients and harvesting the metabolites at regular intervals.
  • 32.  Nutrients are added many times (in the beginning and in between the fermentation process).  The process is not stopped for the collection of the products, but it is continuously taken out from the fermenter.
  • 33.  Smaller size fermenter is required.  The yield of the product is very high.  Environmental conditions (pH, Tmp, con.CO2) in the fermenter will be kept constant.  Suitable for the primary metabolites whose production is associated with the growth of the organism.  Example: organic acids, amino acids.
  • 34.  Less commonly used for large scale production.  Chance of contamination is more.
  • 35.  Two types of Continuous bioreactors: 1. Chemostat bioreactors 2. Turbidostat bioreactors
  • 36. Chemostat bioreactors:  A chemostat is a bioreactor to which fresh medium is continuously added, and metabolic end products and microorganisms are continuously removed.  One of the most important features of chemostats is that microorganisms can be grown in a physiological steady state under constant environmental conditions and culture parameters.
  • 37.  Chemostats are frequently used in the industrial manufacturing of ethanol.  Chemostats in research are used for investigations in cell biology, as a source for large volumes of uniform cells or protein.  Chemostats can also be used to enrich specific types of bacterial mutants in culture such as auxotrophs.
  • 38. Turbidostat bioreactors:  A turbidostat is a continuous fermentation device, similar to a chemostat.  In this case turbidity measurement is used to monitor the addition of nutrients, removal of end products and biomass concentration.
  • 39.
  • 40. Applications of continuous fermentation:  Continuous fermentation process have been used for the production of antibiotics, organic solvents, single cell protein, ethanol and waste water treatments.
  • 41. Advantages of continuous fermentation:  The size of the bioreactor are smaller than compared to batch fermentation.  The yield of the product is constant.  Continuous fermentation may run continuously for a period of 30 to 40 days.
  • 42. Disadvantages:  It is not used widely in industries.  Maintenance of sterile conditions is difficult.  Nutrient variations also alter the growth and physiology of the cells and product yield.