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Enzymatic Catalysis in Synthesis
of fine Chemicals
Research supervisor Research student
Prof. G.D.Yadav Shrinivas A. Shete
_
• Synthesis of novel support
• Characterization of support
• Immobilization of lipase
• Characterization of biocatalyst
• Synthesis of hexyl acetate
Outline of project
2
Classification of catalysis_
Catalysis
Bio- Chemo-
Organo - Inorganic
Organo
metalic
Enzyme
3
Biocatalysis can be either homogeneous or
heterogeneous
Homogeneous
Heterogeneous
Chemo-
catalysis
Bio-
catalysis
Organo
Metalic
Organic
compounds
Acids and
bases
Free
enzyme
Inorganic
solids
Organic
resins
Immobilized
enzymes
Whole
cells
_
4
 Stability in organic solvents
 Mild reaction conditions
 Do not require cofactors
 Eco friendly catalyst
 Higher reaction rates
 Possess broad substrate specificity
 Exhibit high enantioselectivity
Lipase (3.1.1.3)_
Lipase can be employed in the production of pharmaceuticals, cosmetics, leather,
detergents, foods, perfumery and other organic synthetic materials.
5
They are
soluble
catalysts
Usually
very
unstable
They may
be strongly
inhibited by
substrates
and
products
work well on
natural
substrates
and under
physiologica
l conditions
High cost
Limitations of enzyme in addition to
their excellent catalytic properties
_
6
Engineering of enzymes from biological to
chemical industry
• Screening of enzymes with suitable properties
• Improvement of enzyme properties via techniques of
molecular biology
• improvement of enzyme properties via reaction and
reactor engineering
_
•Improvement of enzyme properties via
immobilization
7
Development of Biocatalyst
• Factors to be considered in design of a biocatalyst.
A
Reuse of Enzyme
B
Immobilization method
C
Enzyme stability
_
Cost effectiveness & Simplicity
D
Development of Biocatalyst_
8
Support for enzyme immobilization
Support
Natural Synthetic Inorganic
1. cellulose
2. dextran
3. agar
4. chitin
1. polyacrylate
2. polymethacrylates
3. polyacrylamide
1. silica
2. bentonite
3. glass
_
9
Silica support
Porous silica
Microporous
<2nm
Mesoporous
2-50nm
Macroporous
>50nm
MCM-41 HMS SBA-15 MCF
_
10
Mesocellular foam [MCF]_
B
High pore volume, up to 2 ml/g
Large surface area, up to 1,000 m2/g
C
A
3D pore system
A
Connected by uniform windows (9-22 nm)
D
Large spherical cells (24-42 nm)
11
P123-4g + H2O-65ml + HCl-10ml
Stir at 40 ºC for 2 hours
Static at 40 ºC for 20 hours
Age at 100 ºC for 24 hours
Filter, dry & Calcination at 550 ºC
for 6 hours
TMB
TEOS
NH4F
Synthesis of MCF_
Characterization of MCF_
1. FT-IR
2. ASAP
3. SEM
13
4000.0 3000 2000 1500 1000 400.0
-1.5
5
10
15
20
25
30
35
40
45
50
55
61.9
cm-1
%T
3465.76
1652.48
1086.56
972.84
804.97
462.88
FT-IR of MCF_
14
ASAP of MCF_
15
Silica
Surface Area (m2/g) Pore volume (cm3/g) Pore
size
(nm)Single
Point
BET
BJH
Adsorption
BJH
Desorption
Single
point
BJH
Adsorption
BJH
Desorption
MCF 431.74 447.79 471.62 739.11 1.92 1.90 1.93 17.19
ASAP results_
16
SEM of MCF_
17
Advantages of Immobilization_
Immobilization
18
Methods of enzyme immobilization
Methods
Adsorption Entrapment
Micro-
encapsulation
Entrapment Cross linking
Covalent
binding
_
19
Total protein estimation
y= 0.026x
R² =0.998
0
0.05
0.1
0.15
0.2
0.25
0.3
0 2 4 6 8 10 12
Absorbance
Microgram of Protein/100ul
BradfordCalibrationCurve(Microassay) Bradford Calibration Curve (Macroassay)
y = 0.007x
R2
= 0.9912
0
0.1
0.2
0.3
0.4
0.5
0.6
0.7
0.8
0 20 40 60 80 100 120
micro gram protein/100ul
absorbance
_
20
Olive
oil
Tributy
rin
P-nitro
phenol
Lipase assay_
Various assay methods are used to determine the enzyme activity.
