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FERMENTATION
CONTENTS
 Introduction
 Types of fermentation
 Production of –
1. Antibiotics : Penicillin & Streptomycin
2. Vitamins: B2 & B12
 References
2
Introduction
 Pasteur definition: “life without air”, anaerobe red
ox reactions in organisms.
 New definition: a form of metabolism in which the
end products could be further oxidized.
For example: a yeast cell obtains 2 molecules of ATP
per molecule of glucose when it ferments it to ethanol
3
4
Some important fermentation products
PRODUCT ORGANISM USES
Ethanol Saccharomyces
cerevisiae
Industrial
solvents
beverages
Glycerol Saccharomyces
cerevisiae
Production of
explosives
Lactic acid Lactobacillus
bulgaricus
Food and
pharmaceutical
Acetone &
Butanol
Clostridium
acetobutylicum
solvents
Difference between FERMENTATION
5
AEROBIC
FERMENTATION
ANAEROBIC
FERMENTATION
Set of chemical reactions
involved in production of
energy by completely
oxidizing food.
Chemical breakdown of
organic substrate into
ethanol or lactic acid by
micro-organism in absence
of oxygen
Occurs in both cytoplasm
and mitochondria
Occurs in cytoplasm
Occurs in higher animals
and plants
Occurs in yeast ,parasites,
and bacteria
6
Uses molecular oxygen as
final electron acceptor in
ETC
Does not use oxygen
Produces 6 water
molecules/glucose
Does not produce water
Glucose completely broken
into CO2 & O2
Glucose incompletely
oxidized either into ethanol
& lactic acid
NAD+ regeneration occurs
in ETC
NAD+ regeneration occurs
during partial oxidation of
Pyruvate
36 ATP is produced Only 2 ATP is produced
Continued……
Penicillin
 Also known as Penicillium Notatum / Chrysogenum.
 It is common in temperate and subtropical region and
can be found on salted food products, but it is mostly
found in indoor enviroments, especially in damp or
water damaged buildings.
 It is source of several β-lactum antibiotics, which
inhibits biosynthesis of bacterial cell wall.
7
Beta lactum ring
8
Production
 P. chyrosegenum is high yielding strain and therefore
most widely used as production strain.
Innoculum preparation- various sequential steps are
necessary like:
1. A starter culture is needed for innoculation.
2. After getting growth on solid media, one or two
growth stages should allowed in shaken flask
cultures to create a suspension, which can be
transfered to seed tanks for further growth.
9
3. After about 24-28 hours, the content of seed tanks is
transfered to primary fermentation tanks.
4. All the bio-parameters like temperature, pH, aeration,
agitation,etc. should be properly maintained.
A. BIO-PARAMETERS-
 pH- near 6.5
 Temperature – 260- 280 C
 Aeration- Continous stream of sterilized air is pumped
into it.
 Agitation- have baffles which allows constant agitation
(200rpm).
10
B. NUTRIENT MEDIA
 Fermentation broth contains all necessary elements
required for the proliferation of micro-organisms.
 Generally it contains-
1. Carbon source
2. Nitrogen source
3. Mineral source
4. Precorsors
5. Anti – foaming agents
11
12
Composition of nutrient media for penicillin
1. Corn steep liquor 3.5%
2. Lactose 3.5%
3. Glucose 1%
4. Calcium carbonate 1%
5. Potassium hydrogen phosphate 0.4%
6. Edible oil 0.25%
Phenyl acetic acid as preservative
C. RECOVERY
 The recovery of Penicillin is carried out in three
successive stages:
1. Removal of mycelium
2. Counter current solvent extraction of penicillin
3. Treatment of crude extract
13
For increasing yield of penicillin
 Adding corn syrup
 Selection of strain
 Mutation and selection
 Sexual reproduction
14
streptomycin
 Streptomycin is an bactericidal antibiotic drug
belonging to class of aminoglycosides.
 Derived from actinobacterium Streptomyces griseus.
 Used against gram negative bacteria especially.
 Chemical composition – It contains 3 sugars derived
from glucose with C, N, O & H elements.
 Chemical formula- C21H39N7O12
15
INNOCULUM
 Streptomyces griseus maintained in soil stocks or
lyophilized in carrrier are innoculated into sporulation
medium which builds up mycelial innoculum.
