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PULLULAN MICROORGANISM
APPLICATIONS
RAW MATERIALS
BIOREACTOR
DESIGN
DOWNSTREAM
PROCESS
Solubility &
Impermeable to O2
Exopolysaccharide
Homopolymer
Produced by fungi
in late stationary
phases
Viscous &
extreme stability
over a range of pH
INTRODUCTION
STRUCTURE
➢ Repeating Unit = Maltotriose
➢Maltotriose – Glucose linked by
α-1,4 linkage
➢ 0.6 % of maltotetrose
➢ 1.5 x 104 to 1.0 x 107 Da
α-1,4 linkage
MICROORGANISMS
Aureobasidium pullulans
Pullularia pullulans
Black yeast
FERMENTATION MEDIUM &
PROCESS PARAMETES
Carbon source
âś“ Saccharify a wide
variety of plantfibres
âś“ Acidified sucrose
syrup
âś“ 10-15% Optimum
✓ What if its ↓ or ↑ ?
Phosphate content
âś“ Optimum- 0.2%
✓ ↑ Phosphate
conc ↓ Mol. Wt.
Nitrogen source
âś“ Ammonium salts
âś“NH4+ ions playmajor
role
âś“Nitrogen limiting
conditions
✓ Regulates α amylase
1
2
3
4
pH
5.5to 7.5
Below 5 suppresses pullulan
production
Temperature
250 to 300C
Oxygen profile
2.0 vvm
Cultivation time
100 hours
BIOREACTOR DESIGN
BIOFILM REACTOR
➢ Immobilized on Plastic Composite Support
➢ PCS – Extrusion product of polypropylene,
agricultural mixture and microbial nutrients
➢ Fitted on the shaft
➢Operated in continuous mode
RECIPROCATINGPLATE REACTOR
➢Plates aid in better mixing
➢Operated in Batch mode
D
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P
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C
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T
A
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I
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D
I
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I
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N
C
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T
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U
G
A
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I
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N
F
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L
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R
A
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I
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C
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C
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N
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R
A
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I
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D
R
Y
I
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G
M
I
L
L
I
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G
DOWNSTREAM PROCESSING
DIETARY
SUBSTITUENT
BINDER
EDIBLE FILMS
GLAZING AGENT
THICKNER
DRUG DELIVERY
MOL WT.
STANDARD
APPLICATIONS

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