Tributyrin method_
188µl tributyrin
+ 1062µl of 0.1M
phosphate
buffer + 250µl
enzyme
Mix thoroughly on
cyclomixer for 1 min
Kept on shaker for 14 min Released acid titrated with
0.05N NaOH
22
0.2 g of Calcined MCF +
20 ml ethanol
Appropriate amount of
APTES
Mixture reflux for 850C
for 8 h.
Wash with DI water &
ethanol
Filter white solid & Dry
at 600C for 24 h
Covalent binding
Functionalization with APTES
_
23
Procedure_
300mg FMCF +
10ml sod. phosphate
buffer. equilibration
for 1 hour
10ml of 0.1%
gluteraldehyde soln
Kept in shaker
for 1 hr at room
temp
Add. of diluted enzyme
Washed three times
with buffer
Protein content &
enzyme activity was
checked
Kept in shaker for 6
hr at room temp
24
Covalent binding results
Immobilization
Method
Dilution
%
Immobilization
Activity
u/g
Covalent
binding
10 27 100
100 31 40
1000 80 15
_
25
300mg MCF + 10ml sod.
phosphate buffer.
equilibration for 1 hour
10ml enzyme solution
Gluteraldehyde crosslinking method - I_
300mg MCF 10ml phosphate buffer
Kept it for 1hr in
incubator shaker
0.1% of Gluteraldehyde
solution
Stirred at 4ºC overnight
Centrifugation &
washing with
buffer 26
Immobilization
Method
Dilution
%
Immobilization
Activity
u/g
Gluteraldehyde
( Method I )
10 78 222
100 79 82
1000 100 24
Gluteraldehyde crosslinking method – I results_
27
Gluteraldehyde crosslinking method – II_
300mg MCF 10ml sod. Phosphate
buffer
300mg MCF + 10ml
sod. phosphate buffer.
equilibration for 1
hour
10ml enzyme solution
Vortexed for 30 sec
& then sonicated for
10sec
Kept on shaker
for 30min
0.1%
gluteraldehyde sol.
Kept on shaker
for 30min
Centrifugation &
washing with
buffer
28
Immobilization
Method
Dilution
%
Immobilization
Activity
u/g
Gluteraldehyd
e
( Method I )
10 97 333
100 99 198
1000 100 75
Gluteraldehyde crosslinking
method – II results
_
29
Comparison of results of immobilization methods
0
50
100
150
200
250
300
350
Gluteraldehyde I Gluteraldehyde II Covalant bonding
Immobilization methods
Enzymeactivityu/g
10 100 1000
_
30
31
Reaction scheme_
CH3 OH +
CH2
O
O CH3
CH3 O O
CH3
+ CH2
OH
CH3 O
vinyl alcohol
vinyl acetate
hexanol
hexyl acetate
acetaldehyde
Lipase
Hexylacetate is a significant green note flavor and widely used in food industry.32
……..Experi
mental
Gas
Chromatography
Contd...