THE HOCKENHUL MEDIUM
1. Glucose 2.5%
2. Extracted soya meal 4%
3. Distillers dried soluble 0.5%
4. Sodium chloride 0.25%
 pH 7.3-7.5
16
Production
A. NUTRIENT MEDIA
 Medium is a nutritive substance in which cultures
are grown for scientific purposes.
 The culture medium for streptomycin consists of:
1. Carbon source
2. Nitrogen source
3. Animal oils
4. Vegetable oils
5. Mineral oils
17
B. FERMENTATION PROCESS
 Spores of S. griseus are innoculated into medium to
establish a culture with high mycelial biomass for
introduction into innoculum tank, using innoculum to
initiate the fermentation process.
 Yield in production vessel responds to high aeration &
agitation condition
 Other condition are:
Temperature 250-300C
pH range 7-8
Time- 5-7 days
18
 The fermentation process for production of
streptomycin involves three phases :
1. Phase I (last up 24 hours)
2. Phase II (takeplace5-7 days)
3. Phase III (harvested before cell lysis)
C. RECOVERY & PURIFICATION
1. Removal of mycelium
2. Recovery process
3. Purification
19
Cyanocobalamine ( B12)
 Cyanocobalamin is industrially produced stable cobalmin
from which is not found in nature
 It is obtained exclusively by fermentation process.
 Merck began production of vitamin B12 by Pseudomonas
dentrificans in 1952 & have improved the efficiency of
culture more than 30 folds relative to the performance of
original soil isolates by genetic manipulations and
microbial screening.
 Mutagenic treatments have resulted in improved activity.
20
 Mutagenic treatments have resulted in improved
activity.
 Structure of cyanocobalamine :
21
22
Downstream process of vitamin B12
Riboflavin (B2)
 Riboflavin has been produced commercially by chemical
synthesis, by fermentation and by combination of
fermentation and chemical synthesis.
 Fermentation route has been widely used as it produces
the vitamin in single step, resulting in substantial cost
savings.
 Most of the producers like BASF, Roche, ADM/
Aventis, Hubei Gaungii prefer fermentative production.
23
 Although bacteria (Clostridium species) & yeasts
(Candida species) are good producers, two closely
related Ascomycete fungi, Eremothecium ashbyii
& Ashbya gossypii, are considered the best
riboflavin producers.
24
25

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FERMENTATION AND ITS TYPES

  • 2. CONTENTS  Introduction  Types of fermentation  Production of – 1. Antibiotics : Penicillin & Streptomycin 2. Vitamins: B2 & B12  References 2
  • 3. Introduction  Pasteur definition: “life without air”, anaerobe red ox reactions in organisms.  New definition: a form of metabolism in which the end products could be further oxidized. For example: a yeast cell obtains 2 molecules of ATP per molecule of glucose when it ferments it to ethanol 3
  • 4. 4 Some important fermentation products PRODUCT ORGANISM USES Ethanol Saccharomyces cerevisiae Industrial solvents beverages Glycerol Saccharomyces cerevisiae Production of explosives Lactic acid Lactobacillus bulgaricus Food and pharmaceutical Acetone & Butanol Clostridium acetobutylicum solvents
  • 5. Difference between FERMENTATION 5 AEROBIC FERMENTATION ANAEROBIC FERMENTATION Set of chemical reactions involved in production of energy by completely oxidizing food. Chemical breakdown of organic substrate into ethanol or lactic acid by micro-organism in absence of oxygen Occurs in both cytoplasm and mitochondria Occurs in cytoplasm Occurs in higher animals and plants Occurs in yeast ,parasites, and bacteria
  • 6. 6 Uses molecular oxygen as final electron acceptor in ETC Does not use oxygen Produces 6 water molecules/glucose Does not produce water Glucose completely broken into CO2 & O2 Glucose incompletely oxidized either into ethanol & lactic acid NAD+ regeneration occurs in ETC NAD+ regeneration occurs during partial oxidation of Pyruvate 36 ATP is produced Only 2 ATP is produced Continued……
  • 7. Penicillin  Also known as Penicillium Notatum / Chrysogenum.  It is common in temperate and subtropical region and can be found on salted food products, but it is mostly found in indoor enviroments, especially in damp or water damaged buildings.  It is source of several β-lactum antibiotics, which inhibits biosynthesis of bacterial cell wall. 7
