1/16/2009 epoxidationof allyl etherschemistry.unpad.ac.id/isc-proceeding/2008/pdf/pl ppt/mircea...
TRANSCRIPT
EPOXIDATION OF ALLYL ETHERS
1/16/2009
Mirce
a M
anea
Mircea Manea
Mirce
a M
anea
1
CYCLIC ETHERS
1/16/2009
Mirce
a M
anea
2
CYCLIC ETHERS IN NATURE
1/16/2009
Mirce
a M
anea
� Vernonia oil
3
� Oxylipins are know in nature.
� Some plants such as Vernonia galamentis and Euphoria lagascae produce about 60% vernolic acid in the seed oil.
CYCLIC ETHERS IN NATURE
1/16/2009
Mirce
a M
anea
� Paclitaxel
O
O
O
OH
NH OO
O
4
� extract from the rare Pacific
yew tree Taxus brevifolia.
OOO
O
HO
OH
O
EPOXY APPLICATIONS
1/16/2009
Mirce
a M
anea
5
EPOXY RESINS
� DeTrey Frères produced in 1936, a low melting
bisphenol A-based epoxy resin that gave a
thermoset composition with phthalic anhydride.
� 1946 the first epoxy adhesive was shown at the
Swiss Industries Fair
1/16/2009
Mirce
a M
anea
Swiss Industries Fair
� First commercial high solids epoxy systems in
1950s (Pittsburgh Coke & Chemical).The coating
exhibited an increased water resistance, thermal
plasticity, durability and corrosion resistance.
6
EPOXY MARKET SITUATION 2006
1/16/2009
Mirce
a M
anea
7
THE WORKING HORSES
� Cross-linked with amines /
poly(amido-amines) and
anhydrides
1/16/2009
Mirce
a M
anea
8
� Cross-linked with polyacids
THE WORKING HORSES IN POWDER
COATINGS
1/16/2009
Mirce
a M
anea
N
N
N
O
O
O
O
O
O
9
(TGIC)1,3,5-tris(oxiran-2-ylmethyl)-1,3,5-triazinane-2,4,6-trione
O OO
OH
O
O
O
REACTIVE SOLVENTS (MONOFUNCTIONAL)
1/16/2009
Mirce
a M
anea
10
REACTIVE SOLVENTS (POLYFUNCTIONAL)
1/16/2009
Mirce
a M
anea
11
PURPOSE
� Manufacturing of glycidyl ethers avoiding the use
of epichlorhydrine
1/16/2009
Mirce
a M
anea
12
OPTIONS
� Chemical oxidation via Prileshajev
� Chemo-enzymatic oxidation
1/16/2009
Mirce
a M
anea
13
CHEMICAL OXIDATION VIA
PRILESHAJEV
1/16/2009
Mirce
a M
anea
14
CHEMO-ENZYMATIC OXIDATION
� Lipase, H2O2, Carboxylic acid
1/16/2009
Mirce
a M
anea
15
THE NATURE OF THE ALLYL ETHER
1/16/2009
Mirce
a M
anea
� TMPME � TMPDE
� TMPTE
Water soluble Organic solvent soluble
16
HO O
O
O O
O
CHEMO-ENZYMATIC EPOXIDATION OF
TMPME
� Novozym 435
� Carboxylic acid
� Solvent
� TMPME
Internal standard: hexadecane
1/16/2009
Mirce
a M
anea
� Internal standard: hexadecane
17
STABILITY OF THE GLYCIDYL ETHER
� In situ generated peracid
� Reaction temperature
50ºC
� Allyl group completely
consumed
1/16/2009
Mirce
a M
anea
20
30
Concentration (mM)
� No glycidyl group detected
at the end
� Acid catalyzed hydrolysis
of the glycidyl group
18
0
10
20
0 12 24 36
Time (h)
Concentration (mM)
20mM/50ºC
DEGRADATION PROFILE OF THE
GLYCIDYL ETHER IN DIFFERENT
SOLUTIONS
� (◊◊◊◊) water,
� (o) mono sodium
phosphate
solution, pH 4,
� (x) phosphate
1/16/2009
Mirce
a M
anea
100
120
140
160
Norm
alised G
C-area
� (x) phosphate
buffer, pH 7,
� (∆∆∆∆) tri-sodium
phosphate
solution, pH 14,
� (□) acetone
19
0
20
40
60
80
100
0 12 24 36 48
Time (h)
Norm
alised G
C-area
RESIDUAL CONCENTRATION OF PEROXY ACID
AND FORMATION OF THE GLYCIDYL ETHER
DURING EPOXIDATION OF TMPME
� (◊) spontaneous degradation (in the absence of TMPME) of preformed palmitic peracid at 50 ºC
� (□) conversion of the palmitic
1/16/2009
Mirce
a M
anea
60
70
� (□) conversion of the palmiticperacid during epoxidation of TMPME
� (x) palmitic peracid consumed during epoxidation (excluding spontaneous degradation)