water bath
hexanol + vinyl acetate +
biocatalyst in organic
solvent
t0…………….t1………….tn
glass reactor
pitched blade glass
stirrer
Analysis
Effect of acyl donors
0
10
20
30
40
50
60
70
80
90
100
0 30 60 90 120 150
%conversionofhexanol
Time (min)
vinyl acetate acetic anhydride acetic acid triacetin
_
Reaction parameter
Speed of
agitation
300RPM
Temp. 50 ºC
Solvent Toluene
Enzyme
loaded MCF
20mg
hexanol:acyl
donar
1:2
35
Effect of speed of agitation
0
10
20
30
40
50
60
70
80
90
100
0 30 60 90 120 150
%Conversionofhexanol
Time ( min )
200 RPM 300 RPM 400 RPM 500 RPM
_
Temp. 50 ºC
Solvent Toluene
Enzyme loaded
MCF
20mg
hexanol:vinyl
acetate
1:2
Reaction parameter
36
Effect of solvents
0
10
20
30
40
50
60
70
80
90
100
0 30 60 90 120 150
%ConversionofHexanol
Time (min)
Toluene Benzene 1,4 Dioxane Acetonitrile
_
Reaction parameter
Speed of
agitation
300RPM
Temp. 50 ºC
Enzyme loaded
MCF
20mg
hexanol:vinyl
acetate
1:2
37
Effect of catalyst loading
0
10
20
30
40
50
60
70
80
90
100
0 30 60 90 120 150
%Conversionofhexanol
Time(min)
5mg 10mg 15mg 20mg
_
Speed of
agitation
300RPM
Temp. 50 ºC
Solvent toluene
hexanol:vinyl
acetate
1:2
Reaction parameter
38
Effect of temperature
0
10
20
30
40
50
60
70
80
90
100
0 30 60 90 120 150
%Conversionofhexanol
Time (min)
30ºC 40ºC 50ºC
_
Speed of
agitation
300RPM
Enzyme loaded
MCF
20mg
Solvent toluene
hexanol:vinyl
acetate
1:2
Reaction parameter
39
y = 0.0027x
R2 = 0.9976
y = 0.0065x
R2 = 0.9855
y = 0.0098x
R2 = 0.994
0
0.2
0.4
0.6
0.8
1
1.2
1.4
0 30 60 90 120 150
ln((2-Xa)/2*(1-Xa))
Time (min)
30ºC 40ºC 50ºC
Second order plot_
40
-6
-5.5
-5
-4.5
-4
-3.5
-3
0.00305 0.0031 0.00315 0.0032 0.00325 0.0033 0.00335
ln(k)
1/T×103 (1/K)
Arrhenius plot
Activation energy
= 52.6KJ/mol
=12.58Kcal/mol
_
41
Effect of mole ratio
0
10
20
30
40
50
60
70
80
90
100
0 30 60 90 120 150
%Conversionofhexanol
Time (min)
1:01 1:05 1:02 01:02.5 1:03
_
Speed of
agitation
300RPM
Enzyme loaded
MCF
20mg
Solvent toluene
Temp. 40ºC
Reaction parameter
42
Substrate study
0.00E+00
1.00E-05
2.00E-05
3.00E-05
4.00E-05
5.00E-05
6.00E-05
7.00E-05
8.00E-05
9.00E-05
1.00E-04
Initialrate(mols/lit.min)
Mole:ratio (hexanol:vinyl acetate)
_
Speed of
agitation
300RPM
Enzyme loaded
MCF
20mg
Solvent toluene
Temp. 50ºC
Reaction parameter
43
0.00E+00
1.00E+04
2.00E+04
3.00E+04
4.00E+04
5.00E+04
6.00E+04
7.00E+04
8.00E+04
0 0.05 0.1 0.15 0.2
1/[initialrate]
1/[vinyl acetate]
5mM 15mM 20mM 10mM
Lineweaver-Burk plot
44
Parameters Values refined by polymath
Vmax (mol/lit.min)
0.00057
KmA (mol/lit)
0.065
KmB (mol/lit)
0.533
KiA (mol/lit)
0.083
Ki
B 0.013
Kinetic parameters
45
• MCF is the best support for enzyme immobilization
• Gluteraldehyde cross-linking method II (ship-in-a-bottle-
approach) is the best method for lipase immobilization
• Selective biocatalyst for hexyl acetate synthesis
• Economic process as compared to other reported
methods
46
Future plan………
• Functionalization of MCF for effective immobilization
of Enzyme
• Enhancement of thermo stability of enzyme by
immobilization method
• Carry out reactions with packed bed reactor
• Synthesis of chiral MCF
47
• Prof. G. D. Yadav
• Prof. A. M. Lali
• DBT Govt. of India
• Novo Nordisk
• Dr. Reddy’s lab.