  • 9. Production  P. chyrosegenum is high yielding strain and therefore most widely used as production strain. Innoculum preparation- various sequential steps are necessary like: 1. A starter culture is needed for innoculation. 2. After getting growth on solid media, one or two growth stages should allowed in shaken flask cultures to create a suspension, which can be transfered to seed tanks for further growth. 9
  • 10. 3. After about 24-28 hours, the content of seed tanks is transfered to primary fermentation tanks. 4. All the bio-parameters like temperature, pH, aeration, agitation,etc. should be properly maintained. A. BIO-PARAMETERS-  pH- near 6.5  Temperature – 260- 280 C  Aeration- Continous stream of sterilized air is pumped into it.  Agitation- have baffles which allows constant agitation (200rpm). 10
  • 11. B. NUTRIENT MEDIA  Fermentation broth contains all necessary elements required for the proliferation of micro-organisms.  Generally it contains- 1. Carbon source 2. Nitrogen source 3. Mineral source 4. Precorsors 5. Anti – foaming agents 11
  • 12. 12 Composition of nutrient media for penicillin 1. Corn steep liquor 3.5% 2. Lactose 3.5% 3. Glucose 1% 4. Calcium carbonate 1% 5. Potassium hydrogen phosphate 0.4% 6. Edible oil 0.25% Phenyl acetic acid as preservative
  • 13. C. RECOVERY  The recovery of Penicillin is carried out in three successive stages: 1. Removal of mycelium 2. Counter current solvent extraction of penicillin 3. Treatment of crude extract 13
  • 14. For increasing yield of penicillin  Adding corn syrup  Selection of strain  Mutation and selection  Sexual reproduction 14
  • 15. streptomycin  Streptomycin is an bactericidal antibiotic drug belonging to class of aminoglycosides.  Derived from actinobacterium Streptomyces griseus.  Used against gram negative bacteria especially.  Chemical composition – It contains 3 sugars derived from glucose with C, N, O & H elements.  Chemical formula- C21H39N7O12 15
  • 16. INNOCULUM  Streptomyces griseus maintained in soil stocks or lyophilized in carrrier are innoculated into sporulation medium which builds up mycelial innoculum. THE HOCKENHUL MEDIUM 1. Glucose 2.5% 2. Extracted soya meal 4% 3. Distillers dried soluble 0.5% 4. Sodium chloride 0.25%  pH 7.3-7.5 16 Production
  • 17. A. NUTRIENT MEDIA  Medium is a nutritive substance in which cultures are grown for scientific purposes.  The culture medium for streptomycin consists of: 1. Carbon source 2. Nitrogen source 3. Animal oils 4. Vegetable oils 5. Mineral oils 17
  • 18. B. FERMENTATION PROCESS  Spores of S. griseus are innoculated into medium to establish a culture with high mycelial biomass for introduction into innoculum tank, using innoculum to initiate the fermentation process.  Yield in production vessel responds to high aeration & agitation condition  Other condition are: Temperature 250-300C pH range 7-8 Time- 5-7 days 18
  • 19.  The fermentation process for production of streptomycin involves three phases : 1. Phase I (last up 24 hours) 2. Phase II (takeplace5-7 days) 3. Phase III (harvested before cell lysis) C. RECOVERY & PURIFICATION 1. Removal of mycelium 2. Recovery process 3. Purification 19
  • 20. Cyanocobalamine ( B12)  Cyanocobalamin is industrially produced stable cobalmin from which is not found in nature  It is obtained exclusively by fermentation process.  Merck began production of vitamin B12 by Pseudomonas dentrificans in 1952 & have improved the efficiency of culture more than 30 folds relative to the performance of original soil isolates by genetic manipulations and microbial screening.  Mutagenic treatments have resulted in improved activity. 20
  • 21.  Mutagenic treatments have resulted in improved activity.  Structure of cyanocobalamine : 21
  • 23. Riboflavin (B2)  Riboflavin has been produced commercially by chemical synthesis, by fermentation and by combination of fermentation and chemical synthesis.  Fermentation route has been widely used as it produces the vitamin in single step, resulting in substantial cost savings.  Most of the producers like BASF, Roche, ADM/ Aventis, Hubei Gaungii prefer fermentative production. 23
  • 24.  Although bacteria (Clostridium species) & yeasts (Candida species) are good producers, two closely related Ascomycete fungi, Eremothecium ashbyii & Ashbya gossypii, are considered the best riboflavin producers. 24
  • 25. 25