� (∆) concentration of the epoxide product formed during reaction
� Solvent= toluene
200
10
20
30
40
50
60
0 6 12 18 24 30 36
Time (h)
Concentration (mmol/L)
FORMATION OF PEROXY PALMITIC ACID
CATALYSED BY NOVOZYM® 435 IN TOLUENE
� (◊)25ºC
� (□) 50 ºC
1/16/2009
Mirce
a M
anea
20
25
30Conversion to peracid (%)
21
0
5
10
15
20
0 1 2 3 4 5 6
Time (h)
Conversion to peracid (%)
1
2
3
4
5
6
Form
ation rate (mM/m
in)
INITIAL RATE OF PERACID FORMATION VS
CARBOXYLIC ACID CONCENTRATION AT 30ºC/50ºC
1/16/2009
Mirce
a M
anea
0.000.050.100.150.200.250.300.350.400.450.500.550.600.65
Peracid concentration (M)
0.00 0.25 0.50 0.75 1.00 1.250
Concentration (M)
Form
ation rate (mM/m
in)
+ Caprylic acid
∆ Lauric acid
30 % H2O2 (19.6 mmol)
22
0 1 2 3 4 5 6 70.000.05
Concentration of acid (M)
Peracid concentration (M)
30ºC 50ºC
0.75
1.00
1.25
C Peracid (M)
PERACID FORMATION FROM CAPRYLIC ACID
AT VARYING H2O2 CONCENTRATIONS
� (x) 50%
� (□) 40%
� (∆) 30%
� (o) 20%
(+)10%
1/16/2009
Mirce
a M
anea
0 1 2 3 4 5 60.00
0.25
0.50
Time (h)
C Peracid (M)
90 % caprylic acid in toluene, 25 °C
� (+)10%
23
PERACID FORMATION FROM
DIFFERENT CARBOXYLIC ACIDS
� (+)
Caprylic
acid, C8,
mp 16.3 °C
� (∆) Lauric
1/16/2009
Mirce
a M
anea0.075
0.100
0.125
Peracid concentration (M)
� (∆) Lauric
acid, C12,
mp 45 °C
� (X)
Palmitic
acid, C16,
63 °C24
0 25 50 75 100 125 150 1750.000
0.025
0.050
0.075
Time (min)
Peracid concentration (M)
0.6 mmol carboxylic acid + 9.8 mmol H2O2
0.3
0.4
0.5
0.6
C Epoxide (M)
Ex situ peracid generation
Yield: 75 %
EPOXIDATION OF TMPME
1/16/2009
Mirce
a M
anea
0 2 4 6 8 10 120.0
0.1
0.2
0.3
Time (h)
C Epoxide (M)
In situ peracid generation
(5.7 M caprylic acid, 18 mmol H2O2, 50 °C) 25
PROCESS
1/16/2009
Mirce
a M
anea
26
Hydrogen peroxide
(Solvent)
Carboxylic acid
Enzyme
(Solvent)
Carboxylic acid
Hydrogen peroxide
Enzyme
Allyl ether
(Solvent)
Peracid
CHEMO-ENZYMATIC EPOXIDATION OF
TMPME
� Two stage process
� Reaction temperature
50ºC
� Allyl group consumed
� Glycidyl group
1/16/2009
Mirce
a M
anea
20
30
Concentration (mM)
� Glycidyl group
generated
correspondingly
27
0
10
0 12 24 36
Time (h)
Concentration (mM)
0.3
0.4
0.5
0.6
Concentration of epoxide (M)
Yield: 75 %
EPOXIDATION OF TMPTE
� (5.7 M
caprylic
acid, 18
mmol
H2O2, 50
1/16/2009
Mirce
a M
anea
0 2 4 6 8 10 120.0
0.1
0.2
0.3
Time (h)
Concentration of epoxide (M)
H2O2, 50
°C)
28
EPOXIDATION OF DIFFERENT ALLYL
ETHERS
1/16/2009
Mirce
a M
anea
Starting material Concentration Yield*
100 mg/ml 80 %OOH
OH
29
100 mg/ml 80 %
100 mg/ml 100 %
100 mg/ml 60 %O
O
O
O
O
O
m
n
p
m+n+p=7
O
O
O
O
3
* By titration (approximate values)
CONCLUSIONS
1/16/2009
Mirce
a M
anea
� Shorter acid does good
� Many allyl ether may be converted
� Aromatic
� Good
� Aliphatic
� Bad
Carboxylic acids Solvents
• 1 step reaction– Low yields
– Low concentrations
– Water degrades
Process
30
may be converted
� Different solvents may be used
� Higher peracidconcentration does good
� Bad
� No solvent
� Very good
– Water degrades epoxide
• 2 steps reaction– Water excluded
– Low concentrations
– Good yields
INTERESTING SPINOFF
1/16/2009
Mirce
a M
anea
31
INTERESTING SPINOFF
1/16/2009
Mirce
a M
anea
32
ACKNOWLEDGMENTS
University of Lund
Alkindo Mitraraya
Perstorp
� Rajni-Hatti-Kaul
� Pär Tufvesson
� Dietlind Adlercreutz
� Sugianto Effendi
� Keith Ogemark
1/16/2009
Mirce
a M
anea
33