• Chem. Engg. Dept. ICT, Mumbai
• Lab mates
Acknowledgm
ent
48
Thank You !

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Shrinivas colloquium 18_06_10

  • 1. Enzymatic Catalysis in Synthesis of fine Chemicals Research supervisor Research student Prof. G.D.Yadav Shrinivas A. Shete
  • 2. _ • Synthesis of novel support • Characterization of support • Immobilization of lipase • Characterization of biocatalyst • Synthesis of hexyl acetate Outline of project 2
  • 3. Classification of catalysis_ Catalysis Bio- Chemo- Organo - Inorganic Organo metalic Enzyme 3
  • 4. Biocatalysis can be either homogeneous or heterogeneous Homogeneous Heterogeneous Chemo- catalysis Bio- catalysis Organo Metalic Organic compounds Acids and bases Free enzyme Inorganic solids Organic resins Immobilized enzymes Whole cells _ 4
  • 5.  Stability in organic solvents  Mild reaction conditions  Do not require cofactors  Eco friendly catalyst  Higher reaction rates  Possess broad substrate specificity  Exhibit high enantioselectivity Lipase (3.1.1.3)_ Lipase can be employed in the production of pharmaceuticals, cosmetics, leather, detergents, foods, perfumery and other organic synthetic materials. 5
  • 6. They are soluble catalysts Usually very unstable They may be strongly inhibited by substrates and products work well on natural substrates and under physiologica l conditions High cost Limitations of enzyme in addition to their excellent catalytic properties _ 6
  • 7. Engineering of enzymes from biological to chemical industry • Screening of enzymes with suitable properties • Improvement of enzyme properties via techniques of molecular biology • improvement of enzyme properties via reaction and reactor engineering _ •Improvement of enzyme properties via immobilization 7
  • 8. Development of Biocatalyst • Factors to be considered in design of a biocatalyst. A Reuse of Enzyme B Immobilization method C Enzyme stability _ Cost effectiveness & Simplicity D Development of Biocatalyst_ 8
  • 9. Support for enzyme immobilization Support Natural Synthetic Inorganic 1. cellulose 2. dextran 3. agar 4. chitin 1. polyacrylate 2. polymethacrylates 3. polyacrylamide 1. silica 2. bentonite 3. glass _ 9
  • 11. Mesocellular foam [MCF]_ B High pore volume, up to 2 ml/g Large surface area, up to 1,000 m2/g C A 3D pore system A Connected by uniform windows (9-22 nm) D Large spherical cells (24-42 nm) 11
  • 12. P123-4g + H2O-65ml + HCl-10ml Stir at 40 ºC for 2 hours Static at 40 ºC for 20 hours Age at 100 ºC for 24 hours Filter, dry & Calcination at 550 ºC for 6 hours TMB TEOS NH4F Synthesis of MCF_
  • 13. Characterization of MCF_ 1. FT-IR 2. ASAP 3. SEM 13
  • 14. 4000.0 3000 2000 1500 1000 400.0 -1.5 5 10 15 20 25 30 35 40 45 50 55 61.9 cm-1 %T 3465.76 1652.48 1086.56 972.84 804.97 462.88 FT-IR of MCF_ 14
  • 16. Silica Surface Area (m2/g) Pore volume (cm3/g) Pore size (nm)Single Point BET BJH Adsorption BJH Desorption Single point BJH Adsorption BJH Desorption MCF 431.74 447.79 471.62 739.11 1.92 1.90 1.93 17.19 ASAP results_ 16
  • 19. Methods of enzyme immobilization Methods Adsorption Entrapment Micro- encapsulation Entrapment Cross linking Covalent binding _ 19
  • 20. Total protein estimation y= 0.026x R² =0.998 0 0.05 0.1 0.15 0.2 0.25 0.3 0 2 4 6 8 10 12 Absorbance Microgram of Protein/100ul BradfordCalibrationCurve(Microassay) Bradford Calibration Curve (Macroassay) y = 0.007x R2 = 0.9912 0 0.1 0.2 0.3 0.4 0.5 0.6 0.7 0.8 0 20 40 60 80 100 120 micro gram protein/100ul absorbance _ 20
  • 21. Olive oil Tributy rin P-nitro phenol Lipase assay_ Various assay methods are used to determine the enzyme activity.
  • 22. Tributyrin method_ 188µl tributyrin + 1062µl of 0.1M phosphate buffer + 250µl enzyme Mix thoroughly on cyclomixer for 1 min Kept on shaker for 14 min Released acid titrated with 0.05N NaOH 22
  • 23. 0.2 g of Calcined MCF + 20 ml ethanol Appropriate amount of APTES Mixture reflux for 850C for 8 h. Wash with DI water & ethanol Filter white solid & Dry at 600C for 24 h Covalent binding Functionalization with APTES _ 23
  • 24. Procedure_ 300mg FMCF + 10ml sod. phosphate buffer. equilibration for 1 hour 10ml of 0.1% gluteraldehyde soln Kept in shaker for 1 hr at room temp Add. of diluted enzyme Washed three times with buffer Protein content & enzyme activity was checked Kept in shaker for 6 hr at room temp 24
  • 26. 300mg MCF + 10ml sod. phosphate buffer. equilibration for 1 hour 10ml enzyme solution Gluteraldehyde crosslinking method - I_ 300mg MCF 10ml phosphate buffer Kept it for 1hr in incubator shaker 0.1% of Gluteraldehyde solution Stirred at 4ºC overnight Centrifugation & washing with buffer 26
  • 27. Immobilization Method Dilution % Immobilization Activity u/g Gluteraldehyde ( Method I ) 10 78 222 100 79 82 1000 100 24 Gluteraldehyde crosslinking method – I results_ 27
  • 28. Gluteraldehyde crosslinking method – II_ 300mg MCF 10ml sod. Phosphate buffer 300mg MCF + 10ml sod. phosphate buffer. equilibration for 1 hour 10ml enzyme solution Vortexed for 30 sec & then sonicated for 10sec Kept on shaker for 30min 0.1% gluteraldehyde sol. Kept on shaker for 30min Centrifugation & washing with buffer 28
  • 29. Immobilization Method Dilution % Immobilization Activity u/g Gluteraldehyd e ( Method I ) 10 97 333 100 99 198 1000 100 75 Gluteraldehyde crosslinking method – II results _ 29
  • 30. Comparison of results of immobilization methods 0 50 100 150 200 250 300 350 Gluteraldehyde I Gluteraldehyde II Covalant bonding Immobilization methods Enzymeactivityu/g 10 100 1000 _ 30
  • 31. 31
  • 32. Reaction scheme_ CH3 OH + CH2 O O CH3 CH3 O O CH3 + CH2 OH CH3 O vinyl alcohol vinyl acetate hexanol hexyl acetate acetaldehyde Lipase Hexylacetate is a significant green note flavor and widely used in food industry.32
  • 33. ……..Experi mental Gas Chromatography Contd... water bath hexanol + vinyl acetate + biocatalyst in organic solvent t0…………….t1………….tn glass reactor pitched blade glass stirrer
  • 35. Effect of acyl donors 0 10 20 30 40 50 60 70 80 90 100 0 30 60 90 120 150 %conversionofhexanol Time (min) vinyl acetate acetic anhydride acetic acid triacetin _ Reaction parameter Speed of agitation 300RPM Temp. 50 ºC Solvent Toluene Enzyme loaded MCF 20mg hexanol:acyl donar 1:2 35
  • 36. Effect of speed of agitation 0 10 20 30 40 50 60 70 80 90 100 0 30 60 90 120 150 %Conversionofhexanol Time ( min ) 200 RPM 300 RPM 400 RPM 500 RPM _ Temp. 50 ºC Solvent Toluene Enzyme loaded MCF 20mg hexanol:vinyl acetate 1:2 Reaction parameter 36
  • 37. Effect of solvents 0 10 20 30 40 50 60 70 80 90 100 0 30 60 90 120 150 %ConversionofHexanol Time (min) Toluene Benzene 1,4 Dioxane Acetonitrile _ Reaction parameter Speed of agitation 300RPM Temp. 50 ºC Enzyme loaded MCF 20mg hexanol:vinyl acetate 1:2 37
  • 38. Effect of catalyst loading 0 10 20 30 40 50 60 70 80 90 100 0 30 60 90 120 150 %Conversionofhexanol Time(min) 5mg 10mg 15mg 20mg _ Speed of agitation 300RPM Temp. 50 ºC Solvent toluene hexanol:vinyl acetate 1:2 Reaction parameter 38
  • 39. Effect of temperature 0 10 20 30 40 50 60 70 80 90 100 0 30 60 90 120 150 %Conversionofhexanol Time (min) 30ºC 40ºC 50ºC _ Speed of agitation 300RPM Enzyme loaded MCF 20mg Solvent toluene hexanol:vinyl acetate 1:2 Reaction parameter 39
  • 40. y = 0.0027x R2 = 0.9976 y = 0.0065x R2 = 0.9855 y = 0.0098x R2 = 0.994 0 0.2 0.4 0.6 0.8 1 1.2 1.4 0 30 60 90 120 150 ln((2-Xa)/2*(1-Xa)) Time (min) 30ºC 40ºC 50ºC Second order plot_ 40
  • 41. -6 -5.5 -5 -4.5 -4 -3.5 -3 0.00305 0.0031 0.00315 0.0032 0.00325 0.0033 0.00335 ln(k) 1/T×103 (1/K) Arrhenius plot Activation energy = 52.6KJ/mol =12.58Kcal/mol _ 41
  • 42. Effect of mole ratio 0 10 20 30 40 50 60 70 80 90 100 0 30 60 90 120 150 %Conversionofhexanol Time (min) 1:01 1:05 1:02 01:02.5 1:03 _ Speed of agitation 300RPM Enzyme loaded MCF 20mg Solvent toluene Temp. 40ºC Reaction parameter 42
  • 43. Substrate study 0.00E+00 1.00E-05 2.00E-05 3.00E-05 4.00E-05 5.00E-05 6.00E-05 7.00E-05 8.00E-05 9.00E-05 1.00E-04 Initialrate(mols/lit.min) Mole:ratio (hexanol:vinyl acetate) _ Speed of agitation 300RPM Enzyme loaded MCF 20mg Solvent toluene Temp. 50ºC Reaction parameter 43
  • 44. 0.00E+00 1.00E+04 2.00E+04 3.00E+04 4.00E+04 5.00E+04 6.00E+04 7.00E+04 8.00E+04 0 0.05 0.1 0.15 0.2 1/[initialrate] 1/[vinyl acetate] 5mM 15mM 20mM 10mM Lineweaver-Burk plot 44
  • 45. Parameters Values refined by polymath Vmax (mol/lit.min) 0.00057 KmA (mol/lit) 0.065 KmB (mol/lit) 0.533 KiA (mol/lit) 0.083 Ki B 0.013 Kinetic parameters 45
  • 46. • MCF is the best support for enzyme immobilization • Gluteraldehyde cross-linking method II (ship-in-a-bottle- approach) is the best method for lipase immobilization • Selective biocatalyst for hexyl acetate synthesis • Economic process as compared to other reported methods 46
  • 47. Future plan……… • Functionalization of MCF for effective immobilization of Enzyme • Enhancement of thermo stability of enzyme by immobilization method • Carry out reactions with packed bed reactor • Synthesis of chiral MCF 47
  • 48. • Prof. G. D. Yadav • Prof. A. M. Lali • DBT Govt. of India • Novo Nordisk • Dr. Reddy’s lab. • Chem. Engg. Dept. ICT, Mumbai • Lab mates Acknowledgm ent 48